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1

Life Cycle Analysis: Integrated Gasification Combined Cycle (IGCC) Power Plant  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Life Cycle Analysis: Integrated Life Cycle Analysis: Integrated Gasification Combined Cycle (IGCC) Power Plant Revision 2, March 2012 DOE/NETL-2012/1551 Disclaimer This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference therein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or

2

Model Predictive Control of Integrated Gasification Combined Cycle Power Plants  

SciTech Connect (OSTI)

The primary project objectives were to understand how the process design of an integrated gasification combined cycle (IGCC) power plant affects the dynamic operability and controllability of the process. Steady-state and dynamic simulation models were developed to predict the process behavior during typical transients that occur in plant operation. Advanced control strategies were developed to improve the ability of the process to follow changes in the power load demand, and to improve performance during transitions between power levels. Another objective of the proposed work was to educate graduate and undergraduate students in the application of process systems and control to coal technology. Educational materials were developed for use in engineering courses to further broaden this exposure to many students. ASPENTECH software was used to perform steady-state and dynamic simulations of an IGCC power plant. Linear systems analysis techniques were used to assess the steady-state and dynamic operability of the power plant under various plant operating conditions. Model predictive control (MPC) strategies were developed to improve the dynamic operation of the power plants. MATLAB and SIMULINK software were used for systems analysis and control system design, and the SIMULINK functionality in ASPEN DYNAMICS was used to test the control strategies on the simulated process. Project funds were used to support a Ph.D. student to receive education and training in coal technology and the application of modeling and simulation techniques.

B. Wayne Bequette; Priyadarshi Mahapatra

2010-08-31T23:59:59.000Z

3

An update technology for integrated biomass gasification combined cycle power plant  

Science Journals Connector (OSTI)

A discussion is presented on the technical analysis of a 6.4 MWe integrated biomass gasification combined cycle (IBGCC) plant. It features three numbers ... producing 5.85 MW electrical power in open cycle and 55...

Paritosh Bhattacharya; Suman Dey

2014-01-01T23:59:59.000Z

4

Biomass Gasification Combined Cycle  

SciTech Connect (OSTI)

Gasification combined cycle continues to represent an important defining technology area for the forest products industry. The ''Forest Products Gasification Initiative'', organized under the Industry's Agenda 2020 technology vision and supported by the DOE ''Industries of the Future'' program, is well positioned to guide these technologies to commercial success within a five-to ten-year timeframe given supportive federal budgets and public policy. Commercial success will result in significant environmental and renewable energy goals that are shared by the Industry and the Nation. The Battelle/FERCO LIVG technology, which is the technology of choice for the application reported here, remains of high interest due to characteristics that make it well suited for integration with the infrastructure of a pulp production facility. The capital cost, operating economics and long-term demonstration of this technology area key input to future economically sustainable projects and must be verified by the 200 BDT/day demonstration facility currently operating in Burlington, Vermont. The New Bern application that was the initial objective of this project is not currently economically viable and will not be implemented at this time due to several changes at and around the mill which have occurred since the inception of the project in 1995. The analysis shows that for this technology, and likely other gasification technologies as well, the first few installations will require unique circumstances, or supportive public policies, or both to attract host sites and investors.

Judith A. Kieffer

2000-07-01T23:59:59.000Z

5

Catalytic combustor for integrated gasification combined cycle power plant  

DOE Patents [OSTI]

A gasification power plant 10 includes a compressor 32 producing a compressed air flow 36, an air separation unit 22 producing a nitrogen flow 44, a gasifier 14 producing a primary fuel flow 28 and a secondary fuel source 60 providing a secondary fuel flow 62 The plant also includes a catalytic combustor 12 combining the nitrogen flow and a combustor portion 38 of the compressed air flow to form a diluted air flow 39 and combining at least one of the primary fuel flow and secondary fuel flow and a mixer portion 78 of the diluted air flow to produce a combustible mixture 80. A catalytic element 64 of the combustor 12 separately receives the combustible mixture and a backside cooling portion 84 of the diluted air flow and allows the mixture and the heated flow to produce a hot combustion gas 46 provided to a turbine 48. When fueled with the secondary fuel flow, nitrogen is not combined with the combustor portion.

Bachovchin, Dennis M. (Mauldin, SC); Lippert, Thomas E. (Murrysville, PA)

2008-12-16T23:59:59.000Z

6

Method and system to estimate variables in an integrated gasification combined cycle (IGCC) plant  

DOE Patents [OSTI]

System and method to estimate variables in an integrated gasification combined cycle (IGCC) plant are provided. The system includes a sensor suite to measure respective plant input and output variables. An extended Kalman filter (EKF) receives sensed plant input variables and includes a dynamic model to generate a plurality of plant state estimates and a covariance matrix for the state estimates. A preemptive-constraining processor is configured to preemptively constrain the state estimates and covariance matrix to be free of constraint violations. A measurement-correction processor may be configured to correct constrained state estimates and a constrained covariance matrix based on processing of sensed plant output variables. The measurement-correction processor is coupled to update the dynamic model with corrected state estimates and a corrected covariance matrix. The updated dynamic model may be configured to estimate values for at least one plant variable not originally sensed by the sensor suite.

Kumar, Aditya; Shi, Ruijie; Dokucu, Mustafa

2013-09-17T23:59:59.000Z

7

Feasibility Studies to Improve Plant Availability and Reduce Total Installed Cost in Integrated Gasification Combined Cycle Plants  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Feasibility Studies to Improve Plant Feasibility Studies to Improve Plant Availability and Reduce Total Installed Cost in Integrated Gasification Combined Cycle Plants Background Gasification provides the means to turn coal and other carbonaceous solid, liquid and gaseous feedstocks as diverse as refinery residues, biomass, and black liquor into synthesis gas and valuable byproducts that can be used to produce low-emissions power, clean-burning fuels and a wide range of commercial products to support

8

Is Integrated Gasification Combined Cycle with Carbon Capture-Storage the Solution for Conventional Coal Power Plants  

E-Print Network [OSTI]

Engineering Management Field Project Is Integrated Gasification Combined Cycle with Carbon Capture-Storage the Solution for Conventional Coal Power Plants By Manish Kundi Fall Semester, 2011 An EMGT Field Project report... 2.4 Environmental Aspects-Emissions 23 3.0 Procedure & Methodology 3.1 Working technology – Conventional Coal Plants 30 3.2 Working technology – IGCC Power Plants 32 3.3 Carbon Capture and Storage 35 3...

Kundi, Manish

2011-12-16T23:59:59.000Z

9

CoalFleet RD&D augmentation plan for integrated gasification combined cycle (IGCC) power plants  

SciTech Connect (OSTI)

To help accelerate the development, demonstration, and market introduction of integrated gasification combined cycle (IGCC) and other clean coal technologies, EPRI formed the CoalFleet for Tomorrow initiative, which facilitates collaborative research by more than 50 organizations from around the world representing power generators, equipment suppliers and engineering design and construction firms, the U.S. Department of Energy, and others. This group advised EPRI as it evaluated more than 120 coal-gasification-related research projects worldwide to identify gaps or critical-path activities where additional resources and expertise could hasten the market introduction of IGCC advances. The resulting 'IGCC RD&D Augmentation Plan' describes such opportunities and how they could be addressed, for both IGCC plants to be built in the near term (by 2012-15) and over the longer term (2015-25), when demand for new electric generating capacity is expected to soar. For the near term, EPRI recommends 19 projects that could reduce the levelized cost-of-electricity for IGCC to the level of today's conventional pulverized-coal power plants with supercritical steam conditions and state-of-the-art environmental controls. For the long term, EPRI's recommended projects could reduce the levelized cost of an IGCC plant capturing 90% of the CO{sub 2} produced from the carbon in coal (for safe storage away from the atmosphere) to the level of today's IGCC plants without CO{sub 2} capture. EPRI's CoalFleet for Tomorrow program is also preparing a companion RD&D augmentation plan for advanced-combustion-based (i.e., non-gasification) clean coal technologies (Report 1013221). 7 refs., 30 figs., 29 tabs., 4 apps.

NONE

2007-01-15T23:59:59.000Z

10

Avestar® - Integrated Gasification Combined Cycle (IGCC) Dynamic Simulator  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Integrated Gasification Combined Cycle (IGCC) Dynamic Simulator Integrated Gasification Combined Cycle (IGCC) Dynamic Simulator The AVESTAR® center offers courses using the Integrated Gasification Combined Cycle (IGCC) Dynamic Simulator. The IGCC simulator builds on and reaches beyond existing combined-cycle and conventional-coal power plant simulators to combine--for the first time--a Gasification with CO2 Capture process simulator with a Combined-Cycle power simulator together in a single dynamic simulation framework. The AVESTAR® center IGCC courses provide unique, comprehensive training on all aspects of an IGCC plant, illustrating the high-efficiency aspects of the gasifier, gas turbine, and steam turbine integration. IGCC Operator training station HMI display for overview of IGCC Plant - Train A Reference:

11

Studies of the thermal circuit of an advanced integrated gasification combined-cycle power plant  

Science Journals Connector (OSTI)

The results obtained from a study of the thermal circuit of a combined-cycle plant with coal gasification are presented, and ... of producer gas and calculated values of the combined-cycle power plant efficiency ...

D. G. Grigoruk; A. V. Turkin

2010-02-01T23:59:59.000Z

12

Off-Design Performance of Power Plants: An Integrated Gasification Combined-Cycle Example  

Science Journals Connector (OSTI)

...that of a normal natural gas-fired combined-cycle...for operation in the natural gas-fired combined-cycle...inlet flow around the high-pressure section of the turbine...when converting from natural gas firing to IGCC opera-tion...

M. R. ERBES; J. N. PHILLIPS; M. S. JOHNSON; J. PAFFENBARGER; M. GLUCKMAN; R. H. EUSTIS

1987-07-24T23:59:59.000Z

13

Technoeconomic Analysis and Life Cycle Assessment of an Integrated Biomass Gasification Combined Cycle System  

Science Journals Connector (OSTI)

A biomass gasification combined-cycle power plant, consisting of a low pressure...®...Economic analyses were then performed to determine the levelized cost of electricity. The economic viability and efficiency of...

M. K. Mann; P. L. Spath

1997-01-01T23:59:59.000Z

14

Modeling and Optimization of Membrane Reactors for Carbon Capture in Integrated Gasification Combined Cycle Units  

Science Journals Connector (OSTI)

Modeling and Optimization of Membrane Reactors for Carbon Capture in Integrated Gasification Combined Cycle Units ... This paper investigates the alternative of precombustion capture of carbon dioxide from integrated gasification combined cycle (IGCC) plants using membrane reactors equipped with H2-selective zeolite membranes for the water gas shift reaction. ...

Fernando V. Lima; Prodromos Daoutidis; Michael Tsapatsis; John J. Marano

2012-03-08T23:59:59.000Z

15

"Integrated Gasification Combined Cycle"  

U.S. Energy Information Administration (EIA) Indexed Site

Status of technologies and components modeled by EIA" Status of technologies and components modeled by EIA" ,"Revolutionary","Evolutionary","Mature" "Pulverized Coal",,,"X" "Pulverized Coal with CCS" " - Non-CCS portion of Pulverized Coal Plant",,,"X" " - CCS","X" "Integrated Gasification Combined Cycle" " - Advanced Combustion Turbine",,"X" " - Heat Recovery Steam Generator",,,"X" " - Gasifier",,"X" " - Balance of Plant",,,"X" "Conventional Natural Gas Combined Cycle" " - Conventional Combustion Turbine",,,"X" " - Heat Recovery Steam Generator",,,"X" " - Balance of Plant",,,"X"

16

Integration of coal utilization and environmental control in integrated gasification combined cycle systems  

Science Journals Connector (OSTI)

Integration of coal utilization and environmental control in integrated gasification combined cycle systems ... The Cost of Carbon Capture and Storage for Natural Gas Combined Cycle Power Plants ... The Cost of Carbon Capture and Storage for Natural Gas Combined Cycle Power Plants ...

H. Christopher Frey; Edward S. Rubin

1992-10-01T23:59:59.000Z

17

EIS-0409: Kemper County Integrated Gasification Combined Cycle Project, Mississippi  

Broader source: Energy.gov [DOE]

This EIS analyzes DOE's decision to provide funding for the Kemper County Integrated Gasification Combined Cycle Project in Kemper County, Mississippi to assess the potential environmental impacts associated with the construction and operation of a project proposed by Southern Power Company, through its affiliate Mississippi Power Company, which has been selected by DOE for consideration under the Clean Coal Power Initiative (CCPI) program.

18

An evaluation of integrated-gasification-combined-cycle and pulverized-coal-fired steam plants: Volume 1, Base case studies: Final report  

SciTech Connect (OSTI)

An evaluation of the performance and costs for a Texaco-based integrated gasification combined cycle (IGCC) power plant as compared to a conventional pulverized coal-fired steam (PCFS) power plant with flue gas desulfurization (FGD) is provided. A general set of groundrules was used within which each plant design was optimized. The study incorporated numerous sensitivity cases along with up-to-date operating and cost data obtained through participation of equipment vendors and process developers. Consequently, the IGCC designs presented in this study use the most recent data available from Texaco's ongoing international coal gasification development program and General Electric's continuing gas turbine development efforts. The Texaco-based IGCC has advantages over the conventional PCFS technology with regard to environmental emissions and natural resource requirements. SO/sub 2/, NOx, and particulate emissions are lower. Land area and water requirements are less for IGCC concepts. Coal consumption is less due to the higher plant thermal efficiency attainable in the IGCC plant. The IGCC plant also has the capability to be designed in several different configurations, with and without the use of natural gas or oil as a backup fuel. This capability may prove to be particularly advantageous in certain utility planning and operation scenarios. 107 figs., 114 tabs.

Pietruszkiewicz, J.; Milkavich, R.J.; Booras, G.S.; Thomas, G.O.; Doss, H.

1988-09-01T23:59:59.000Z

19

Modeling the Performance, Emissions, and Cost of an Entrained-Flow Gasification Combined Cycle System Using  

E-Print Network [OSTI]

1 Modeling the Performance, Emissions, and Cost of an Entrained-Flow Gasification Combined Cycle-based Integrated Gasification Combined Cycle (IGCC) system using ASPEN. ASPEN is a steady-state chemical process-flow Integrated Gasification Combined Cycle (IGCC) system. This study aims at developing a base case analysis

Frey, H. Christopher

20

Improved System Integration for Integrated Gasification Combined Cycle (IGCC) Systems  

Science Journals Connector (OSTI)

Improved System Integration for Integrated Gasification Combined Cycle (IGCC) Systems ... The model is applied to evaluate integration schemes involving nitrogen injection, air extraction, and combinations of both, as well as different ASU pressure levels. ... The optimal nitrogen injection only case in combination with an elevated pressure ASU had the highest efficiency and power output and approximately the lowest emissions per unit output of all cases considered, and thus is a recommended design option. ...

H. Christopher Frey; Yunhua Zhu

2006-02-02T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


21

Dynamic simulation and load-following control of an integrated gasification combined cycle (IGCC) power plant with CO{sub 2} capture  

SciTech Connect (OSTI)

Load-following control of future integrated gasification combined cycle (IGCC) plants with pre-combustion CO{sub 2} capture is expected to be far more challenging as electricity produced by renewable energy is connected to the grid and strict environmental limits become mandatory requirements. To study control performance during load following, a plant-wide dynamic simulation of a coal-fed IGCC plant with CO{sub 2} capture has been developed. The slurry-fed gasifier is a single-stage, downward-fired, oxygen-blown, entrained-flow type with a radiant syngas cooler (RSC). The syngas from the outlet of the RSC goes to a scrubber followed by a two-stage sour shift process with inter-stage cooling. The acid gas removal (AGR) process is a dual-stage physical solvent-based process for selective removal of H{sub 2}S in the first stage and CO{sub 2} in the second stage. Sulfur is recovered using a Claus unit with tail gas recycle to the AGR. The recovered CO{sub 2} is compressed by a split-shaft multistage compressor and sent for sequestration after being treated in an absorber with triethylene glycol for dehydration. The clean syngas is sent to two advanced “F”-class gas turbines (GTs) partially integrated with an elevated-pressure air separation unit. A subcritical steam cycle is used for heat recovery steam generation. A treatment unit for the sour water strips off the acid gases for utilization in the Claus unit. The steady-state model developed in Aspen Plus® is converted to an Aspen Plus Dynamics® simulation and integrated with MATLAB® for control studies. The results from the plant-wide dynamic model are compared qualitatively with the data from a commercial plant having different configuration, operating condition, and feed quality than what has been considered in this work. For load-following control, the GT-lead with gasifier-follow control strategy is considered. A modified proportional–integral–derivative (PID) control is considered for the syngas pressure control. For maintaining the desired CO{sub 2} capture rate while load-following, a linear model predictive controller (LMPC) is implemented in MATLAB®. A combined process and disturbance model is identified by considering a number of model forms and choosing the final model based on an information-theoretic criterion. The performance of the LMPC is found to be superior to the conventional PID control for maintaining CO{sub 2} capture rates in an IGCC power plant while load following.

Bhattacharyya, D,; Turton, R.; Zitney, S.

2012-01-01T23:59:59.000Z

22

Sensor placement algorithm development to maximize the efficiency of acid gas removal unit for integrated gasification combined cycle (IGCC) power plant with CO{sub 2} capture  

SciTech Connect (OSTI)

Future integrated gasification combined cycle (IGCC) power plants with CO{sub 2} capture will face stricter operational and environmental constraints. Accurate values of relevant states/outputs/disturbances are needed to satisfy these constraints and to maximize the operational efficiency. Unfortunately, a number of these process variables cannot be measured while a number of them can be measured, but have low precision, reliability, or signal-to-noise ratio. In this work, a sensor placement (SP) algorithm is developed for optimal selection of sensor location, number, and type that can maximize the plant efficiency and result in a desired precision of the relevant measured/unmeasured states. In this work, an SP algorithm is developed for an selective, dual-stage Selexol-based acid gas removal (AGR) unit for an IGCC plant with pre-combustion CO{sub 2} capture. A comprehensive nonlinear dynamic model of the AGR unit is developed in Aspen Plus Dynamics® (APD) and used to generate a linear state-space model that is used in the SP algorithm. The SP algorithm is developed with the assumption that an optimal Kalman filter will be implemented in the plant for state and disturbance estimation. The algorithm is developed assuming steady-state Kalman filtering and steady-state operation of the plant. The control system is considered to operate based on the estimated states and thereby, captures the effects of the SP algorithm on the overall plant efficiency. The optimization problem is solved by Genetic Algorithm (GA) considering both linear and nonlinear equality and inequality constraints. Due to the very large number of candidate sets available for sensor placement and because of the long time that it takes to solve the constrained optimization problem that includes more than 1000 states, solution of this problem is computationally expensive. For reducing the computation time, parallel computing is performed using the Distributed Computing Server (DCS®) and the Parallel Computing® toolbox from Mathworks®. In this presentation, we will share our experience in setting up parallel computing using GA in the MATLAB® environment and present the overall approach for achieving higher computational efficiency in this framework.

Paul, P.; Bhattacharyya, D.; Turton, R.; Zitney, S.

2012-01-01T23:59:59.000Z

23

NOVEL GAS CLEANING/ CONDITIONING FOR INTEGRATED GASIFICATION COMBINED CYCLE  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

INTEGRATED GASIFICATION COMBINED CYCLE VOLUME I - CONCEPTUAL COMMERCIAL EVALUATION OPTIONAL PROGRAM FINAL REPORT September 1, 2001 - December 31, 2005 By Dennis A. Horazak (Siemens), Program Manager Richard A. Newby (Siemens) Eugene E. Smeltzer (Siemens) Rachid B. Slimane (GTI) P. Vann Bush (GTI) James L. Aderhold, Jr. (GTI) Bruce G. Bryan (GTI) December 2005 DOE Award Number: DE-AC26-99FT40674 Prepared for U.S. Department of Energy National Energy Technology Laboratory Prepared by Siemens Power Generation, Inc. 4400 Alafaya Trail Orlando, FL 32826 & Gas Technology Institute 1700 S. Mt. Prospect Rd. Des Plaines, Illinois 60018 DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government.

24

Gasification combined cycle: Carbon dioxide recovery, transport, and disposal  

SciTech Connect (OSTI)

The objective of the project is to develop engineering evaluations of technologies for the capture, use, and disposal of carbon dioxide (CO{sub 2}). This project emphasizes CO{sub 2}-capture technologies combined with integrated gasification combined-cycle (IGCC) power systems. Complementary evaluations address CO{sub 2} transportation, CO{sub 2} use, and options for the long-term sequestering of unused CO{sub 2}. Commercially available CO{sub 2}-capture technology is providing a performance and economic baseline against which to compare innovative technologies. The intent is to provide the CO{sub 2} budget, or an {open_quotes}equivalent CO{sub 2}{close_quotes} budget, associated with each of the individual energy-cycle steps, in addition to process design capital and operating costs. The value used for the {open_quotes}equivalent CO{sub 2}{close_quotes} budget is 1 kg of CO{sub 2} per kilowatt-hour (electric). The base case is a 458-MW IGCC system that uses an air-blown Kellogg-Rust-Westinghouse agglomerating fluidized-bed gasifier, Illinois No. 6 bituminous coal feed, and in-bed sulfur removal. Mining, feed preparation, and conversion result in a net electric power production of 454 MW, with a CO{sub 2} release rate of 0.835 kg/kWhe. Two additional life-cycle energy balances for emerging technologies were considered: (1) high-temperature CO{sub 2} separation with calcium- or magnesium-based sorbents, and (2) ambient-temperature facilitated-transport polymer membranes for acid-gas removal.

Doctor, R.D.; Molburg, J.C.; Thimmapuram, P.R.; Berry, G.F.; Livengood, C.D.

1994-09-01T23:59:59.000Z

25

Advanced CO2 Capture Technology for Low Rank Coal Integrated Gasification Combined Cycle (IGCC) Systems  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

CO CO 2 Capture Technology for Low Rank Coal Integrated Gasification Combined Cycle (IGCC) Systems Background Gasification of coal or other solid feedstocks (wood waste, petroleum coke, etc.) is a clean way to produce electricity and produce or co-produce a variety of commercial products. The major challenge is cost reduction; current integrated gasification combined cycle (IGCC) technology is estimated to produce power at a cost higher than that of pulverized coal combustion. However, the Gasification

26

Integrated Gasification Combined Cycle Based on Pressurized Fluidized Bed Gasification  

Science Journals Connector (OSTI)

Enviropower Inc. has developed a modern power plant concept based on an integrated pressurized fluidized bed gasification and gas turbine combined cycle (IGCC)....

Kari Salo; J. G. Patel

1997-01-01T23:59:59.000Z

27

Model predictive control system and method for integrated gasification combined cycle power generation  

SciTech Connect (OSTI)

Control system and method for controlling an integrated gasification combined cycle (IGCC) plant are provided. The system may include a controller coupled to a dynamic model of the plant to process a prediction of plant performance and determine a control strategy for the IGCC plant over a time horizon subject to plant constraints. The control strategy may include control functionality to meet a tracking objective and control functionality to meet an optimization objective. The control strategy may be configured to prioritize the tracking objective over the optimization objective based on a coordinate transformation, such as an orthogonal or quasi-orthogonal projection. A plurality of plant control knobs may be set in accordance with the control strategy to generate a sequence of coordinated multivariable control inputs to meet the tracking objective and the optimization objective subject to the prioritization resulting from the coordinate transformation.

Kumar, Aditya; Shi, Ruijie; Kumar, Rajeeva; Dokucu, Mustafa

2013-04-09T23:59:59.000Z

28

Life cycle assessment of a biomass gasification combined-cycle power system  

SciTech Connect (OSTI)

The potential environmental benefits from biomass power are numerous. However, biomass power may also have some negative effects on the environment. Although the environmental benefits and drawbacks of biomass power have been debated for some time, the total significance has not been assessed. This study serves to answer some of the questions most often raised in regard to biomass power: What are the net CO{sub 2} emissions? What is the energy balance of the integrated system? Which substances are emitted at the highest rates? What parts of the system are responsible for these emissions? To provide answers to these questions, a life cycle assessment (LCA) of a hypothetical biomass power plant located in the Midwest United States was performed. LCA is an analytical tool for quantifying the emissions, resource consumption, and energy use, collectively known as environmental stressors, that are associated with converting a raw material to a final product. Performed in conjunction with a technoeconomic feasibility study, the total economic and environmental benefits and drawbacks of a process can be quantified. This study complements a technoeconomic analysis of the same process, reported in Craig and Mann (1996) and updated here. The process studied is based on the concept of power Generation in a biomass integrated gasification combined cycle (BIGCC) plant. Broadly speaking, the overall system consists of biomass production, its transportation to the power plant, electricity generation, and any upstream processes required for system operation. The biomass is assumed to be supplied to the plant as wood chips from a biomass plantation, which would produce energy crops in a manner similar to the way food and fiber crops are produced today. Transportation of the biomass and other materials is by both rail and truck. The IGCC plant is sized at 113 MW, and integrates an indirectly-heated gasifier with an industrial gas turbine and steam cycle. 63 refs., 34 figs., 32 tabs.

Mann, M.K.; Spath, P.L.

1997-12-01T23:59:59.000Z

29

Analysis of Biomass/Coal Co-Gasification for Integrated Gasification Combined Cycle (IGCC) Systems with Carbon Capture.  

E-Print Network [OSTI]

?? In recent years, Integrated Gasification Combined Cycle Technology (IGCC) has become more common in clean coal power operations with carbon capture and sequestration (CCS).… (more)

Long, Henry A, III

2011-01-01T23:59:59.000Z

30

Design of advanced fossil-fuel systems (DAFFS): a study of three developing technologies for coal-fired, base-load electric power generation. Integrated coal gasification/combined cycle power plant with Texaco gasification process  

SciTech Connect (OSTI)

The objectives of this report are to present the facility description, plant layouts and additional information which define the conceptual engineering design, and performance and cost estimates for the Texaco Integrated Gasification Combined Cycle (IGCC) power plant. Following the introductory comments, the results of the Texaco IGCC power plant study are summarized in Section 2. In Section 3, a description of plant systems and facilities is provided. Section 4 includes pertinent performance information and assessments of availability, natural resource requirements and environmental impact. Estimates of capital costs, operation and maintenance costs and cost of electricity are presented in Section 5. A Bechtel Group, Inc. assessment and comments on the designs provided by Burns and Roe-Humphreys and Glasgow Synthetic Fuel, Inc. are included in Section 6. The design and cost estimate reports which were prepared by BRHG for those items within their scope of responsibility are included as Appendices A and B, respectively. Appendix C is an equipment list for items within the BGI scope. The design and cost estimate classifications chart referenced in Section 5 is included as Appendix D. 8 references, 17 figures, 15 tables.

Not Available

1983-06-01T23:59:59.000Z

31

Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, Final Environmental Impact Statement  

Broader source: Energy.gov (indexed) [DOE]

8 8 U.S. Department of Energy Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project Final Environmental Impact Statement November 2002 U.S. Department of Energy National Energy Technology Laboratory COVER SHEET Responsible Agency: U.S. Department of Energy (DOE) Title: Kentucky Pioneer Integrated Gasification Combined Cycle (IGCC) Demonstration Project Final Environmental Impact Statement (EIS) (DOE/EIS-0318) Location: Clark County, Kentucky Contacts: For further information on this environmental For further information on the DOE National impact statement (EIS), call: Environmental Policy Act (NEPA) process, call: 1-800-432-8330 ext. 5460 1-800-472-2756 or contact: or contact: Mr. Roy Spears Ms. Carol Borgstrom

32

Carbon Dioxide Capture from Integrated Gasification Combined Cycle Gas Streams Using the Ammonium Carbonate-Ammonium Bicarbonate Process  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Integrated Integrated Gasification Combined Cycle Gas Streams Using the Ammonium Carbonate- Ammonium Bicarbonate Process Description Current commercial processes to remove carbon dioxide (CO 2 ) from conventional power plants are expensive and energy intensive. The objective of this project is to reduce the cost associated with the capture of CO 2 from coal based gasification processes, which convert coal and other carbon based feedstocks to synthesis gas.

33

Integrated Gasification Combined Cycle Dynamic Model: H2S Absorption/Stripping, Water?Gas Shift Reactors, and CO2 Absorption/Stripping  

Science Journals Connector (OSTI)

Integrated Gasification Combined Cycle Dynamic Model: H2S Absorption/Stripping, Water?Gas Shift Reactors, and CO2 Absorption/Stripping ... Future chemical plants may be required to have much higher flexibility and agility than existing process facilities in order to be able to handle new hybrid combinations of power and chemical units. ...

Patrick J. Robinson; William L. Luyben

2010-04-26T23:59:59.000Z

34

Application of the integrated gasification combined cycle technology and BGL gasification design for power generation  

SciTech Connect (OSTI)

Integrated gasification combined cycle (IGCC) technology promises to be the power generation technology of choice in the late 1990s and beyond. Based on the principle that almost any fuel can be burned more cleanly and efficiently if first turned into a gas, an IGCC plant extracts more electricity from a ton of coal by burning it as a gas in a turbine rather than as a solid in a boiler. Accordingly, coal gasification is the process of converting coal to a clean-burning synthetic gas. IGCC technology is the integration of the coal-gasification plant with a conventional combined-cycle plant to produce electricity. The benefits of this technology merger are many and result in a highly efficient and environmentally superior energy production facility. The lGCC technology holds significant implications for Asia-Pacific countries and for other parts of the world. High-growth regions require additional baseload capacity. Current low prices for natural gas and minimal emissions that result from its use for power generation favor its selection as the fuel source for new power generation capacity. However, fluctuations in fuel price and fuel availability are undermining the industry`s confidence in planning future capacity based upon gas-fueled generation. With the world`s vast coal reserves, there is a continuing effort to provide coal-fueled power generation technologies that use coal cleanly and efficiently. The lGCC technology accomplishes this objective. This chapter provides a summary of the status of lGCC technology and lGCC projects known to date. It also will present a technical overview of the British Gas/Lurgi (BGL) technology, one of the leading and most promising coal gasifier designs.

Edmonds, R.F. Jr.; Hulkowich, G.J.

1993-12-31T23:59:59.000Z

35

Black liquor gasification combined cycle with Co2 capture – Technical and economic analysis  

Science Journals Connector (OSTI)

Abstract The pulp and paper sector is intensive in the use of energy, and presents a high participation in the industrial context, specially based in the black liquor, a renewable source generated in the pulp process. Black liquor gasification is not still completely dominated; however, it has the potential of becoming an important alternative for the pulp and paper sector. In this article, the traditional steam cycle based on chemical recovery and biomass boilers associated to backpressure/extraction turbine is compared to black liquor gasification combined cycle schemes, associated to biomass boiler, considering the technical and economic attractiveness of capturing and sequestering CO2. Results show that despite its interesting exergetic efficiency, the adoption CO2 capture system for BLGCC did not prove to be attractive under the prescribed conditions without major incentive.

Elzimar Tadeu de Freitas Ferreira; José Antonio Perrella Balestieri

2014-01-01T23:59:59.000Z

36

System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801  

SciTech Connect (OSTI)

S partial gasification combined cycle with CO{sub 2} recovery is proposed in this paper. Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of syngas produces only CO{sub 2} and H{sub 2}O, so the CO{sub 2} can be separated through cooling the working fluid. This decreases the amount of energy consumption to separate CO{sub 2} compared with conventional methods. The novel system integrates the above two key technologies by injecting steam from a steam turbine into the combustion chamber of a gas turbine to combine the Rankine cycle with the Brayton cycle. The thermal efficiency of this system will be higher based on the cascade utilization of energy level. Compared with the conventional integrated gasification combined cycle (IGCC), the compressor of the gas turbine, heat recovery steam generator (HRSG) and gasifier are substituted for a pump, reheater, and partial gasifier, so the system is simplified. Furthermore, the novel system is investigated by means of energy-utilization diagram methodology and provides a simple analysis of their economic and environmental performance. As a result, the thermal efficiency of this system may be expected to be 45%, with CO{sub 2} recovery of 41.2%, which is 1.5-3.5% higher than that of an IGCC system. At the same time, the total investment cost of the new system is about 16% lower than that of an IGCC. The comparison between the partial gasification technology and the IGCC technology is based on the two representative cases to identify the specific feature of the proposed system.

Xu, Y.J.; Jin, H.G.; Lin, R.M.; Han, W. [Chinese Academy of Science, Beijing (China)

2008-09-15T23:59:59.000Z

37

Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, Final Environmental Impact Statement  

Broader source: Energy.gov (indexed) [DOE]

S-1 S-1 SUMMARY The U.S. Department of Energy (DOE) prepared this environmental impact statement (EIS) on the proposed Kentucky Pioneer Integrated Gasification Combined Cycle (IGCC) Demonstration Project in compliance with the National Environmental Policy Act (NEPA). The National Environmental Policy Act Process NEPA is a federal law that serves as the basic national charter for protection of the environment. For major federal actions that may significantly affect the quality of the environment, NEPA requires federal agencies to prepare a detailed statement that includes the potential environmental impacts of the Proposed Action and reasonable alternatives. A fundamental objective of NEPA is to foster better decisionmaking by ensuring that high quality environmental information is available to public officials and members of the

38

Filter system cost comparison for integrated gasification combined cycle and pressurized fluidized-bed combustion power systems  

SciTech Connect (OSTI)

To assess the relative cost of components and sub-systems for a hot gas particulate cleanup system a cost comparison between the filter systems for two advanced coal-based power plants was conducted. Assessing component and sub-system costs permits the most beneficial areas for product improvement to be identified. The results from this study are presented. The filter system is based on a Westinghouse Advanced Particulate Filter Concept which is designed to operate with ceramic candle filters. The Foster Wheeler second Generation 453 MWe (net) Pressurized Fluidized-Bed Combustor (PFBC) and the KRW 458 MWe (net) Integrated Gasification Combined Cycle (IGCC) power plants are used for the comparison. The comparison presents the general differences of the two power plants and the process related filtration conditions for PFBC and IGCC systems. The results present the conceptual designs for the PFBC and IGCC filter systems as well as a cost summary comparison. The cost summary comparison includes the total plant cost, the fixed operating and maintenance cost, the variable operating and maintenance cost and the effect on the cost of electricity for the two filter systems. The most beneficial areas for product improvement are identified.

Dennis, R.A.; McDaniel, H.M. [Dept. of Energy, Morgantown, WV (United States). Morgantown Energy Technology Center; Buchanan, T.; Chen, H.; Harbaugh, L.B.; Klett, M.; Zaharchuk, R. [Gilbert/Commonwealth, Reading, PA (United States)

1995-12-31T23:59:59.000Z

39

A Review of Hazardous Chemical Species Associated with CO2 Capture from Coal-Fired Power Plants and Their Potential Fate in CO2 Geologic Storage  

E-Print Network [OSTI]

Integrated Gasification Combined Cycle Technology: IGCC.integrated gasification combined cycle (IGCC) power plants (output. Integrated gas combined cycle (IGCC) plants are

Apps, J.A.

2006-01-01T23:59:59.000Z

40

Integrated Gasification Combined Cycle (IGCC) demonstration project, Polk Power Station -- Unit No. 1. Annual report, October 1993--September 1994  

SciTech Connect (OSTI)

This describes the Tampa Electric Company`s Polk Power Station Unit 1 (PPS-1) Integrated Gasification Combined Cycle (IGCC) demonstration project which will use a Texaco pressurized, oxygen-blown, entrained-flow coal gasifier to convert approximately 2,300 tons per day of coal (dry basis) coupled with a combined cycle power block to produce a net 250 MW electrical power output. Coal is slurried in water, combined with 95% pure oxygen from an air separation unit, and sent to the gasifier to produce a high temperature, high pressure, medium-Btu syngas with a heat content of about 250 Btu/scf (LHV). The syngas then flows through a high temperature heat recovery unit which cools the syngas prior to its entering the cleanup systems. Molten coal ash flows from the bottom of the high temperature heat recovery unit into a water-filled quench chamber where it solidifies into a marketable slag by-product.

NONE

1995-05-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


41

THERMODYNAMIC MODELLING OF BIOMASS INTEGRATED GASIFICATION COMBINED CYCLE (BIGCC) POWER GENERATION SYSTEM.  

E-Print Network [OSTI]

??An attractive and practicable possibility of biomass utilization for energy production is gasification integrated with a combined cycle. This technology seems to have the possibility… (more)

Desta, Melaku

2011-01-01T23:59:59.000Z

42

The United States of America and the People`s Republic of China experts report on integrated gasification combined-cycle technology (IGCC)  

SciTech Connect (OSTI)

A report written by the leading US and Chinese experts in Integrated Gasification Combined Cycle (IGCC) power plants, intended for high level decision makers, may greatly accelerate the development of an IGCC demonstration project in the People`s Republic of China (PRC). The potential market for IGCC systems in China and the competitiveness of IGCC technology with other clean coal options for China have been analyzed in the report. Such information will be useful not only to the Chinese government but also to US vendors and companies. The goal of this report is to analyze the energy supply structure of China, China`s energy and environmental protection demand, and the potential market in China in order to make a justified and reasonable assessment on feasibility of the transfer of US Clean Coal Technologies to China. The Expert Report was developed and written by the joint US/PRC IGCC experts and will be presented to the State Planning Commission (SPC) by the President of the CAS to ensure consideration of the importance of IGCC for future PRC power production.

NONE

1996-12-01T23:59:59.000Z

43

Analysis of Membrane and Adsorbent Processes for Warm Syngas Cleanup in Integrated Gasification Combined-Cycle Power with CO2 Capture and Sequestration  

Science Journals Connector (OSTI)

Analysis of Membrane and Adsorbent Processes for Warm Syngas Cleanup in Integrated Gasification Combined-Cycle Power with CO2 Capture and Sequestration ... The clean syngas is diluted with N2 from the ASU and enters the gas turbine burner. ... The amount of N2 diluent to be added is determined by the requirement of maintaining the appropriate lower heating value of the syngas feeding into the gas turbine burner to achieve sufficiently low NOx emissions (15–35 ppmv at 15% O2)(36) and to keep the temperature of the gas low enough to avoid blade failure. ...

David J. Couling; Kshitij Prakash; William H. Green

2011-08-11T23:59:59.000Z

44

The role of Life Cycle Assessment in identifying and reducing environmental impacts of CCS  

E-Print Network [OSTI]

Integrated Gasification Combined Cycle (IGCC) Power Plant.Analysis: Natural Gas Combined Cycle (NGCC) Power Plant.assessment of natural gas combined cycle power plant with

Sathre, Roger

2011-01-01T23:59:59.000Z

45

Design of advanced fossil-fuel systems (DAFFS): a study of three developing technologies for coal-fired, base-load electric power generation. Integrated coal-gasification/combined power plant with BGC/Lurgi gasification process  

SciTech Connect (OSTI)

The objectives of this report are to present the facility description, plant layouts and additional information which define the conceptual engineering design, and performance and cost estimates for the BGC/Lurgi Integrated Gasification Combined Cycle (IGCC) power plant. Following the introductory comments, the results of the British Gas Corporation (BGC)/Lurgi IGCC power plant study are summarized in Section 2. In Secion 3, a description of plant systems and facilities is provided. Section 4 includes pertinent performance information and assessments of availability, natural resource requirements and environmental impact. Estimates of capital costs, operating and maintenance costs and cost of electricity are presented in Section 5. A Bechtel Group Inc. (BGI) assessment and comments on the designs provided by Burns and Roe-Humphreys and Glasgow Synthetic Fuels, Inc. (BRHG) are included in Section 6. The design and cost estimate reports which were prepared by BRHG for those items within their scope of responsibility are included as Appendices A and B, respectively. Apendix C is an equipment list for items within the BGI scope. The design and cost estimate classifications chart referenced in Section 5 is included as Appendix D. 8 references, 18 figures, 5 tables.

Not Available

1983-06-01T23:59:59.000Z

46

EIS-0431: Hydrogen Energy California's Integrated Gasification Combined  

Broader source: Energy.gov (indexed) [DOE]

1: Hydrogen Energy California's Integrated Gasification 1: Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, California EIS-0431: Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, California Summary This EIS evaluates the potential environmental impacts of a proposal to provide financial assistance for the construction and operation of Hydrogen Energy California LLC (HECA's) project, which would produce and sell electricity, carbon dioxide and fertilizer. DOE selected this project for an award of financial assistance through a competitive process under the Clean Coal Power Initiative program. Public Comment Opportunities None available at this time. Documents Available for Download September 5, 2013

47

Kinetic mechanism of dimethyl ether production process using syngas from integrated gasification combined cycle power plant  

Science Journals Connector (OSTI)

In a 1-step synthesis gas-to-dimethyl ether process, synthesis gas is converted into dimethyl ether (DME) in a single reactor. Three reactions are involved in this process: methanol synthesis, methanol dehydra...

Hee-Woo Park; Jin-Kuk Ha; Euy Soo Lee

2014-07-01T23:59:59.000Z

48

Conceptual Design of a Fossil Hydrogen Infrastructure with Capture and Sequestration of Carbon Dioxide: Case Study in Ohio  

E-Print Network [OSTI]

integrated gasification combined cycle (IGCC) plant couldintegrated gasification combined cycle (IGCC) plants and the

2005-01-01T23:59:59.000Z

49

Techno-economic assessment of pulverized coal boilers and IGCC power plants with CO2 capture  

Science Journals Connector (OSTI)

The current studies on power plant technologies suggest that Integrated Gasification Combined Cycle (IGCC) systems are an effective and economic CO2 capture technology pathway. In addition, the system in conventi...

Y. Huang; S. Rezvani; D. McIlveen-Wright…

2010-06-01T23:59:59.000Z

50

Power Plant Cycling Costs  

SciTech Connect (OSTI)

This report provides a detailed review of the most up to date data available on power plant cycling costs. The primary objective of this report is to increase awareness of power plant cycling cost, the use of these costs in renewable integration studies and to stimulate debate between policymakers, system dispatchers, plant personnel and power utilities.

Kumar, N.; Besuner, P.; Lefton, S.; Agan, D.; Hilleman, D.

2012-07-01T23:59:59.000Z

51

Future Impacts of Coal Distribution Constraints on Coal Cost  

E-Print Network [OSTI]

integrated gasification combined cycle ( IGCC) power plantsintegrated gasification combined cycle (IGCC) power plants,be integrated gasification combined cycle (IGCC) (Same power

McCollum, David L

2007-01-01T23:59:59.000Z

52

Power Plant Cycling Costs  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Power Plant Cycling Costs Power Plant Cycling Costs April 2012 N. Kumar, P. Besuner, S. Lefton, D. Agan, and D. Hilleman Intertek APTECH Sunnyvale, California NREL Technical Monitor: Debra Lew Subcontract Report NREL/SR-5500-55433 July 2012 NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. National Renewable Energy Laboratory 15013 Denver West Parkway Golden, Colorado 80401 303-275-3000 * www.nrel.gov Contract No. DE-AC36-08GO28308 Power Plant Cycling Costs April 2012 N. Kumar, P. Besuner, S. Lefton, D. Agan, and D. Hilleman Intertek APTECH Sunnyvale, California NREL Technical Monitor: Debra Lew Prepared under Subcontract No. NFT-1-11325-01

53

Cost of energy analysis of integrated gasification combined cycle (IGCC) power plant with respect to CO2 capture ratio under climate change scenarios  

Science Journals Connector (OSTI)

This paper presents the results of the cost of energy (COE) analysis of an integrated gasification...2...capture ratio under the climate change scenarios. To obtain process data for a COE analysis, simulation mod...

Kyungtae Park; Dongil Shin; Gibaek Lee…

2012-09-01T23:59:59.000Z

54

Life Cycle Regulation of Transportation Fuels: Uncertainty and its Policy Implications  

E-Print Network [OSTI]

ethanol; NGCC = natural gas combined-cycle; BIGCC =gasification combined-cycle. P ART III U NCERTAINTY Aaverage, (ii) natural gas combined-cycle (NGCC), (iii) coal

Plevin, Richard Jay

2010-01-01T23:59:59.000Z

55

Prioritizing Climate Change Mitigation Alternatives: Comparing Transportation Technologies to Options in Other Sectors  

E-Print Network [OSTI]

of natural gas-powered combined cycle power plants. The mostintegrated gasification combined cycle (IGCC) coal plants,integrated gasification combined cycle (IGCC) technology for

Lutsey, Nicholas P.

2008-01-01T23:59:59.000Z

56

Estimating Policy-Driven Greenhouse Gas Emissions Trajectories in California: The California Greenhouse Gas Inventory Spreadsheet (GHGIS) Model  

E-Print Network [OSTI]

k. Integrated gasification combined cycle (IGCC) coal l. PCIntegrated Gasification Combined Cycle (IGCC) Power Plant,Analysis: Natural Gas Combined Cycle (NGCC) Power Plant,

Greenblatt, Jeffery B.

2014-01-01T23:59:59.000Z

57

Natural Gas Combined Cycle Power Plant Integrated to Capture Plant  

Science Journals Connector (OSTI)

Natural Gas Combined Cycle Power Plant Integrated to Capture Plant ... A natural gas combined cycle (NGCC) power plant with capacity of about 430 MW integrated to a chemical solvent absorber/stripping capture plant is investigated. ... The natural gas combined cycle (NGCC) is an advanced power generation technology that improves the fuel efficiency of natural gas. ...

Mehdi Karimi; Magne Hillestad; Hallvard F. Svendsen

2012-01-19T23:59:59.000Z

58

Development of a dynamic simulator for a natural gas combined cycle (NGCC) power plant with post-combustion carbon capture  

SciTech Connect (OSTI)

The AVESTAR Center located at the U.S. Department of Energy’s National Energy Technology Laboratory and West Virginia University is a world-class research and training environment dedicated to using dynamic process simulation as a tool for advancing the safe, efficient and reliable operation of clean energy plants with CO{sub 2} capture. The AVESTAR Center was launched with a high-fidelity dynamic simulator for an Integrated Gasification Combined Cycle (IGCC) power plant with pre-combustion carbon capture. The IGCC dynamic simulator offers full-scope Operator Training Simulator (OTS) Human Machine Interface (HMI) graphics for realistic, real-time control room operation and is integrated with a 3D virtual Immersive Training Simulator (ITS), thus allowing joint control room and field operator training. The IGCC OTS/ITS solution combines a “gasification with CO{sub 2} capture” process simulator with a “combined cycle” power simulator into a single high-performance dynamic simulation framework. This presentation will describe progress on the development of a natural gas combined cycle (NGCC) dynamic simulator based on the syngas-fired combined cycle portion of AVESTAR’s IGCC dynamic simulator. The 574 MW gross NGCC power plant design consisting of two advanced F-class gas turbines, two heat recovery steam generators (HRSGs), and a steam turbine in a multi-shaft 2x2x1 configuration will be reviewed. Plans for integrating a post-combustion carbon capture system will also be discussed.

Liese, E.; Zitney, S.

2012-01-01T23:59:59.000Z

59

Assessment of Brine Management for Geologic Carbon Sequestration  

E-Print Network [OSTI]

of  water  use  at  combined-­?cycle  power  plants. ”  Gasification  Combined  Cycle Known  Geothermal  Energy  integrated  gasification  combined   cycle  (IGCC)  CFPP,  

Breunig, Hanna M.

2014-01-01T23:59:59.000Z

60

Development and Application of Advanced Models for Steam Hydrogasification: Process Design and Economic Evaluation  

E-Print Network [OSTI]

S. Integrated Gasification Combined Cycle-A review of IGCCBiomass Gasification Combined Cycle System. December 1997.liquefaction and combined-cycle power plant. Pittsburgh (

Lu, Xiaoming

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


61

Coal-Fuelled Combined Cycle Power Plants  

Science Journals Connector (OSTI)

Combined cycle power plant, when used as a generic ... which converts heat into mechanical energy in a combined gas and steam turbine process. Combined cycle processes with coal gasification or coal combustion .....

Dr. Hartmut Spliethoff

2010-01-01T23:59:59.000Z

62

Efficiency combined cycle power plant  

SciTech Connect (OSTI)

This patent describes a method of operating a combined cycle power plant. It comprises: flowing exhaust gas from a combustion turbine through a heat recovery steam generator (HRSG); flowing feed water through an economizer section of the HRSG at a flow rate and providing heated feed water; flowing a first portion of the heated feed water through an evaporator section of the HRSG and producing saturated steam at a production rate, the flow rate of the feed water through the economizer section being greater than required to sustain the production rate of steam in the evaporator section; flowing fuel for the turbine through a heat exchanger; and, flowing a second portion of the heated feed water provided by the economizer section through the heat exchanger then to an inlet of the economizer section, thereby heating the fuel flowing through the heat exchanger.

Pavel, J.; Meyers, G.A.; Baldwin, T.S.

1990-06-12T23:59:59.000Z

63

Binary Cycle Power Plant | Open Energy Information  

Open Energy Info (EERE)

Binary Cycle Power Plant Binary Cycle Power Plant (Redirected from Binary Cycle Power Plants) Jump to: navigation, search GEOTHERMAL ENERGYGeothermal Home Binary Cycle Power Plant General List of Binary Plants Binary power plant process diagram - DOE EERE 2012 Binary cycle geothermal power generation plants differ from Dry Steam and Flash Steam systems in that the water or steam from the geothermal reservoir never comes in contact with the turbine/generator units. Low to moderately heated (below 400°F) geothermal fluid and a secondary (hence, "binary") fluid with a much lower boiling point that water pass through a heat exchanger. Heat from the geothermal fluid causes the secondary fluid to flash to vapor, which then drives the turbines and subsequently, the generators.

64

Binary Cycle Power Plant | Open Energy Information  

Open Energy Info (EERE)

Binary Cycle Power Plant Binary Cycle Power Plant (Redirected from Binary) Jump to: navigation, search GEOTHERMAL ENERGYGeothermal Home Binary Cycle Power Plant General List of Binary Plants Binary power plant process diagram - DOE EERE 2012 Binary cycle geothermal power generation plants differ from Dry Steam and Flash Steam systems in that the water or steam from the geothermal reservoir never comes in contact with the turbine/generator units. Low to moderately heated (below 400°F) geothermal fluid and a secondary (hence, "binary") fluid with a much lower boiling point that water pass through a heat exchanger. Heat from the geothermal fluid causes the secondary fluid to flash to vapor, which then drives the turbines and subsequently, the generators. Binary cycle power plants are closed-loop systems and virtually nothing

65

E:\\PUBLAW\\PUBL058.109  

Broader source: Energy.gov (indexed) [DOE]

tees for the following gasification projects: (1) INTEGRATED GASIFICATION COMBINED CYCLE PROJECTS.- Integrated gasification combined cycle plants meeting the emis- sion levels...

66

Combustion and Flame 150 (2007) 246262 www.elsevier.com/locate/combustflame  

E-Print Network [OSTI]

compression ignition (HCCI) engines [1] and integrated gasification combined cycle (IGCC) power plants [2

Wooldridge, Margaret S.

67

Binary Cycle Power Plant | Open Energy Information  

Open Energy Info (EERE)

GEOTHERMAL ENERGYGeothermal Home GEOTHERMAL ENERGYGeothermal Home Binary Cycle Power Plant General List of Binary Plants Binary power plant process diagram - DOE EERE 2012 Binary cycle geothermal power generation plants differ from Dry Steam and Flash Steam systems in that the water or steam from the geothermal reservoir never comes in contact with the turbine/generator units. Low to moderately heated (below 400°F) geothermal fluid and a secondary (hence, "binary") fluid with a much lower boiling point that water pass through a heat exchanger. Heat from the geothermal fluid causes the secondary fluid to flash to vapor, which then drives the turbines and subsequently, the generators. Binary cycle power plants are closed-loop systems and virtually nothing (except water vapor) is emitted to the atmosphere. Resources below 400°F

68

Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, Final Environmental Impact Statement  

Broader source: Energy.gov (indexed) [DOE]

A-1 A-1 APPENDIX A CONSULTATION LETTERS This appendix includes consultation/approval letters between the U.S. Department of Energy and the U.S. Fish and Wildlife Service regarding threatened and endangered species, and between other state and Federal agencies as needed. Consultation Letters A-2 Kentucky Pioneer IGCC Demonstration Project Final Environmental Impact Statement A-3 Consultation Letters A-4 Kentucky Pioneer IGCC Demonstration Project Final Environmental Impact Statement A-5 Consultation Letters A-6 Kentucky Pioneer IGCC Demonstration Project Final Environmental Impact Statement A-7 Consultation Letters A-8 Kentucky Pioneer IGCC Demonstration Project Final Environmental Impact Statement B-1 APPENDIX B NOTICE OF INTENT TO PREPARE AN ENVIRONMENTAL IMPACT STATEMENT FOR THE

69

Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, Final Environmental Impact Statement  

Broader source: Energy.gov (indexed) [DOE]

Comments Comments Kentucky Pioneer IGCC Demonstration Project Final Environmental Impact Statement Clark County Public Library Winchester, KY Page 1 of 5 D-1 Comment No. 1 Issue Code: 11 Gasification is different from incineration. It is a better, more environmentally responsible approach to generating energy from the use of fossil fuels and refuse derived fuel (RDF). Incineration produces criteria pollutants, semi-volatile and volatile organic compounds and dioxin/furan compounds. Ash from hazardous waste incinerators is considered a hazardous waste under the Resource Conservation and Recovery Act (RCRA). In contrast, gasification, which occurs at high temperatures and pressures, produces no air emissions, only small amounts of wastewater containing salts. Synthesis gas (syngas)

70

EIS-0431: Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, California  

Broader source: Energy.gov [DOE]

This EIS evaluates the potential environmental impacts of a proposal to provide financial assistance for the construction and operation of Hydrogen Energy California's LLC project, which would produce and sell electricity, carbon dioxide and fertilizer. DOE selected this project for an award of financial assistance through a competitive process under the Clean Coal Power Initiative program.

71

Simulation and optimization of hot syngas separation processes in integrated gasification combined cycle  

E-Print Network [OSTI]

IGCC with CO2 capture offers an exciting approach for cleanly using abundant coal reserves of the world to generate electricity. The present state-of-the-art synthesis gas (syngas) cleanup technologies in IGCC involve ...

Prakash, Kshitij

2009-01-01T23:59:59.000Z

72

EIS-0429: Department of Energy Loan Guarantee for Indiana Integrated Gasification Combined Cycle, Rockport, IN  

Broader source: Energy.gov [DOE]

This EIS evaluates the environmental impacts of a coal-to-substitute natural gas facility proposed to be built in Rockport, IN by Indiana Gasification. The facility would utilize Illinois Basin coal. Other products would be marketable sulfuric acid, argon, and electric power.

73

EIS-0428: Department of Energy Loan Guarantee for Mississippi Integrated Gasification Combined Cycle, Moss Point, Mississippi  

Broader source: Energy.gov [DOE]

This EIS evaluates the environmental impacts of a petroleum coke-to-substitute natural gas facility proposed to be built by Mississippi Gasification. The facility would be designed to produce 120 million standard cubic feet of gas per day. Other products would be marketable sulfuric acid, carbon dioxide, argon, and electric power.

74

EIS-0318: Kentucky Pioneer Integrated Gasification Combined Cycle (IGCC) Demonstration Project, Trapp, Kentucky (Clark County)  

Broader source: Energy.gov [DOE]

This EIS analyzes DOE's decision to provide cost-shared financial support for The Kentucky Pioneer IGCC Demonstration Project, an electrical power station demonstrating use of a Clean Coal Technology in Clark County, Kentucky.

75

The development of Coke Carried-Heat Gasification Coal-Fired Combined Cycle  

Science Journals Connector (OSTI)

Carried-Heat Partial Gasification Combined cycle is a novel combined cycle which was proposed by Thermal Engineering Department ... technology, Coke Carried-Heat Gasification Coal-Fired Combined Cycle, as the imp...

Li Zhao; Xiangdong Xu

1999-12-01T23:59:59.000Z

76

Parabolic Trough Organic Rankine Cycle Power Plant  

SciTech Connect (OSTI)

Arizona Public Service (APS) is required to generate a portion of its electricity from solar resources in order to satisfy its obligation under the Arizona Environmental Portfolio Standard (EPS). In recent years, APS has installed and operates over 4.5 MWe of fixed, tracking, and concentrating photovoltaic systems to help meet the solar portion of this obligation and to develop an understanding of which solar technologies provide the best cost and performance to meet utility needs. During FY04, APS began construction of a 1-MWe parabolic trough concentrating solar power plant. This plant represents the first parabolic trough plant to begin construction since 1991. The plant will also be the first commercial deployment of the Solargenix parabolic trough collector technology developed under contract to the National Renewable Energy Laboratory (NREL). The plant will use an organic Rankine cycle (ORC) power plant, provided by Ormat. The ORC power plant is much simpler than a conventional steam Rankine cycle power plant and allows unattended operation of the facility.

Canada, S.; Cohen, G.; Cable, R.; Brosseau, D.; Price, H.

2005-01-01T23:59:59.000Z

77

Combined cycle power plant incorporating coal gasification  

DOE Patents [OSTI]

A combined cycle power plant incorporating a coal gasifier as the energy source. The gases leaving the coal gasifier pass through a liquid couplant heat exchanger before being used to drive a gas turbine. The exhaust gases of the gas turbine are used to generate both high pressure and low pressure steam for driving a steam turbine, before being exhausted to the atmosphere.

Liljedahl, Gregory N. (Tariffville, CT); Moffat, Bruce K. (Simsbury, CT)

1981-01-01T23:59:59.000Z

78

Single stage rankine and cycle power plant  

SciTech Connect (OSTI)

The specification describes a Rankine cycle power plant of the single stage type energized by gasified freon, the latter being derived from freon in the liquid state in a boiler provided in the form of a radio frequency heating cell adapted at low energy input to effect a rapid change of state from liquid freon at a given temperature and pressure to gaseous freon of relatively large volume, thereby to drive a Rankine cycle type of engine recognized in the prior art as a steam engine type of engine of the piston or turbine type.

Closs, J.J.

1981-10-13T23:59:59.000Z

79

Use of combined-cycle power units at cogeneration plants  

Science Journals Connector (OSTI)

Indices of reconstructed and new cogeneration plants (CPs) using combined cycle units (CCPUs) are considered. The conclusions...

V. M. Batenin; Yu. A. Zeigarnik; V. M. Maslennikov; Yu. L. Shekhter…

2008-12-01T23:59:59.000Z

80

Mastering the pilot domestic binary combined-cycle plants  

Science Journals Connector (OSTI)

Results are presented from mastering the pilot binary combined-cycle plants of Type PGU-450T (installed at...

Yu. A. Radin

2006-07-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


81

Accelerating progress toward operational excellence of fossil energy plants with CO2 capture  

SciTech Connect (OSTI)

To address challenges in attaining operational excellence for clean energy plants, the National Energy Technology Laboratory has launched a world-class facility for Advanced Virtual Energy Simulation Training And Research (AVESTARTM). The AVESTAR Center brings together state-of-the-art, real-time, high-fidelity dynamic simulators with operator training systems and 3D virtual immersive training systems into an integrated energy plant and control room environment. This paper will highlight the AVESTAR Center simulators, facilities, and comprehensive training, education, and research programs focused on the operation and control of an integrated gasification combined cycle power plant (IGCC) with carbon dioxide capture.

Zitney, S.; Liese, E.; Mahapatra, P.; Turton, R. Bhattacharyya, D.

2012-01-01T23:59:59.000Z

82

Advanced Coal Wind Hybrid: Economic Analysis  

E-Print Network [OSTI]

such as synthetic crude gasification combined cycle powerstand-alone integrated gasification combined cycle powertransmission integrated gasification, combined cycle power

Phadke, Amol

2008-01-01T23:59:59.000Z

83

AVESTAR Center: Dynamic simulation-based collaboration toward achieving opertional excellence for IGCC plants with crbon capture  

SciTech Connect (OSTI)

To address challenges in attaining operational excellence for clean energy plants, the National Energy Technology Laboratory has launched a world-class facility for Advanced Virtual Energy Simulation Training And Research (AVESTAR(TM)). The AVESTAR Center brings together state-of-the-art, real-time, high-fidelity dynamic simulators with operator training systems and 3D virtual immersive training systems into an integrated energy plant and control room environment. This paper will highlight the AVESTAR Center simulators, facilities, and comprehensive training, education, and research programs focused on the operation and control of an integrated gasification combined cycle power plant (IGCC) with carbon dioxide capture.

Zitney, Strphen E. [U.S. DOE; Liese, Eric A. [U.S. DOE; Mahapatra, Priyadarshi [URS; Turton, Richard [WVU; Bhattacharyya, Debangsu [WVU; Provost, Graham [Fossil Consulting Services

2012-01-01T23:59:59.000Z

84

Analysis of a coal fired combined cycle with carried-heat gasification  

Science Journals Connector (OSTI)

In the research of a more efficient, less costly, more environmentally responsible and less technically difficult method for generating electrical power from coal, the Carried-heat Gasification Combined Cycle (CG...

Xiangdong Xu; Weimin Zhu; Li Zhao; F. N. Fett

85

SUPERCRITICAL STEAM CYCLE FOR NUCLEAR POWER PLANT  

SciTech Connect (OSTI)

Revolutionary improvement of the nuclear plant safety and economy with light water reactors can be reached with the application of micro-fuel elements (MFE) directly cooled by a supercritical pressure light-water coolant-moderator. There are considerable advantages of the MFE as compared with the traditional fuel rods, such as: Using supercritical and superheated steam considerably increases the thermal efficiency of the Rankine cycle up to 44-45%. Strong negative coolant and void reactivity coefficients with a very short thermal delay time allow the reactor to shutdown quickly in the event of a reactivity or power excursion. Core melting and the creation of corium during severe accidents are impossible. The heat transfer surface area is larger by several orders of magnitude due to the small spherical dimensions of the MFE. The larger heat exchange surface significantly simplifies residual heat removal by natural convection and radiation from the core to a subsequent passive system of heat removal.

Tsiklauri, Georgi V.; Talbert, Robert J.; Schmitt, Bruce E.; Filippov, Gennady A.; Bogojavlensky, Roald G.; Grishanin, Evgeny I.

2005-07-01T23:59:59.000Z

86

Resource Limits and Conversion Efficiency with Implications for Climate Change  

E-Print Network [OSTI]

using Integrated Gasification Combined Cycle (IGCC) plants.Natural gas-fired combined cycle plants can be converted toand more efficient combined-cycle plants. Combined cycle

Croft, Gregory Donald

2009-01-01T23:59:59.000Z

87

Insights for Quantitative Risk Assessment of Combined Cycle Power Plants  

Science Journals Connector (OSTI)

Traditional techniques of risk analysis have been fitted for the application to combined cycle power plants and the results of several...

Gabriele Ballocco; Andrea Carpignano…

2004-01-01T23:59:59.000Z

88

Experience with organic Rankine cycles in heat recovery power plants  

SciTech Connect (OSTI)

Over the last 30 years, organic Rankine cycles (ORC) have been increasingly employed to produce power from various heat sources when other alternatives were either technically not feasible or economical. These power plants have logged a total of over 100 million turbine hours of experience demonstrating the maturity and field proven technology of the ORC cycle. The cycle is well adapted to low to moderate temperature heat sources such as waste heat from industrial plants and is widely used to recover energy from geothermal resources. The above cycle technology is well established and applicable to heat recovery of medium size gas turbines and offers significant advantages over conventional steam bottoming cycles.

Bronicki, L.Y.; Elovic, A.; Rettger, P.

1996-11-01T23:59:59.000Z

89

Hybrid solar central receiver for combined cycle power plant  

DOE Patents [OSTI]

A hybrid combined cycle power plant including a solar central receiver for receiving solar radiation and converting it to thermal energy. The power plant includes a molten salt heat transfer medium for transferring the thermal energy to an air heater. The air heater uses the thermal energy to preheat the air from the compressor of the gas cycle. The exhaust gases from the gas cycle are directed to a steam turbine for additional energy production.

Bharathan, Desikan (Lakewood, CO); Bohn, Mark S. (Golden, CO); Williams, Thomas A. (Arvada, CO)

1995-01-01T23:59:59.000Z

90

NETL: Gasification - Feasibility Studies to Improve Plant Availability and  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Feasibility Studies to Improve Plant Availability and Reduce Total Installed Cost in IGCC Plants Feasibility Studies to Improve Plant Availability and Reduce Total Installed Cost in IGCC Plants General Electric Company Project Number: FE0007859 Project Description General Electric Company (GE) is studying the feasibility of improving plant availability and reducing total installed costs in Integrated Gasification Combined Cycle (IGCC) plants. GE is evaluating the IGCC technology effects of total installed cost and availability through deployment of a multi-faceted approach in technology evaluation, constructability, and design methodology. Eastman Chemical Company will be supporting the GE effort on certain technologies by providing consulting on the evaluations and technology transfer phases of the project. The end result is aimed at reducing the time to technological maturity and enabling plants to reach higher values of availability in a shorter period of time and at a lower installed cost.

91

AVESTAR Center for operational excellence of IGCC power plants with CO2 capture  

SciTech Connect (OSTI)

This presentation begins with a description of U.S. Energy Challenges, particularly Power Generation Capacity and Clean Energy Plant Operations. It goes on to describe the missions and goals of the Advanced Virtual Energy Simulation Training And Research (AVESTARTM). It moves on to the subject of Integrated Gasification Combined Cycle (IGCC) with CO{sub 2} Capture, particularly a Process/Project Overview, Dynamic Simulator/Operator Training System (OTS), 3D Virtual Immersive Training System (ITS), Facilities, Training, Education, and R&D, and Future Simulators/Directions

Provost, G,

2012-01-01T23:59:59.000Z

92

AVESTAR Center for operational excellence of IGCC power plants with CO2 capture  

SciTech Connect (OSTI)

This slideshow presentation begins by outlining US energy challenges, particularly with respect to power generation capacity and clean energy plant operations. It goes on to describe the Advanced Virtual Energy Simulation Training And Research (AVESTAR{sup TM}). Its mission and goals are given, followed by an overview of integrated gasification combined cycle (IGCC) with CO{sub 2} capture. The Dynamic Simulator/Operator Training System (OTS) and 3D Virtual Immersive Training System (ITS) are then presented. Facilities, training, education, and R&D are covered, followed by future simulators and directions.

Provost, G,

2012-01-01T23:59:59.000Z

93

Record of Decision for the Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, (DOE/EIS-0318) (February 4, 2003)  

Broader source: Energy.gov (indexed) [DOE]

8 8 Federal Register / Vol. 68, No. 23 / Tuesday, February 4, 2003 / Notices DEPARTMENT OF ENERGY Energy Information Administration Agency Information Collection Activities: Submission for OMB Review; Comment Request AGENCY: Energy Information Administration (EIA), Department of Energy (DOE). ACTION: Agency information collection activities: Submission for OMB review; comment request. SUMMARY: The EIA has submitted the energy information collections listed at the end of this notice to the Office of Management and Budget (OMB) for review and a three-year extension under section 3507(h)(1) of the Paperwork Reduction Act of 1995 (Pub. L. 104-13) (44 U.S.C. 3501 et seq). DATES: Comments must be filed on or before March 6, 2003. If you anticipate that you will be submitting comments

94

Life-cycle assessment of wastewater treatment plants  

E-Print Network [OSTI]

This thesis presents a general model for the carbon footprints analysis of wastewater treatment plants (WWTPs), using a life cycle assessment (LCA) approach. In previous research, the issue of global warming is often related ...

Dong, Bo, M. Eng. Massachusetts Institute of Technology

2012-01-01T23:59:59.000Z

95

Simulation of an Industrial Rankine Cycle Cogeneration Plant  

E-Print Network [OSTI]

and transient loads and the resulting interactions between system components may be assessed. A thermal energy system simulation code is utilized and expanded to predict the performance of an industrial Rankine cycle (steam turbine) cogeneration plant having...

Carattie, G.; Wepfer, W. J.

1984-01-01T23:59:59.000Z

96

Advanced Coal Wind Hybrid: Economic Analysis  

E-Print Network [OSTI]

IGCC PC advanced coal-wind hybrid combined cycle power plantnatural gas combined cycle gas turbine power plant carboncrude gasification combined cycle power plant with carbon

Phadke, Amol

2008-01-01T23:59:59.000Z

97

Performance improvement of combined cycle power plant based on the optimization of the bottom cycle and heat recuperation  

Science Journals Connector (OSTI)

Many F class gas turbine combined cycle (GTCC) power plants are built in ... the efficiency improvement of GTCC plant. A combined cycle with three-pressure reheat heat recovery steam ... HRSG inlet gas temperatur...

Wenguo Xiang; Yingying Chen

2007-03-01T23:59:59.000Z

98

DOE Signs Cooperative Agreement for New Hydrogen Power Plant | Department  

Broader source: Energy.gov (indexed) [DOE]

DOE Signs Cooperative Agreement for New Hydrogen Power Plant DOE Signs Cooperative Agreement for New Hydrogen Power Plant DOE Signs Cooperative Agreement for New Hydrogen Power Plant November 6, 2009 - 12:00pm Addthis Washington, D.C. -- The U.S. Department of Energy (DOE) has signed a cooperative agreement with Hydrogen Energy California LLC (HECA) to build and demonstrate a hydrogen-powered electric generating facility, complete with carbon capture and storage, in Kern County, Calif. The new plant is a step toward commercialization of a clean technology that enables use of our country's vast fossil energy resources while addressing the need to reduce greenhouse gas emissions. HECA, which is owned by Hydrogen Energy International, BP Alternative Energy, and Rio Tinto, plans to construct an advanced integrated gasification combined cycle (IGCC) plant that will produce power by

99

Effective Renewable Energy Policy: Leave It to the States?  

E-Print Network [OSTI]

solid waste, or coal integrated gasification combined cycle.integrated gasification combined cycle technologies, waste

Weissman, Steven

2011-01-01T23:59:59.000Z

100

Mesaba next-generation IGCC plant  

SciTech Connect (OSTI)

Through a US Department of Energy (DOE) cooperative agreement awarded in June 2006, MEP-I LLC plans to demonstrate a next generation integrated gasification-combined cycle (IGCC) electric power generating plant, the Mesaba Energy Project. The 606-MWe plant (the first of two similarly sized plants envisioned by project sponsors) will feature next-generation ConocoPhillips E-Gas{trademark} technology first tested on the DOE-funded Wabash River Coal Gasification Repowering project. Mesaba will benefit from recommendations of an industry panel applying the Value Improving Practices process to Wabash cost and performance results. The project will be twice the size of Wabash, while demonstrating better efficient, reliability and pollutant control. The $2.16 billion project ($36 million federal cost share) will be located in the Iron Range region north of Duluth, Minnesota. Mesaba is one of four projects selected under Round II of the Clean Coal Power Initiative. 1 fig.

NONE

2006-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


101

Cheng Cycle Brings Flexibility to Steam Plant  

E-Print Network [OSTI]

. Based upon an estimated steam load between 5,000 and 50,000 Ibjhr and an electrical load of approximately 1500 KW, the Engineering Department examined several energy optimization systems for this site. It was determined that a modified gas turbine... within the borders allows exact tracking of desired electrical and thermal outputs. The Allison engine used in the Cheng Cycle system was selected for its proved performance and its ample surge margin which permits stable steam injection...

Keller, D. C.; Bynum, D.; Kosla, L.

102

Thermodynamics of combined-cycle electric power plants  

Science Journals Connector (OSTI)

Published data imply an average thermal efficiency of about 0.34 for U.S. electricity generating plants. With clever use of thermodynamics and technology modern gas and steam turbines can be coupled to effect dramatic efficiency increases. These combined-cycle power plants now reach thermal efficiencies in excess of 0.60. It is shown how the laws of thermodynamics make this possible.

Harvey S. Leff

2012-01-01T23:59:59.000Z

103

Use and recovery of ammonia in power plant cycles  

SciTech Connect (OSTI)

The paper presents some practical and theoretical aspects of the use of ammonia in power plant water/steam cycles. The plants considered are fully automated units with once-through boilers, which operate under complex conditions and are subject to frequent starts and load changes. The boilers are chemically conditioned with combined oxygen ammonia treatment and the condensate polishing plant is only operated during start-up, in the event of a condenser leak or to remove excess ammonia. The paper also covers the recovery of ammonia from the condensate polishing plant waste regenerants and reuse for conditioning the feedwater. In particular, the paper deals with the following points: theoretical analysis of the chemical equilibrium of ammonia and carbon dioxide in water, including calculation of the concentrations from the parameters normally measured, such as conductivities and pH; equipment for monitoring and controlling the amount of ammonia fed to the water/steam cycle, including the optimum positioning of the sampling and feed-points, the parameters suitable for feed control and their temperature dependence; the partial pressure and distribution coefficient of ammonia; the consumption and losses of ammonia through the water/steam cycle during operation; the recovery of ammonia from condensate polishing plant waste regenerants by steam stripping. The paper should be of interest to both planning engineers and plant operators.

Pflug, H.D.; Bettenworth, H.J.; Syring, H.A. [Preussen Elektra AG, Hanover (Germany)

1995-01-01T23:59:59.000Z

104

Life Cycle Results from the IGCC LCI&C Study  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Results from the IGCC LCI&C Study Results from the IGCC LCI&C Study Robert E. James III, Timothy J. Skone Office of Systems, Analyses and Planning National Energy Technology Laboratory (NETL), U.S. DOE Revision 2, June 2013 DOE/NETL-2012/1551 ‹#› Conceptual Study Boundary Integrated Gasification Combined Cycle (IGCC) ‹#› LCA's Expanded Boundary for IGCC Mine Construction Train & Rail Manufacturing Plant Construction/ Installation Coal Extraction/ Operation Train Operation Mine Decommissioning Stage #1 Raw Material Acquisition Stage #2 Raw Material Transport Plant Operation Carbon Capture (CC), Operation CO 2 Pipeline, Operation CO 2 Sequestration, Operation Plant Decommissioning Construction & Installation Deinstallation Transmission & Distribution, Operation

105

Performance Diagnosis using Optical Torque Sensor for Selection of a Steam Supply Plant among Advanced Combined Cycle Power Plants  

Science Journals Connector (OSTI)

A newly developed optical torque sensor was applied to select a steam supply plant among advanced combined cycle, i.e. ACC, power plants of...

Shuichi Umezawa

2007-01-01T23:59:59.000Z

106

Weighing the Costs and Benefits of Renewables Portfolio Standards: A Comparative Analysis of State-Level Policy Impact Projections  

E-Print Network [OSTI]

integrated gasification combined cycle plants, and measuresrate of a new combined-cycle natural gas generator.displaces natural gas combined- cycle generation, and RPS

Chen, Cliff; Wiser, Ryan; Bolinger, Mark

2007-01-01T23:59:59.000Z

107

Japan's Long-term Energy Demand and Supply Scenario to 2050 - Estimation for the Potential of Massive CO2 Mitigation  

E-Print Network [OSTI]

of 1,500-degree-Celsius combined cycle plants. Oil thermalintegrated gasification combined cycle) and other highlyof 1,700-degree-Celsius combined cycle generation systems.

Komiyama, Ryoichi

2010-01-01T23:59:59.000Z

108

Assessing Vehicle Electricity Demand Impacts on California Electricity Supply  

E-Print Network [OSTI]

IGCC Integrated gasification combined cycle IID ImperialCorporation NGCC Natural gas combined-cycle NGCT Natural gas79% from natural gas combined cycle (NGCC) power plants, and

McCarthy, Ryan W.

2009-01-01T23:59:59.000Z

109

Steam turbines of the Ural Turbine Works for combined-cycle plants  

Science Journals Connector (OSTI)

Matters concerned with selecting the equipment for combined-cycle plants within the framework of work on ... Works regarding the supplies of steam turbines for combined-cycle plants used at retrofitted and newly ...

G. D. Barinberg; A. E. Valamin; A. Yu. Kultyshev; T. Yu. Linder

2009-09-01T23:59:59.000Z

110

DOE Science Showcase - Energy Plants of the Future | OSTI, US Dept of  

Office of Scientific and Technical Information (OSTI)

DOE Science Showcase - Energy Plants of the Future DOE Science Showcase - Energy Plants of the Future Advanced Integrated Gasification Combined Cycle Power Plants Advanced IGCC is a flexible technology for generating low-cost electricity while meeting all future environment requirements Secretary Chu Announces $14 Million for Six New Projects to Advance IGCC Technology DOE Press Release DOE-Sponsored IGCC Project in Texas Takes Important Step Forward, Fossil Energy Techline Gasification Technology R&D How Coal Gasification Power Plants Work 2010 Worldwide Gasification Database Follow NETL Gasification IGCC Research in DOE Databases Energy Citations Database Information Bridge Science.gov WorldWideScience.org Visit the Science Showcase homepage. OSTI Homepage Mobile Gallery Subscribe to RSS OSTI Blog Get Widgets Get Alert Services

111

Advanced Feed Water and Cooling Water Treatment at Combined Cycle Power Plant  

Science Journals Connector (OSTI)

Tokyo Gas Yokosuka Power Station is an IPP combined cycle power plant supplied by Fuji Electric Systems...

Ryo Takeishi; Kunihiko Hamada; Ichiro Myogan…

2007-01-01T23:59:59.000Z

112

DOE Awards $235 Million to Southern Company to Build Clean Coal Plant |  

Broader source: Energy.gov (indexed) [DOE]

235 Million to Southern Company to Build Clean Coal 235 Million to Southern Company to Build Clean Coal Plant DOE Awards $235 Million to Southern Company to Build Clean Coal Plant February 22, 2006 - 12:13pm Addthis WASHINGTON , DC - The U.S. Department of Energy awarded $235 million to Southern Company, in partnership with the Orlando Utilities Commission and Kellogg, Brown and Root, to develop one of the cleanest coal-fired power plants in the world. Representatives of the Energy Department and Southern Company signed a cooperative agreement that launches the design, construction, and demonstration of an integrated gasification combined cycle (IGCC) power generation system at the Orlando Utilities Commission's Stanton Energy Center. The system will produce 285 megawatts of electricity for the Orlando area - which will power approximately 285,000 households - and is

113

Dynamic modeling of IGCC power plants  

Science Journals Connector (OSTI)

Integrated Gasification Combined Cycle (IGCC) power plants are an effective option to reduce emissions and implement carbon-dioxide sequestration. The combination of a very complex fuel-processing plant and a combined cycle power station leads to challenging problems as far as dynamic operation is concerned. Dynamic performance is extremely relevant because recent developments in the electricity market push toward an ever more flexible and varying operation of power plants. A dynamic model of the entire system and models of its sub-systems are indispensable tools in order to perform computer simulations aimed at process and control design. This paper presents the development of the lumped-parameters dynamic model of an entrained-flow gasifier, with special emphasis on the modeling approach. The model is implemented into software by means of the Modelica language and validated by comparison with one set of data related to the steady operation of the gasifier of the Buggenum power station in the Netherlands. Furthermore, in order to demonstrate the potential of the proposed modeling approach and the use of simulation for control design purposes, a complete model of an exemplary IGCC power plant, including its control system, has been developed, by re-using existing models of combined cycle plant components; the results of a load dispatch ramp simulation are presented and shortly discussed.

F. Casella; P. Colonna

2012-01-01T23:59:59.000Z

114

Future Impacts of Coal Distribution Constraints on Coal Cost  

E-Print Network [OSTI]

coal (PC) or integrated gasification combined cycle ( IGCC)coal (PC) or integrated gasification combined cycle (IGCC)will be integrated gasification combined cycle (IGCC) (Same

McCollum, David L

2007-01-01T23:59:59.000Z

115

Modular high temperature gas-cooled reactor plant design duty cycle. Revision 3  

SciTech Connect (OSTI)

This document defines the Plant Design Duty Cycle (PCDC) for the Modular High Temperature Gas-cooled Reactor (MHTGR). The duty cycle is a set of events and their design number of occurrences over the life of the plant for which the MHTGR plant shall be designed to ensure that the plant meets all the top-level requirements. The duty cycle is representative of the types of events to be expected in multiple reactor module-turbine plant configurations of the MHTGR. A synopsis of each PDDC event is presented to provide an overview of the plant response and consequence. 8 refs., 1 fig., 4 tabs.

Chan, T.

1989-12-31T23:59:59.000Z

116

Mathematical Modeling and Computer Simulation of a Combined Cycle Power Plant  

Science Journals Connector (OSTI)

This paper presents the simulation procedure developed to predict the performance of a combined cycle power plant from given performance characteristics of ... . Effects of gas turbine and steam turbine cycle par...

Nikhil Dev; Samsher; S. S. Kachhwaha; Mohit

2012-01-01T23:59:59.000Z

117

Proceedings: 7th International Conference on Cycle Chemistry in Fossil Plants  

SciTech Connect (OSTI)

The purity of boiler water, feedwater, and steam is central to ensuring component availability and reliability in fossil-fired plants. These proceedings of EPRI's Seventh International Conference on Cycle Chemistry in Fossil Plants address the state of the art in fossil plant and combined cycle/heat recovery steam generator (HRSG) cycle chemistry as well as international practices for corrosion control and water preparation and purification.

None

2004-02-01T23:59:59.000Z

118

Rankine cycle power plant with improved organic working fluid  

SciTech Connect (OSTI)

In a Rankine cycle power plant having a boiler for vaporizing an organic working fluid which is applied to a turbine in which vaporized working fluid produced by the boiler expands and produces work, a condenser for condensing expanded vaporized working fluid exhausted by the turbine and producing condensate, and means for returning the condensate to the boiler, the improvement is described comprising: (a) operating the boiler so that the organic fluid vaporizes at substantially constant pressure and a temperature not exceeding 400/sup 0/C; (b) applying only vaporized working fluid to the turbine; and (c) using as the working fluid, a compound selected from the group consisting of bicyclic hydrocarbons, substituted bicyclic aromatic hydrocarbons, heterobicyclic aromatic hydrocarbons, substituted heterobicyclic aromatic hydrocarbons, bicyclic compounds where one ring is aromatic and the other condensed ring is nonaromatic, and their mixtures.

Yogev, A.; Mahlab, D.

1988-08-02T23:59:59.000Z

119

Steam turbines produced by the Ural Turbine Works for combined-cycle plants  

Science Journals Connector (OSTI)

The most interesting and innovative solutions adopted in the projects of steam turbines for combined-cycle plants with capacities from...

A. E. Valamin; A. Yu. Kultyshev; T. L. Shibaev; A. A. Gol’dberg…

2013-08-01T23:59:59.000Z

120

The efficiency of technical retrofitting of cogeneration stations using combined-cycle plants  

Science Journals Connector (OSTI)

We consider the problem of technical retrofitting of gas-and-oil fired steam-turbine cogeneration stations by converting them into combined-cycle plants...

L. S. Popyrin; M. D. Dil’man; G. M. Belyaeva

2006-02-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


121

Constructing the Russian combined-cycle cogeneration plant and mastering its operation  

Science Journals Connector (OSTI)

The main results obtained from the development, construction, mastering, and operation of the PGU-450T combined-cycle power plant are described.

P. A. Berezinets; V. M. Grinenko; I. V. Dolinin; V. N. Kondrat’ev…

2011-06-01T23:59:59.000Z

122

Adaptive hybrid predictive control for a combined cycle power plant optimization .  

E-Print Network [OSTI]

??The design and development of an adaptive hybrid predictive controller for the optimization of a real combined cycle power plant (CCPP) are presented. The real… (more)

Sáez, D.

2008-01-01T23:59:59.000Z

123

Investigations of supercritical CO2 Rankine cycles for geothermal power plants  

SciTech Connect (OSTI)

Supercritical CO2 Rankine cycles are investigated for geothermal power plants. The system of equations that describe the thermodynamic cycle is solved using a Newton-Rhapson method. This approach allows a high computational efficiency of the model when thermophysical properties of the working fluid depend strongly on the temperature and pressure. Numerical simulation results are presented for different cycle configurations in order to assess the influences of heat source temperature, waste heat rejection temperatures and internal heat exchanger design on cycle efficiency. The results show that thermodynamic cycle efficiencies above 10% can be attained with the supercritical brayton cycle while lower efficiencies can be attained with the transcritical CO2 Rankine cycle.

Sabau, Adrian S [ORNL; Yin, Hebi [ORNL; Qualls, A L [ORNL; McFarlane, Joanna [ORNL

2011-01-01T23:59:59.000Z

124

Investigation of combined-cycle steam-plant problems. Final report  

SciTech Connect (OSTI)

The operation and maintenance of gas turbine combined-cycle steam generators is reviewed. Feedwater cycles and auxiliary equipment are also discussed, and the results of on-site discussions with operating and maintenance personnel are presented. Actual problems encountered are delineated, and recommendations are given for improving operation of existing plants, for design of new plants, and for future research and development.

Crutchfield, H.C.

1982-07-01T23:59:59.000Z

125

Natural Gas Weekly Update  

Annual Energy Outlook 2013 [U.S. Energy Information Administration (EIA)]

at multiple commercial-scale Integrated Gasification Combined Cycle (IGCC) clean coal power plants. The FutureGen concept announced in 2003 planned the creation of a...

126

Quantifying Uncertainty in Computer Predictions | netl.doe.gov  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

power plants. Advanced energy technologies such as Integrated Gasification Combined Cycle (IGCC) and Carbon Capture and Storage (CCS) can potentially lead to the...

127

novel-membranes-pitt-nd | netl.doe.gov  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

CO2 removal in reducing environments, such as those found in integrated gasification combined cycle (IGCC) power plant fuel gas streams or natural gas sweetening (NGS). In...

128

Next Generation Geothermal Power Plants (NGGPP) process data for binary cycle plants  

SciTech Connect (OSTI)

The Next Generation Geothermal Power Plants (NGGPP) study provides the firm estimates - in the public domain - of the cost and performance of U.S. geothermal systems and their main components in the early 1990s. The study was funded by the U.S. Department of Energy Geothermal Research Program, managed for DOE by Evan Hughes of the Electric Power Research Institute, Palo Alto, CA, and conducted by John Brugman and others of the CE Holt Consulting Firm, Pasadena, CA. The printed NGGPP reports contain detailed data on the cost and performance for the flash steam cycles that were characterized, but not for the binary cycles. The nine Tables in this document are the detailed data sheets on cost and performance for the air cooled binary systems that were studied in the NGGPP.

Not Available

1996-10-02T23:59:59.000Z

129

Thermodynamic evaluation of solar integration into a natural gas combined cycle power plant  

Science Journals Connector (OSTI)

Abstract The term integrated solar combined-cycle (ISCC) has been used to define the combination of solar thermal energy into a natural gas combined-cycle (NGCC) power plant. Based on a detailed thermodynamic cycle model for a reference ISCC plant, the impact of solar addition is thoroughly evaluated for a wide range of input parameters such as solar thermal input and ambient temperature. It is shown that solar hybridization into an NGCC plant may give rise to a substantial benefit from a thermodynamic point of view. The work here also indicates that a significant solar contribution may be achieved in an ISCC plant, thus implying substantial fuel savings and environmental benefits.

Guangdong Zhu; Ty Neises; Craig Turchi; Robin Bedilion

2015-01-01T23:59:59.000Z

130

Modeling of a Biomass Gasification CHP Plant: Influence of Various Parameters on Energetic and Exergetic Efficiencies  

Science Journals Connector (OSTI)

Modeling of a Biomass Gasification CHP Plant: Influence of Various Parameters on Energetic and Exergetic Efficiencies ... This paper presents a theoretical assessment of energy, exergy, and syngas cleaning performances in a biomass gasification combined heat and power (CHP) plant with varying operating parameters. ... The analysis is carried out using a detailed model of a biomass gasification CHP plant developed with Aspen Plus. ...

Jessica François; Guillain Mauviel; Michel Feidt; Caroline Rogaume; Yann Rogaume; Olivier Mirgaux; Fabrice Patisson; Anthony Dufour

2013-10-21T23:59:59.000Z

131

Notice of Availability for the Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project Final Environmental Impact Statement (12/13/02)  

Broader source: Energy.gov (indexed) [DOE]

740 740 Federal Register / Vol. 67, No. 240 / Friday, December 13, 2002 / Notices [FR Doc. 02-31431 Filed 12-12-02; 8:45 am] BILLING CODE 6450-01-C ENVIRONMENTAL PROTECTION AGENCY [ER-FRL-6635-7] Environmental Impact Statments; Notice of Availability Responsible Agency: Office of Federal Activities, General Information (202) 564-7167 or http://www.epa.gov/ compliance/nepa/. Weekly receipt of Environmental Impact Statements filed December 2, 2002, through December 6, 2002. Pursuant to 40 CFR 1506.9. EIS No. 020498, Draft EIS, SFW, WA, Daybreak Mine Expansion and Habitat Enhancement Project, Habitat Conservation Plan, Issuance of a Multiple Species Permit for Incidental Take, Implementation, Clark County, WA , Comment Period Ends: February 21, 2003. Contact: Tim Romanski

132

Power Systems Life Cycle Analysis Tool (Power L-CAT).  

SciTech Connect (OSTI)

The Power Systems L-CAT is a high-level dynamic model that calculates levelized production costs and tracks environmental performance for a range of electricity generation technologies: natural gas combined cycle (using either imported (LNGCC) or domestic natural gas (NGCC)), integrated gasification combined cycle (IGCC), supercritical pulverized coal (SCPC), existing pulverized coal (EXPC), nuclear, and wind. All of the fossil fuel technologies also include an option for including carbon capture and sequestration technologies (CCS). The model allows for quick sensitivity analysis on key technical and financial assumptions, such as: capital, O&M, and fuel costs; interest rates; construction time; heat rates; taxes; depreciation; and capacity factors. The fossil fuel options are based on detailed life cycle analysis reports conducted by the National Energy Technology Laboratory (NETL). For each of these technologies, NETL's detailed LCAs include consideration of five stages associated with energy production: raw material acquisition (RMA), raw material transport (RMT), energy conversion facility (ECF), product transportation and distribution (PT&D), and end user electricity consumption. The goal of the NETL studies is to compare existing and future fossil fuel technology options using a cradle-to-grave analysis. The NETL reports consider constant dollar levelized cost of delivered electricity, total plant costs, greenhouse gas emissions, criteria air pollutants, mercury (Hg) and ammonia (NH3) emissions, water withdrawal and consumption, and land use (acreage).

Andruski, Joel; Drennen, Thomas E.

2011-01-01T23:59:59.000Z

133

The thermodynamic efficiency of the condensing process circuits of binary combined-cycle plants with gas-assisted heating of cycle air  

Science Journals Connector (OSTI)

The thermal efficiencies of condensing-type circuits of binary combined-cycle plants containing one, two, and three ... gas turbine unit, and with preheating of cycle air are analyzed by way of comparison ... ini...

V. P. Kovalevskii

2011-09-01T23:59:59.000Z

134

Coordinated optimization of the parameters of the cooled gas-turbine flow path and the parameters of gas-turbine cycles and combined-cycle power plants  

Science Journals Connector (OSTI)

In the present paper, we evaluate the effectiveness of the coordinated solution to the optimization problem for the parameters of cycles in gas turbine and combined cycle power plants and to the optimization prob...

A. M. Kler; Yu. B. Zakharov; Yu. M. Potanina

2014-06-01T23:59:59.000Z

135

Life-cycle analysis results for geothermal systems in comparison to other power systems: Part II.  

SciTech Connect (OSTI)

A study has been conducted on the material demand and life-cycle energy and emissions performance of power-generating technologies in addition to those reported in Part I of this series. The additional technologies included concentrated solar power, integrated gasification combined cycle, and a fossil/renewable (termed hybrid) geothermal technology, more specifically, co-produced gas and electric power plants from geo-pressured gas and electric (GPGE) sites. For the latter, two cases were considered: gas and electricity export and electricity-only export. Also modeled were cement, steel and diesel fuel requirements for drilling geothermal wells as a function of well depth. The impact of the construction activities in the building of plants was also estimated. The results of this study are consistent with previously reported trends found in Part I of this series. Among all the technologies considered, fossil combustion-based power plants have the lowest material demand for their construction and composition. On the other hand, conventional fossil-based power technologies have the highest greenhouse gas (GHG) emissions, followed by the hybrid and then two of the renewable power systems, namely hydrothermal flash power and biomass-based combustion power. GHG emissions from U.S. geothermal flash plants were also discussed, estimates provided, and data needs identified. Of the GPGE scenarios modeled, the all-electric scenario had the highest GHG emissions. Similar trends were found for other combustion emissions.

Sullivan, J.L.; Clark, C.E.; Yuan, L.; Han, J.; Wang, M. (Energy Systems)

2012-02-08T23:59:59.000Z

136

Thermodynamic analysis of a closed-cycle, solar gas-turbine plant  

Science Journals Connector (OSTI)

Thermodynamic analysis of a closed-cycle, Brayton gas-turbine plant with a heat exchanger powered by the sun has been studied. A Brayton cycle is simpler than a Rankine cycle and has an advantage in places where water is scarce and expensive. A simple expression is derived for calculating the efficiency of the cycle in terms of the compression pressure ratio, the pressure loss coefficient and the ratio of the lower to higher temperature in the cycle with the efficiency of various components. The maximum permissible pressure loss coefficient has also been calculated.

P. Gandhidasan

1993-01-01T23:59:59.000Z

137

Optimizing the start-up operations of combined cycle power plants using soft computing methods  

Science Journals Connector (OSTI)

......Fast Start-up of a Combined-Cycle Power Plant: a Simulation Study with Modelica. In: Proceedings 5th International Modelica Conference (2006) 3-10. Modelica Association eds. [4] Zimmerman HJ . Fuzzy set theory (1991) Kluwer Academic......

Ilaria Bertini; Matteo De Felice; Alessandro Pannicelli; Stefano Pizzuti

2012-08-01T23:59:59.000Z

138

Investigation of coal fired combined-cycle cogeneration plants for power, heat, syngas, and hydrogen  

Science Journals Connector (OSTI)

The methodology for determination of technical and economic efficiency of coal fired combined-cycle cogeneration plant (CCCP) with low-pressure ... steam-gas generator and continuous flow gasifier at combined pro...

V. E. Nakoryakov; G. V. Nozdrenko; A. G. Kuzmin

2009-12-01T23:59:59.000Z

139

Fuzzy Optimization of Start-Up Operations for Combined Cycle Power Plants  

Science Journals Connector (OSTI)

In this paper we present a study on the application of fuzzy sets for the start-up optimisation of a combined cycle power plant. We fuzzyfy the output process variables and then we properly combine the resulting ...

Ilaria Bertini; Alessandro Pannicelli…

2010-01-01T23:59:59.000Z

140

Steam turbines of the Ural Turbine Works for advanced projects of combined-cycle plants  

Science Journals Connector (OSTI)

We describe the design features, basic thermal circuits, and efficiency of steam turbines developed on the basis of serially produced steam turbines of Ural Turbine Works and used as part of combined-cycle plants...

G. D. Barinberg; A. E. Valamin; A. Yu. Kultyshev

2009-09-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


141

Discussion of the Key Problems on Designing 350 MW-Class Combined Cycle Power Plant  

Science Journals Connector (OSTI)

With adjustment of energy structure and enhancement of environmental protection standard, gas-steam combined cycle power plants will be erupt gradually, especially...gas being moved from WEST to EAST and liquefie...

Tai Lu; Sike Hu; Wenrui Wu

2007-01-01T23:59:59.000Z

142

Optimization of a Combined-Cycle Plant with Thermodynamic, Economic and Environmental Considerations  

Science Journals Connector (OSTI)

Environmental considerations are combined with thermodynamics and economics for the design optimization of a double-pressure combined-cycle plant, which produces electricity. Two pollutants...2 and NOX, and a pen...

Christos A. Frangopoulos; Vasilios A. Bulmetis

1993-01-01T23:59:59.000Z

143

AVESTAR Center for operational excellence of clean energy plants and DYNSIM OTS / EyeSim ITS integration  

SciTech Connect (OSTI)

This Power-Point presentation with notes starts with a brief overview of US energy challenging, particularly as regards power generation capacity and clean energy plant operations. It then goes on to present Advanced Virtual Energy Simulation Training And Research (AVESTAR{trademark}) beginning with a statement of its missions and goals, then moves to the subject of Integrated Gasification Combined Cycle (IGCC) with CO{sub 2} Capture, first providing a brief overview of the process, then moving on to Dynamic Simulator/Operator Training System (OTS) and 3D Virtual Immersive Training System (ITS). The presentation continues to describe AVESTAR center facilities, locations, and training systems and to look at future directions for virtual energy simulation.

Provost, G.

2012-01-01T23:59:59.000Z

144

Chapter 11 - Germination Ecology of Plants with Specialized Life Cycles and/or Habitats  

Science Journals Connector (OSTI)

The germination ecology of parasitic plants, myco-heterotrophic plants, orchids, carnivorous plants, aquatics, halophytes or psammophytes is approached from a global perspective because these kinds of plants generally occur in more than one vegetation zone. These groups of plants have unusual life cycles and/or unique habitat requirements, and they have long attracted much attention from botanists, ecologists and other scientists. This chapter surveys the kinds of dormancy found in freshly-matured seeds in each of the seven groups of plants, and it considers available data on the environmental conditions required to break dormancy and stimulate germination.

Carol C. Baskin; Jerry M. Baskin

2014-01-01T23:59:59.000Z

145

Diagrams of regimes of cogeneration steam turbines for combined-cycle power plants  

Science Journals Connector (OSTI)

General considerations regarding the form of the steam-consumption diagram for a three-loop cogeneration-type combined-cycle plant are formulated on the basis of ... 12.4 steam turbine for the PGU-410 combined-cycle

A. Yu. Kultyshev; M. Yu. Stepanov; T. Yu. Linder

2012-12-01T23:59:59.000Z

146

Electric power generating plant having direct-coupled steam and compressed-air cycles  

DOE Patents [OSTI]

An electric power generating plant is provided with a Compressed Air Energy Storage (CAES) system which is directly coupled to the steam cycle of the generating plant. The CAES system is charged by the steam boiler during off peak hours, and drives a separate generator during peak load hours. The steam boiler load is thereby levelized throughout an operating day.

Drost, M.K.

1981-01-07T23:59:59.000Z

147

Electric power generating plant having direct coupled steam and compressed air cycles  

DOE Patents [OSTI]

An electric power generating plant is provided with a Compressed Air Energy Storage (CAES) system which is directly coupled to the steam cycle of the generating plant. The CAES system is charged by the steam boiler during off peak hours, and drives a separate generator during peak load hours. The steam boiler load is thereby levelized throughout an operating day.

Drost, Monte K. (Richland, WA)

1982-01-01T23:59:59.000Z

148

Combined-cycle gas and steam turbine power plants. 2. edition  

SciTech Connect (OSTI)

First published in 1991, this book is the leading reference on technical and economic factors of combined-cycle applications now leading the trend toward merchant plants and the peaking power needed in newly deregulated markets around the world, this long-awaited second edition is more important than ever. In it, Kehlhofer -- an internationally recognized authority in the field of new combined-cycle power plants -- and his co-authors widen the scope and detail found in the first edition. Included are tips on system layout, details on controls and automation, and operating instructions. Loaded with case studies, reference tables, and more than 150 figures, this text offers solid advice on system layout, controls and automation, and operating and maintenance instructions. The author provides real-world examples to apply to one`s own applications. The contents include: Introduction; The electricity market; Thermodynamic principles of combined-cycle plants; Combined-cycle concepts; Applications of combined-cycle; Components; Control and automation; Operating and part load behavior; Environmental considerations; Developmental trends; Typical combined-cycle plants already built; Conclusion; Appendices; Conversions; Calculation of the operating performance of combined-cycle installations; Definitions of terms and symbols; Bibliography; and Index.

Kehlhofer, R.; Bachmann, R.; Nielson, H.; Warner, J.

1999-01-01T23:59:59.000Z

149

Raft River binary-cycle geothermal pilot power plant final report  

SciTech Connect (OSTI)

The design and performance of a 5-MW(e) binary-cycle pilot power plant that used a moderate-temperature hydrothermal resource, with isobutane as a working fluid, are examined. Operating problems experienced and solutions found are discussed and recommendations are made for improvements to future power plant designs. The plant and individual systems are analyzed for design specification versus actual performance figures.

Bliem, C.J.; Walrath, L.F.

1983-04-01T23:59:59.000Z

150

Selective Exhaust Gas Recycle with Membranes for CO2 Capture from Natural Gas Combined Cycle Power Plants  

Science Journals Connector (OSTI)

The combination of the combustion turbine (Brayton cycle) and steam turbine (Rankine cycle) yields a combined cycle power plant with efficiencies as high as 50%–55% (compared to 35%–40% in a typical subcritical pulverized coal power plant). ... Of course, it is also possible to combine these designs so that both parallel and series membranes are used. ...

Timothy C. Merkel; Xiaotong Wei; Zhenjie He; Lloyd S. White; J. G. Wijmans; Richard W. Baker

2012-11-27T23:59:59.000Z

151

Comparative Analysis of Alternative Configurations of the Mercury 50 Recuperated Gas-Turbine-Based Biomass Integrated Gasification Combined Heat and Power (BIGCHP) Plant  

Science Journals Connector (OSTI)

In this paper, several original configurations of the cogeneration system based on different gasification technologies and Mercury 50 recuperated gas turbine are proposed and examined theoretically. ... (14) Another key problem of the successful commercialization of the technology is the commercial availability of reliable and efficient gas turbines (GTs) modified for syngas operation. ... In particular, the paper presents current development status and design challenges being addressed by Siemens Westinghouse Power Corp. for large industrial engines (>200 MW) and by Solar Turbines for smaller engines (Turbine Systems (ATS) program. ...

Jacek Kalina

2011-11-29T23:59:59.000Z

152

VOC Emission Control with the Brayton Cycle Pilot Plant Operations  

E-Print Network [OSTI]

A mobile pilot plant capable of removing VOC emissions from exhaust air streams was cooperatively funded by SCE, EPRI, 3M, and NUCON. Valuable information about the process and the recovery operation has been gained by performing tests at a number...

Enneking, J. C.

153

Mechanisms of plant species impacts on ecosystem nitrogen cycling  

E-Print Network [OSTI]

, this microbial nitrogen loop is driven by plant-supplied carbon and provides a strong negative feedback through by an increase in the relative nitrogen content in decomposing litter and a much lower carbon-to-nitrogen ratio by a microbial nitrogen loop. Nitrogen is released from the soil organic matter and incorporated into microbial

Minnesota, University of

154

Binary Cycle Geothermal Demonstration Power Plant New Developments  

SciTech Connect (OSTI)

San Diego Gas and Electric Company (SDG and E) has been associated with geothermal exploration and development in the Imperial Valley since 1971. SDG and E currently has interests in the four geothermal reservoirs shown. Major SDG and E activities have included drilling and flow testing geothermal exploration wells, feasibility and process flow studies, small-scale field testing of power processes and equipment, and pilot plant scale test facility design, construction and operation. Supporting activities have included geothermal leasing, acquisition of land and water rights, pursual of a major new transmission line to carry Imperial Valley geothermal and other sources of power to San Diego, and support of Magma Electric's 10 MW East Mesa Geothermal Power Plant.

Lacy, Robert G.; Jacobson, William O.

1980-12-01T23:59:59.000Z

155

Task report No. 3. Systems analysis of organic Rankine bottoming cycles. [Fuel cell power plant  

SciTech Connect (OSTI)

A model was developed that predicts the design performance and cost of a Fuel Cell/Rankine cycle powerplant. The Rankine cycle utilizes the rejected heat of an 11.3 MW phosphoric acid fuel cell powerplant. Improvements in the total plant heat rate and efficiency of up to 10% were attainalbe, using ammonia as the working fluid. The increase in total plant cost divided by the increase in total plant power ranged from $296/kW to $1069/kW for the cases run, and was a strong function of ambient temperature. The concept appears to be capable of producing substantial energy savings in large fuel cell powerplants, at reasonable costs. However, a much more detailed study that includes such factors as duty cycle, future cost of fuel and site meteorology needs to be done to prove the design for any potential site.

Bloomfield, D.; Fried, S.

1980-12-01T23:59:59.000Z

156

Exergetic analysis and evaluation of coal-fired supercritical thermal power plant and natural gas-fired combined cycle power plant  

Science Journals Connector (OSTI)

The present work has been undertaken for energetic and exergetic analysis of coal-fired supercritical thermal power plant and natural gas-fired combined cycle power plant. Comparative analysis has been conducted ...

V. Siva Reddy; S. C. Kaushik; S. K. Tyagi

2014-03-01T23:59:59.000Z

157

Using energy balances for processing the results from tests of a single-shaft combined-cycle power plant  

Science Journals Connector (OSTI)

Application of the balance method for dividing the overall power output produced by a single-shaft combined-cycle power plant between the steam turbine and...

G. G. Ol’khovskii

2012-09-01T23:59:59.000Z

158

A new Rankine cycle for hydrogen-fired power generation plants and its exergetic efficiency  

Science Journals Connector (OSTI)

A novel power generation cycle is proposed in this paper taking hydrogen as fuel and using steam generated by hydrogen firing as working fluid. The progress of the development work and side issues such as the application of hydrogen combustion turbines to environmentally clean fossil fuel power plants for early commercialisation of the system are reviewed. We propose the hydrogen-fired Rankine cycle as similar to (C) type developed earlier by Hisadome et al. and Sugishita et al. and then making a new design of it by increasing the performance characteristics and efficiencies with (reheating, regenerative and recuperation) of the working fluid of the bottoming cycle respectively, and in this case we present two types (C1 and C2). In the case of type C2 the cycle is called the ''New Rankine Cycle''. These cycles are also compared with the Rankine cycle of type (C) for hydrogen-fired to show the advantages of the performance characteristics of the new design at which the highest value of exergetic efficiency reaches 63.58% as HHV at 1700°C of the combustor discharge temperature. These cycles are analysed through thermodynamics, particularly by exergy analysis, and the performance characteristics of the cycles are also studied.

Mohammed Ghiyath Soufi; Terushige Fujii; Katsumi Sugimoto; Hitoshi Asano

2004-01-01T23:59:59.000Z

159

Heber binary-cycle geothermal demonstration power plant: Startup and low-power testing: Special report  

SciTech Connect (OSTI)

In 1974 the geothermal industry recognized the need for binary cycle technology in the development of moderate temperature geothermal resources. The electric utilities further expressed a need to demonstrate the technology on a scale representative of commercial operation in order to resolve issues of performance cost and environmental acceptability, and to confirm the maturity of the technology. In response to the needs, EPRI conducted feasibility studies and a series of field experiments intended to culminate with the construction and demonstration of a nominal 50 MWe binary cycle power plant in cooperation with other interested organizations. The early work by EPRI, the Department of Energy and the San Diego Gas and Electric Company led to the formation of the present multi-sponsored project in late 1980. Construction of the demonstration plant was completed in June 1985 at the Heber geothermal field in the Imperial Valley of Southern California. The plant is rated at 46 MWe and converts the thermal energy from 360 F (182 C) geothermal fluid to electricity. Start-up of the plant was completed in December 1985 and the first extended run at low power was completed in June 1986. The results from this run and other tests associated with the plant and the geothermal production facilities during this period are contained in this report. During this period, the brine supply was lower than expected and the reinjection pressure higher than expected. The power cycle performed essentially as projected for the load levels at which the plant was tested.

Berning, J.; Bigger, J.E.; Fishbaugher, J.

1987-10-01T23:59:59.000Z

160

Exergoeconomic analysis of a biomass post-firing combined-cycle power plant  

Science Journals Connector (OSTI)

Abstract Biomass can be converted thermo- and bio-chemically to solid, liquid and gaseous biofuels. In this paper, energy, exergy and exergoeconomic analyses are applied to a biomass integrated post-firing combined-cycle power plant. The energy and exergy efficiencies of the cycle are found to be maximized at specific compressor pressure ratio values, and that higher pressure ratios reduce the total unit product cost. Increasing the gas turbine inlet temperature and decreasing the compressor pressure ratio decreases the CO2 mole fraction exiting the power plant. The exergoeconomic factor for the biomass integrated post-firing combined-cycle power plant at the optimum energy/exergy efficiency is 0.39. This implies that the major cost rate of this power plant configuration is attributable to the exergy destruction cost rate. Increasing the compressor pressure ratio decreases the mass of air per mass of steam in the power plant, implying a reduction in the gas turbine plant size. Increasing both the compressor pressure ratio and the heat recovery steam generator inlet gas temperature increases the capital investment cost compared with the exergy destruction cost. However, increasing the gas turbine inlet temperature decreases this ratio.

Hassan Athari; Saeed Soltani; Seyed Mohammad Seyed Mahmoudi; Marc A. Rosen; Tatiana Morosuk

2014-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


161

Operating experience of single cylinder steam turbine with 40 inch last blade applied for combined cycle plant  

SciTech Connect (OSTI)

Inquiries and orders for combined cycle plant have increased recently because of the better efficiency of combined cycle plant in comparison with the usual fossil fuel power plant. The typical features of the steam turbine for combined cycle plant are the lower inlet steam conditions and the more driving steam flow quantity compared with the steam turbine for usual fossil fuel plants. This paper introduces the design and results of operation about 122 MW single cylinder steam turbine. Furthermore, the results of periodical overhaul inspection carried out after one year`s commercial operation is also presented.

Kishimoto, Masaru; Yamamoto, Tetsuya [Mitsubishi Heavy Industries, Ltd., Yokohama (Japan); Yokota, Hiroshi [Mitsubishi Heavy Industries, Ltd., Nagasaki (Northern Mariana Islands); Umaya, Masahide [Mitsubishi Heavy Industries, Ltd., Takasago (Japan)

1994-12-31T23:59:59.000Z

162

Altheim geothermal Plant for electricity production by Organic Rankine Cycle turbogenerator  

SciTech Connect (OSTI)

The paper describes the plan of the town Altheim in Upper Austria to produce electricity by an Organic Rankine Cycle-turbogenerator in the field of utilization of low temperatured thermal water. The aim of the project is to improve the technical and economic situation of the geothermal plant.

Pernecker, Gerhard; Ruhland, Johannes

1996-01-24T23:59:59.000Z

163

Altheim geothermal plant for electricity production by organic Rankine cycle turbogenerator  

SciTech Connect (OSTI)

The paper describes the plan of the town Altheim in Upper Austria to produce electricity by an Organic Rankine Cycle-turbogenerator in the field of utilization of low temperatured thermal water. The aim of the project is to improve the technical and economic situation of the geothermal plant.

Pernecker, G. [Municipality of Altheim (Austria); Ruhland, J. [TERRAWAT GmbH, Schwaben (Germany)

1996-12-31T23:59:59.000Z

164

Method of optimizing performance of Rankine cycle power plants. [US DOE Patent  

DOE Patents [OSTI]

A method is described for efficiently operating a Rankine cycle power plant to maximize fuel utilization efficiency or energy conversion efficiency or minimize costs by selecting a turbine fluid inlet state which is substantially on the area adjacent and including the transposed critical temperature line.

Pope, W.L.; Pines, H.S.; Doyle, P.A.; Silvester, L.F.

1980-06-23T23:59:59.000Z

165

Optimization of Fog Inlet Air Cooling System for Combined Cycle Power Plants using Genetic Algorithm  

Science Journals Connector (OSTI)

Abstract In this research paper, a comprehensive thermodynamic modeling of a combined cycle power plant is first conducted and the effects of gas turbine inlet fogging system on the first and second law efficiencies and net power outputs of combined cycle power plants are investigated. The combined cycle power plant (CCPP) considered for this study consist of a double pressure heat recovery steam generator (HRSG) to utilize the energy of exhaust leaving the gas turbine and produce superheated steam to generate electricity in the Rankine cycle. In order to enhance understanding of this research and come up with optimum performance assessment of the plant, a complete optimization is using a genetic algorithm conducted. In order to achieve this goal, a new objective function is defined for the system optimization including social cost of air pollution for the power generation systems. The objective function is based on the first law efficiency, energy cost and the external social cost of air pollution for an operational system. It is concluded that using inlet air cooling system for the CCPP system and its optimization results in an increase in the average output power, first and second law efficiencies by 17.24%, 3.6% and 3.5%, respectively, for three warm months of year.

Mehdi A. Ehyaei; Mojtaba Tahani; Pouria Ahmadi; M. Esfandiari

2014-01-01T23:59:59.000Z

166

NREL: News - NREL Calculates Emissions and Costs of Power Plant Cycling  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

013 013 NREL Calculates Emissions and Costs of Power Plant Cycling Necessary for Increased Wind and Solar in the West September 24, 2013 New research from the Energy Department's National Renewable Energy Laboratory (NREL) quantifies the potential impacts of increasing wind and solar power generation on the operators of fossil-fueled power plants in the West. To accommodate higher amounts of wind and solar power on the electric grid, utilities must ramp down and ramp up or stop and start conventional generators more frequently to provide reliable power for their customers - a practice called cycling. The study finds that the carbon emissions induced by more frequent cycling are negligible (<0.2%) compared with the carbon reductions achieved through the wind and solar power generation evaluated in the study. Sulfur dioxide

167

Carbon Dioxide Sequestration:  

Science Journals Connector (OSTI)

...known as integrated gasification combined cycle, or...and petro-chemical industries (Fig. 4). FIGURE...Schematic of an integrated gasification combined cycle (IGCC...CO2/y from a coal gasification plant in North Dakota...proportionally more solid waste and requires more chemicals...

Edward S. Rubin

168

Implications of Near-Term Coal Power Plant Retirement for SO2 and NOX and Life Cycle GHG Emissions  

Science Journals Connector (OSTI)

Implications of Near-Term Coal Power Plant Retirement for SO2 and NOX and Life Cycle GHG Emissions ... Life cycle GHG emissions were found to decrease by less than 4% in almost all scenarios modeled. ... Resulting changes in fuel use, life cycle greenhouse gas (GHG) emissions, and emissions of sulfur and nitrogen oxides are estimated. ...

Aranya Venkatesh; Paulina Jaramillo; W. Michael Griffin; H. Scott Matthews

2012-08-13T23:59:59.000Z

169

Life Cycle Greenhouse Gas Emissions of Coal-Fired Electricity Generation: Systematic Review and Harmonization  

SciTech Connect (OSTI)

This systematic review and harmonization of life cycle assessments (LCAs) of utility-scale coal-fired electricity generation systems focuses on reducing variability and clarifying central tendencies in estimates of life cycle greenhouse gas (GHG) emissions. Screening 270 references for quality LCA methods, transparency, and completeness yielded 53 that reported 164 estimates of life cycle GHG emissions. These estimates for subcritical pulverized, integrated gasification combined cycle, fluidized bed, and supercritical pulverized coal combustion technologies vary from 675 to 1,689 grams CO{sub 2}-equivalent per kilowatt-hour (g CO{sub 2}-eq/kWh) (interquartile range [IQR]= 890-1,130 g CO{sub 2}-eq/kWh; median = 1,001) leading to confusion over reasonable estimates of life cycle GHG emissions from coal-fired electricity generation. By adjusting published estimates to common gross system boundaries and consistent values for key operational input parameters (most importantly, combustion carbon dioxide emission factor [CEF]), the meta-analytical process called harmonization clarifies the existing literature in ways useful for decision makers and analysts by significantly reducing the variability of estimates ({approx}53% in IQR magnitude) while maintaining a nearly constant central tendency ({approx}2.2% in median). Life cycle GHG emissions of a specific power plant depend on many factors and can differ from the generic estimates generated by the harmonization approach, but the tightness of distribution of harmonized estimates across several key coal combustion technologies implies, for some purposes, first-order estimates of life cycle GHG emissions could be based on knowledge of the technology type, coal mine emissions, thermal efficiency, and CEF alone without requiring full LCAs. Areas where new research is necessary to ensure accuracy are also discussed.

Whitaker, M.; Heath, G. A.; O'Donoughue, P.; Vorum, M.

2012-04-01T23:59:59.000Z

170

Heber Binary-Cycle Geothermal Demonstration Power Plant: Half-load testing, performance, and thermodynamics  

SciTech Connect (OSTI)

This report describes the project's activities during the period July 1986 through June 1987; and includes results of two annual outages and eight months of low power testing and operating. The Heber Binary-Cycle Geothermal Demonstration Power Plant is a 45 MWe electric power generating plant in the Imperial Valley of Southern California. The purpose of the Heber Binary Project is to demonstrate the capability of binary-cycle technology to economically utilize moderate-temperature (300/degree/F to 410/degree/F (150/degree/C to 210/degree/C)) geothermal resources for electric power production. The main objective of the project is to show performance, cost, and environmental acceptability of binary-cycle technology. Experience with demonstration plant and heat supply facilities is described. Details of equipment problems are included. Heat supply shortfall prevented the planned ascent to full power, but binary-cycle experience was favorable at power levels up to 50% of design. 68 refs., 80 figs., 34 tabs.

Berning, J.L.; Fishbaugher, J.R.

1988-08-01T23:59:59.000Z

171

Co-gasification of coal–petcoke and biomass in the Puertollano IGCC power plant  

Science Journals Connector (OSTI)

Abstract Integrated Gasification Combined Cycle plants (IGCC) are efficient power generation systems with low pollutants emissions. Moreover, the entrained flow gasifier of IGCC plants allows the combined use of other lower cost fuels (biomass and waste) together with coal. Co-firing with biomass is beneficial for the reduction of CO2 emissions of fossil source. In this paper the results of co-gasification tests with two types of biomass deriving from agricultural residues, namely 2% and 4% by weight of olive husk and grape seed meal, in the 335 MWeISO IGCC power plant of ELCOGAS in Puertollano (Spain) are reported. No significant change in the composition of both the raw syngas and the clean syngas was observed. Furthermore, a process simulation model of the IGCC plant of Puertollano was developed and validated with available industrial data. The model was used to assess the technical and economic feasibility of the process co-fired with higher biomass contents up to 60% by weight. The results indicate that a 54% decrease of fossil CO2 emissions implies an energy penalty (a loss of net power) of about 20% while does not cause significant change of the net efficiency of the plant. The mitigation cost (the additional cost of electricity per avoided ton of CO2) is significantly dependent on the price of the biomass cost compared to the price of the fossil fuel.

Daniele Sofia; Pilar Coca Llano; Aristide Giuliano; Mariola Iborra Hernández; Francisco García Peña; Diego Barletta

2014-01-01T23:59:59.000Z

172

A commercial project for private investments. Update of the 280 MW api Energia IGCC plant construction in central Italy.  

SciTech Connect (OSTI)

This paper has the aim to give a general overview of the api Energia IGCC project starting from the project background in 1992 and ending with the progress of construction. api Energia S.p.A., a joint VENTURE between api anonima petroli italiana S.p.A., Roma, Italy (51%), ABB Sae Sadelmi S.p.A., Milano, Italy (25%) and Texaco Development Corporation (24%), is building a 280 MW Integrated Gasification Combined Cycle plant in the api refinery at Falconara Marittima, on Italy' s Adriatic coast, using heavy oil residues. The plant is based on the modern concept of employing a highly efficient combined cycle power plant fed with a low heating value fuel gas produced by gasifying heavy refinery residues. This scheme provides consistent advantages in terms of efficiency and environmental impact over alternative applications of the refinery residues. The electric power produced will feed the national grid. The project has been financed using the ``project financing'' scheme: over 1,000 billion Lira, representing 75% of the overall capital requirement, have been provided by a pool of international banks. In November 1996 the project reached financial closure and immediately after the detailed design and procurement activities started. Engineering, Procurement and Construction activities, carried out by a Consortium of companies of the ABB group, are totally in line with the schedule. Commercial operation of the plant, is scheduled for November 1999.

Del Bravo, R.; Pinacci, P.; Trifilo, R.

1998-07-01T23:59:59.000Z

173

Optimization of waste heat recovery boiler of a combined cycle power plant  

SciTech Connect (OSTI)

This paper describes the details of a procedure developed for optimization of a waste heat recovery boiler (WHRB) of a combined cycle power plant (CCPP) using the program for performance prediction of a typical CCPP, details of which have been presented elsewhere (Seyedan et al., 1994). In order to illustrate the procedure, the optimum design of a WHRB for a typical CCPP (employing dual-pressure bottoming cycle) built by a prominent Indian company, has been carried out. The present design of a WHRB is taken as the base design and the newer designs generated by this procedure are compared with it to assess the extent of cost reduction possible.

Seyedan, B.; Dhar, P.L.; Gaur, R.R. [Indian Inst. of Tech., New Delhi (India). Dept. of Mechanical Engineering; Bindra, G.S. [Bharat Heavy Electrical Ltd., New Delhi (India)

1996-07-01T23:59:59.000Z

174

Off-design performance of integrated waste-to-energy, combined cycle plants  

Science Journals Connector (OSTI)

This paper focuses on the off-design operation of plants where a waste-to-energy (WTE) system fed with municipal solid waste (MSW) is integrated with a natural gas-fired combined cycle (CC). Integration is accomplished by sharing the steam cycle: saturated steam generated in a MSW grate combustor is exported to the heat recovery steam generator (HRSG) of the combined cycle, where it is superheated and then fed to a steam turbine serving both the CC and the WTE plant. Most likely, the WTE section and the natural gas-fired CC section are subject to different operation and maintenance schedules, so that the integrated plant operates in conditions different from those giving full power output. In this paper we discuss and give performance estimates for the two situations that delimit the range of operating conditions: (a) WTE plant at full power and gas turbine down; (b) WTE plant down and gas turbine at full power. This is done for two integrated plants having the same WTE section, i.e. grate combustors with an overall MSW combustion power of 180 MWLHV, coupled with Combined Cycles based on two different heavy-duty gas turbines: a medium-size, 70 MW class turbine and a large-size, 250 MW class turbine. For each situation we discuss the control strategy and the actions that can help to achieve safe and reliable off-design operation. Heat and mass balances and performances at off-design conditions are estimated by accounting for the constraints imposed by the available heat transfer areas in boilers, heaters and condenser, as well as the characteristic curve of the steam turbine. When the gas turbine is down the net electric efficiency of the WTE section is very close to the one of the stand-alone WTE plant; instead, when the WTE section is down, the efficiency of the CC is much below the one of a stand alone CC. These performances appear most congenial to what is likely to be the operational strategy of these plants, i.e. paramount priority to waste treatment and CC dispatched according to the requirements of the national grid.

Stefano Consonni; Paolo Silva

2007-01-01T23:59:59.000Z

175

Chapter 4 - Natural Gas–fired Gas Turbines and Combined Cycle Power Plants  

Science Journals Connector (OSTI)

Abstract Gas turbines can burn a range of liquid and gaseous fuels but most burn natural gas. Power plants based on gas turbines are one of the cheapest types of plant to build, but the cost of their electricity depends heavily on the cost of their fuel. Two types of gas turbine are used for power generation: aero-derivative gas turbines and heavy-duty gas turbines. The former are used to provide power to the grid at times of peak demand. The latter are most often found in combined cycle power stations. These are capable of more than 60% efficiency. There are a number of ways of modifying the gas turbine cycle to improve efficiency, including reheating and intercooling. Micro-turbines have been developed for very small-scale generation of both electricity and heat. The main atmospheric emissions from gas turbines are carbon dioxide and nitrogen oxide.

Paul Breeze

2014-01-01T23:59:59.000Z

176

Tsiklauri-Durst combined cycle (T-D Cycle{trademark}) application for nuclear and fossil-fueled power generating plants  

SciTech Connect (OSTI)

The Tsiklauri-Durst combined cycle is a combination of the best attributes of both nuclear power and combined cycle gas power plants. A technology patented in 1994 by Battelle Memorial Institute offers a synergistic approach to power generation. A typical combined cycle is defined as the combination of gas turbine Brayton Cycle, topping steam turbine Rankine Cycle. Exhaust from the gas turbine is used in heat recovery steam generators to produce steam for a steam turbine. In a standard combined cycle gas turbine-steam turbine application, the gas turbine generates about 65 to 70 percent of system power. The thermal efficiency for such an installation is typically about 45 to 50 percent. A T-D combined cycle takes a new, creative approach to combined cycle design by directly mixing high enthalpy steam from the heat recovery steam generator, involving the steam generator at more than one pressure. Direct mixing of superheated and saturated steam eliminates the requirement for a large heat exchanger, making plant modification simple and economical.

Tsiklauri, B.; Korolev, V.N.; Durst, B.M.; Shen, P.K.

1998-07-01T23:59:59.000Z

177

Life-cycle energy and greenhouse gas emission impacts of different corn ethanol plant types.  

SciTech Connect (OSTI)

Since the United States began a program to develop ethanol as a transportation fuel, its use has increased from 175 million gallons in 1980 to 4.9 billion gallons in 2006. Virtually all of the ethanol used for transportation has been produced from corn. During the period of fuel ethanol growth, corn farming productivity has increased dramatically, and energy use in ethanol plants has been reduced by almost by half. The majority of corn ethanol plants are powered by natural gas. However, as natural gas prices have skyrocketed over the last several years, efforts have been made to further reduce the energy used in ethanol plants or to switch from natural gas to other fuels, such as coal and wood chips. In this paper, we examine nine corn ethanol plant types--categorized according to the type of process fuels employed, use of combined heat and power, and production of wet distiller grains and solubles. We found that these ethanol plant types can have distinctly different energy and greenhouse gas emission effects on a full fuel-cycle basis. In particular, greenhouse gas emission impacts can vary significantly--from a 3% increase if coal is the process fuel to a 52% reduction if wood chips are used. Our results show that, in order to achieve energy and greenhouse gas emission benefits, researchers need to closely examine and differentiate among the types of plants used to produce corn ethanol so that corn ethanol production would move towards a more sustainable path.

Wang, M.; Wu, M.; Huo, H.; Energy Systems

2007-04-01T23:59:59.000Z

178

Life-cycle energy and greenhouse gas emission impacts of different corn ethanol plant  

Science Journals Connector (OSTI)

Since the United States began a programme to develop ethanol as a transportation fuel, its use has increased from 175 million gallons in 1980 to 4.9 billion gallons in 2006. Virtually all of the ethanol used for transportation has been produced from corn. During the period of fuel ethanol growth, corn farming productivity has increased dramatically, and energy use in ethanol plants has been reduced by almost by half. The majority of corn ethanol plants are powered by natural gas. However, as natural gas prices have skyrocketed over the last several years, efforts have been made to further reduce the energy used in ethanol plants or to switch from natural gas to other fuels, such as coal and wood chips. In this paper, we examine nine corn ethanol plant types—categorized according to the type of process fuels employed, use of combined heat and power, and production of wet distiller grains and solubles. We found that these ethanol plant types can have distinctly different energy and greenhouse gas emission effects on a full fuel-cycle basis. In particular, greenhouse gas emission impacts can vary significantly—from a 3% increase if coal is the process fuel to a 52% reduction if wood chips are used. Our results show that, in order to achieve energy and greenhouse gas emission benefits, researchers need to closely examine and differentiate among the types of plants used to produce corn ethanol so that corn ethanol production would move towards a more sustainable path.

Michael Wang; May Wu; Hong Huo

2007-01-01T23:59:59.000Z

179

Engineering assessment of condenser deaeration retrofits for cycling fossil plants: Final report  

SciTech Connect (OSTI)

High dissolved oxygen levels in the condensate feedwater system contribute significantly to corrosion problems in steam generators, turbine rotor and blading, feedwater piping, feedwater heaters, and other plant equipment. While ingress of oxygen and oxidizing species into the condensate feedwater system cannot be completely eliminated due to a large number of potential air inleakage paths including air in-leakage into the condensate in the hotwell section of the condenser, oxygen levels could be kept to a minimum even at partial and no-load operation by improved condensate deaeration. The corrosion problems encountered in PWR plants, as well as those causing increased maintenance requirements and plant deterioration in cycling fossil plants are growing concerns to utilities. These concerns have motivated EPRI to investigate the causes and to seek remedies for the high dissolved oxygen levels that occur at start-up, low operating loads and shutdown. The purpose of this project was to develop the design, install and test three independent systems that could serve to reduce and maintain the low, dissolved oxygen content in the condensate of a peaking fossil unit under all operating conditions. If the results of the tests are favorable, the devices could be used at other peaking fossil plants and nuclear plants. 5 refs., 28 figs., 7 tabs.

Oliker, I.; Silaghy, F.; Lessley, R.

1988-01-01T23:59:59.000Z

180

Plant Design and Cost Assessment of Forced Circulation Lead-Bismuth Cooled Reactor with Conventional Power Conversion Cycles  

E-Print Network [OSTI]

Cost of electricity is the key factor that determines competitiveness of a power plant. Thus the proper selection, design and optimization of the electric power generating cycle is of main importance. This report makes an ...

Dostal, Vaclav

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
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181

Life cycle assessment of CO2 emissions from wind power plants: Methodology and case studies  

Science Journals Connector (OSTI)

Wind energy plays an increasingly important role in the world’s electricity market with rapid growth projected in the future. In order to evaluate the potential for wind energy to mitigate the effects of climate change by reducing CO2 intensity of the energy sector, this study developed a new direct and simple method for estimating CO2 emissions per kWh produced during the life cycle of four representative wind power plants (three in developed countries and one in China). The life cycle analysis focuses on the wind power plant as the basic functional object instead of a single wind turbine. Our results show that present-day wind power plants have a lifetime emission intensity of 5.0–8.2 g CO2/kWh electricity, a range significantly lower than estimates in previous studies. Our estimate suggests that wind is currently the most desirable renewable energy in terms of minimizing CO2 emissions per kWh of produced electricity. The production phase contributes the most to overall CO2 emissions, while recycling after decommission could reduce emissions by nearly half, representing an advantage of wind when compared with other energy generation technologies such as nuclear. Compared with offshore wind plants, onshore plants have lower CO2 emissions per kWh electricity and require less transmission infrastructure. Analysis of a case in China indicates that a large amount of CO2 emissions could be saved in the transport phase in large countries by using shorter alternative routes of transportation. As the world’s fastest growing market for wind power, China could potentially save 780 Mtons of CO2 emissions annually by 2030 with its revised wind development target. However, there is still ample room for even more rapid development of wind energy in China, accompanied by significant opportunities for reducing overall CO2 emissions.

Yuxuan Wang; Tianye Sun

2012-01-01T23:59:59.000Z

182

Exergetic analysis of solar concentrator aided natural gas fired combined cycle power plant  

Science Journals Connector (OSTI)

This article deals with comparative energy and exergetic analysis for evaluation of natural gas fired combined cycle power plant and solar concentrator aided (feed water heating and low pressure steam generation options) natural gas fired combined cycle power plant. Heat Transfer analysis of Linear Fresnel reflecting solar concentrator (LFRSC) is used to predict the effect of focal distance and width of reflector upon the reflecting surface area. Performance analysis of LFRSC with energetic and exergetic methods and the effect, of concentration ratio and inlet temperature of the fluid is carried out to determine, overall heat loss coefficient of the circular evacuated tube absorber at different receiver temperatures. An instantaneous increase in power generation capacity of about 10% is observed by substituting solar thermal energy for feed water heater and low pressure steam generation. It is observed that the utilization of solar energy for feed water heating and low pressure steam generation is more effective based on exergetic analysis rather than energetic analysis. Furthermore, for a solar aided feed water heating and low pressure steam generation, it is found that the land area requirement is 7 ha/MW for large scale solar thermal storage system to run the plant for 24 h.

V. Siva Reddy; S.C. Kaushik; S.K. Tyagi

2012-01-01T23:59:59.000Z

183

Renewable Energy and Efficiency Modeling Analysis Partnership: An Analysis of How Different Energy Models Addressed a Common High Renewable Energy Penetration Scenario in 2025  

E-Print Network [OSTI]

integrated gasification combined cycle Integrated Planningwith regard to the gas combined-cycle capacity around theas integrated gasification combined cycle (IGCC) and carbon

Blair, N.

2010-01-01T23:59:59.000Z

184

Economic development through biomass system integration. Volumes 2--4  

SciTech Connect (OSTI)

Report documents a feasibility study for an integrated biomass power system, where an energy crop (alfalfa) is the feedstock for a processing plant and a power plant (integrated gasification combined cycle) in a way that benefits the facility owners.

DeLong, M.M.

1995-10-01T23:59:59.000Z

185

Design of organic Rankine cycles for conversion of waste heat in a polygeneration plant .  

E-Print Network [OSTI]

??Organic Rankine cycles provide an alternative to traditional steam Rankine cycles for the conversion of low grade heat sources, where steam cycles are known to… (more)

DiGenova, Kevin (Kevin J.)

2011-01-01T23:59:59.000Z

186

The Combined Otto and Stirling Cycle Prime-Mover-Based Power Plant.  

E-Print Network [OSTI]

?? An exploratory study of the combined Otto and Stirling cycle prime mover is presented. The Stirling cycle acts as the bottoming cycle on the… (more)

Cullen, Barry, (Thesis)

2011-01-01T23:59:59.000Z

187

Study of Gas-steam Combined Cycle Power Plants Integrated with MCFC for Carbon Dioxide Capture  

Science Journals Connector (OSTI)

Abstract In the field of fossil-fuel based technologies, natural gas combined cycle (NGCC) power plants are currently the best option for electricity generation, having an efficiency close to 60%. However, they produce significant CO2 emissions, amounting to around 0.4 tonne/MWh for new installations. Among the carbon capture and sequestration (CCS) technologies, the process based on chemical absorption is a well-established technology, but markedly reduces the NGCC performances. On the other side, the integration of molten carbonate fuel cells (MCFCs) is recognized as an attractive option to overcome the main drawbacks of traditional CCS technologies. If the cathode side is fed by NGCC exhaust gases, the MCFC operates as a CO2 concentrator, beside providing an additional generating capacity. In this paper the integration of MCFC into a two pressure levels combined cycle is investigated through an energy analysis. To improve the efficiency of MCFC and its integration within the NGCC, plant configurations based on two different gas recirculation options are analyzed. The first is a traditional recirculation of exhaust gases at the compressor inlet; the second, mainly involving the MCFC stack, is based on recirculating a fraction of anode exhaust gases at the cathode inlet. Effects of MCFC operating conditions on energy and environmental performances of the integrated system are evaluated.

Roberto Carapellucci; Roberto Saia; Lorena Giordano

2014-01-01T23:59:59.000Z

188

Advanced Hydrogen Transport Membranes for Vision 21 Fossil Fuel Plants  

SciTech Connect (OSTI)

The objective of this project was to develop an environmentally benign, inexpensive, and efficient method for separating hydrogen from gas mixtures produced during industrial processes, such as coal gasification. A family of hydrogen separation membranes was developed including single phase mixed conducting ceramics, ceramic/ceramic composites, cermet membranes, cermet membranes containing a hydrogen permeable metal, and intermediate temperature composite layered membranes. Each membrane type had different operating parameters, advantages, and disadvantages that were documented over the course of the project. Research on these membranes progressed from ceramics to cermets to intermediate temperature composite layered membranes. During this progression performance was increased from 0.01 mL x min{sup -1} x cm{sup -2} up to 423 mL x min{sup -1} x cm{sup -2}. Eltron and team membranes not only developed each membrane type, but also membrane surface catalysis and impurity tolerance, creation of thin film membranes, alternative applications such as membrane promoted alkane dehydrogenation, demonstration of scale-up testing, and complete engineering documentation including process and mechanical considerations necessary for inclusion of Eltron membranes in a full scale integrated gasification combined cycle power plant. The results of this project directly led to a new $15 million program funded by the Department of Energy. This new project will focus exclusively on scale-up of this technology as part of the FutureGen initiative.

Carl R. Evenson; Shane E. Roark

2006-03-31T23:59:59.000Z

189

Life Cycle Assessment of district heat production in a straw fired CHP plant  

Science Journals Connector (OSTI)

Abstract Due to concerns about the sustainability of the energy sector, conversion of biomass to energy is increasing its hold globally. Life Cycle Impact Assessment (LCIA) is being adopted as an analytical tool to assess the environmental impacts in the entire cycle of biomass production and conversions to different products. This study deals with the LCIA of straw conversion to district heat in a Combined Heat and Power (CHP) plant and in a district heating boiler (producing heat only). Environmental impact categories are Global Warming Potential (GWP), Acidification Potential (AP), aquatic and terrestrial Eutrophication Potential (EP) and Non-Renewable Energy (NRE) use. In the case of CHP, the co-produced electricity is assumed to displace the marginal Danish electricity mix. The current study showed that straw fired in the CHP plant would lead to a GWP of ?187 g CO2-eq, AP 0.01 m2 UES (un-protected ecosystem), aquatic EP 0.16 g NO3-eq, terrestrial EP 0.008 m2 UES, and NRE use ?0.14 MJ-primary per 1 MJ heat production. Straw conversion to heat in the CHP plant showed better environmental performances compared to the district heating boiler. Furthermore, removing straw from the field is related to the consequence e.g. decline in soil carbon sequestration, limiting soil nutrient availability, and when compared with natural gas the conversion of straw to heat would lead to a higher aquatic and terrestrial EP and AP. The study also outlays spaces for the detail sustainability assessment of straw conversion in a biorefinery and compare with the current study.

Ranjan Parajuli; Søren Løkke; Poul Alberg Østergaard; Marie Trydeman Knudsen; Jannick H. Schmidt?; Tommy Dalgaard

2014-01-01T23:59:59.000Z

190

Soil–plant nitrogen cycling modulated carbon exchanges in a western temperate conifer forest in Canada  

Science Journals Connector (OSTI)

Nitrogen controls, on the seasonal and inter-annual variability of net ecosystem productivity (NEP) in a western temperate conifer forest in British Columbia, Canada, were simulated by a coupled carbon and nitrogen (C&N) model. The model was developed by incorporating plant–soil nitrogen algorithms in the Carbon-Canadian Land Surface Scheme (C-CLASS). In the coupled C&N-CLASS, the maximum carboxylation rate of Rubisco (Vcmax) is determined non-linearly from the modelled leaf Rubisco-nitrogen, rather than being prescribed. Hence, variations in canopy assimilation and stomatal conductance are sensitive to leaf nitrogen status through the Rubisco enzyme. The plant–soil nitrogen cycle includes nitrogen pools from photosynthetic enzymes, leaves and roots, as well as organic and mineral reservoirs from soil, which are generated, exchanged, and lost by biological fixation, atmospheric deposition, fertilization, mineralization, nitrification, root uptake, denitrification, and leaching. Model output was compared with eddy covariance flux measurements made over a 5-year period (1998–2002). The model performed very well in simulating half-hourly and monthly mean NEP values for a range of environmental conditions observed during the 5 years. C&N-CLASS simulated NEP values were 274, 437, 354, 352 and 253 g C m?2 for 1998–2002, compared to observed NEP values of 269, 360, 381, 418 and 264 g C m?2, for the respective years. Compared to the default C-CLASS, the coupled C&N model showed improvements in simulating the seasonal and annual dynamics of carbon fluxes in this forest. The nitrogen transformation to soil organic forms, mineralization, plant nitrogen uptake and leaf Rubisco-nitrogen concentration patterns were strongly influenced by seasonal and annual temperature variations. In contrast, the impact of precipitation was insignificant on the overall forest nitrogen budget. The coupled C&N modelling framework will help to evaluate the impact of nitrogen cycle on terrestrial ecosystems and its feedbacks on Earth's climate system.

M. Altaf Arain; Fengming Yuan; T. Andrew Black

2006-01-01T23:59:59.000Z

191

Life Cycle Assessment of a Parabolic Trough Concentrating Solar Power Plant and Impacts of Key Design Alternatives: Preprint  

SciTech Connect (OSTI)

Climate change and water scarcity are important issues for today's power sector. To inform capacity expansion decisions, hybrid life cycle assessment is used to evaluate a reference design of a parabolic trough concentrating solar power (CSP) facility located in Daggett, California, along four sustainability metrics: life cycle greenhouse gas (GHG) emissions, water consumption, cumulative energy demand (CED), and energy payback time (EPBT). This wet-cooled, 103 MW plant utilizes mined nitrate salts in its two-tank, thermal energy storage (TES) system. Design alternatives of dry-cooling, a thermocline TES, and synthetically-derived nitrate salt are evaluated. During its life cycle, the reference CSP plant is estimated to emit 26 g CO2eq per kWh, consume 4.7 L/kWh of water, and demand 0.40 MJeq/kWh of energy, resulting in an EPBT of approximately 1 year. The dry-cooled alternative is estimated to reduce life cycle water consumption by 77% but increase life cycle GHG emissions and CED by 8%. Synthetic nitrate salts may increase life cycle GHG emissions by 52% compared to mined. Switching from two-tank to thermocline TES configuration reduces life cycle GHG emissions, most significantly for plants using synthetically-derived nitrate salts. CSP can significantly reduce GHG emissions compared to fossil-fueled generation; however, dry-cooling may be required in many locations to minimize water consumption.

Heath, G. A.; Burkhardt, J. J.; Turchi, C. S.

2011-09-01T23:59:59.000Z

192

Load-following control of an IGCC plant with CO2 capture  

SciTech Connect (OSTI)

In this paper, a decentralized control strategy is considered for load-following control of an integrated gasification combined cycle (IGCC) plant with CO2 capture without flaring the syngas. The control strategy considered is gas turbine (GT) lead with gasifier follow. In this strategy, the GT controls the power load by manipulating its firing rate while the slurry feed flow to the gasifier is manipulated to control the syngas pressure at the GT inlet. However, the syngas pressure control is an integrating process with significant timedelay. In this work, a modified proportional-integral-derivative (PID) control is considered for syngas pressure control given that conventional PID controllers show poor control performance for integrating processes with large time delays. The conventional PID control is augmented with an internal feedback loop. The P-controller used in this internal loop converts the integrating process to an open-loop stable process. The resulting secondorder plus time delay model uses a PID controller where the tuning parameters are found by minimizing the integral time-weighted absolute error (ITAE) for disturbance rejection. A plant model with single integrator and time delay is identified by a P-control method. When a ramp change is introduced in the set-point of the load controller, the performance of both the load and pressure controllers with the modified PID control strategy is found to be superior to that using a traditional PID controller. Key

Bhattacharyya, D.; Turton, R.; Zitney, S.

2011-01-01T23:59:59.000Z

193

Estimating Policy-Driven Greenhouse Gas Emissions Trajectories in California: The California Greenhouse Gas Inventory Spreadsheet (GHGIS) Model  

E-Print Network [OSTI]

scenarios) k. Integrated gasification combined cycle (IGCC)fuels via pyrolysis, gasification, and biochemicalAnalysis: Integrated Gasification Combined Cycle (IGCC)

Greenblatt, Jeffery B.

2014-01-01T23:59:59.000Z

194

Conceptual Design of a Fossil Hydrogen Infrastructure with Capture and Sequestration of Carbon Dioxide: Case Study in Ohio  

E-Print Network [OSTI]

production of H 2 using coal gasification and 2) distributeda more modern integrated gasification combined cycle (IGCC)and efficient integrated gasification combined cycle (IGCC)

2005-01-01T23:59:59.000Z

195

Life Cycle Assessment of a Parabolic Trough Concentrating Solar Power Plant and the Impacts of Key Design Alternatives  

Science Journals Connector (OSTI)

To inform capacity expansion decisions, hybrid life cycle assessment is used to evaluate a reference design of a parabolic trough concentrating solar power (CSP) facility located in Daggett, CA, along four sustainability metrics: life cycle (LC) greenhouse gas (GHG) emissions, water consumption, cumulative energy demand (CED), and energy payback time (EPBT). ... Power plant system: components typically associated with the power block (e.g., turbine generator set), in addition to other balance-of-plant components, such as buildings, roads, and parking lots. ... The majority of the remaining water consumption is attributed to water consumed during the manufacturing phase (10% of LC or 0.47 L/kWh). ...

John J. Burkhardt; III; Garvin A. Heath; Craig S. Turchi

2011-02-23T23:59:59.000Z

196

Techno-economic modelling of integrated advanced power cycles  

Science Journals Connector (OSTI)

Concerns regarding the environmental impacts of power generation have stimulated interest in energy efficient cycles such as the integrated gasification combined cycle (IGCC) and the integrated gasification humid air turbine (IGHAT) cycle. These advanced power cycles are complex owing to the large number of units involved, interactions among the units, and the presence of streams of diverse compositions and properties. In this paper, techno-economic computer models of IGCC and IGHAT cycles are presented along with some sample results that illustrate the models' capabilities. The models, which were validated using actual data, provide performance predictions, inventories of capital and operating costs, as well as levels of gaseous emissions and solid wastes. While the models are simple enough for use in parametric, sensitivity and optimisation studies, they are responsive to variations in coal characteristics, design and operating conditions, part load operations and financial parameters.

A.O. Ong'iro; V.I. Ugursal; A.M. Al Taweel

2001-01-01T23:59:59.000Z

197

Nexant Parabolic Trough Solar Power Plant Systems Analysis; Task 2: Comparison of Wet and Dry Rankine Cycle Heat Rejection, 20 January 2005 - 31 December 2005  

SciTech Connect (OSTI)

Subcontract report by Nexant, Inc., regarding a system analysis comparing solar parabolic trough plants with wet and dry rankine cycle heat rejection.

Kelly, B.

2006-07-01T23:59:59.000Z

198

A dynamic process model of a natural gas combined cycle -- Model development with startup and shutdown simulations  

SciTech Connect (OSTI)

Research in dynamic process simulation for integrated gasification combined cycles (IGCC) with carbon capture has been ongoing at the National Energy Technology Laboratory (NETL), culminating in a full operator training simulator (OTS) and immersive training simulator (ITS) for use in both operator training and research. A derivative work of the IGCC dynamic simulator has been a modification of the combined cycle section to more closely represent a typical natural gas fired combined cycle (NGCC). This paper describes the NGCC dynamic process model and highlights some of the simulator’s current capabilities through a particular startup and shutdown scenario.

Liese, Eric [U.S. DOE; Zitney, Stephen E. [U.S. DOE

2013-01-01T23:59:59.000Z

199

Design of organic Rankine cycles for conversion of waste heat in a polygeneration plant  

E-Print Network [OSTI]

Organic Rankine cycles provide an alternative to traditional steam Rankine cycles for the conversion of low grade heat sources, where steam cycles are known to be less efficient and more expensive. This work examines organic ...

DiGenova, Kevin (Kevin J.)

2011-01-01T23:59:59.000Z

200

High-potential Working Fluids for Next Generation Binary Cycle Geothermal Power Plants  

SciTech Connect (OSTI)

A thermo-economic model has been built and validated for prediction of project economics of Enhanced Geothermal Projects. The thermo-economic model calculates and iteratively optimizes the LCOE (levelized cost of electricity) for a prospective EGS (Enhanced Geothermal) site. It takes into account the local subsurface temperature gradient, the cost of drilling and reservoir creation, stimulation and power plant configuration. It calculates and optimizes the power plant configuration vs. well depth. Thus outputs from the model include optimal well depth and power plant configuration for the lowest LCOE. The main focus of this final report was to experimentally validate the thermodynamic properties that formed the basis of the thermo-economic model built in Phase 2, and thus build confidence that the predictions of the model could be used reliably for process downselection and preliminary design at a given set of geothermal (and/or waste heat) boundary conditions. The fluid and cycle downselected was based on a new proprietary fluid from a vendor in a supercritical ORC cycle at a resource condition of 200?C inlet temperature. The team devised and executed a series of experiments to prove the suitability of the new fluid in realistic ORC cycle conditions. Furthermore, the team performed a preliminary design study for a MW-scale turbo expander that would be used for a supercritical ORC cycle with this new fluid. The following summarizes the main findings in the investigative campaign that was undertaken: 1. Chemical compatibility of the new fluid with common seal/gasket/Oring materials was found to be problematic. Neoprene, Viton, and silicone materials were found to be incompatible, suffering chemical decomposition, swelling and/or compression set issues. Of the materials tested, only TEFLON was found to be compatible under actual ORC temperature and pressure conditions. 2. Thermal stability of the new fluid at 200?C and 40 bar was found to be acceptable after 399 hours of exposure?only 3% of the initial charge degraded into by products. The main degradation products being an isomer and a dimer. 3. In a comparative experiment between R245fa and the new fluid under subcritical conditions, it was found that the new fluid operated at 1 bar lower than R245fa for the same power output, which was also predicted in the Aspen HSYSY model. As a drop-in replacement fluid for R245fa, this new fluid was found to be at least as good as R245fa in terms of performance and stability. Further optimization of the subcritical cycle may lead to a significant improvement in performance for the new fluid. 4. For supercritical conditions, the experiment found a good match between the measured and model predicted state point property data and duties from the energy balance. The largest percent differences occurred with densities and evaporator duty (see Figure 78). It is therefore reasonable to conclude that the state point model was experimentally validated with a realistic ORC system. 5. The team also undertook a preliminary turbo-expander design study for a supercritical ORC cycle with the new working fluid. Variants of radial and axial turbo expander geometries went through preliminary design and rough costing. It was found that at 15MWe or higher power rating, a multi-stage axial turbine is most suitable providing the best performance and cost. However, at lower power ratings in the 5MWe range, the expander technology to be chosen depends on the application of the power block. For EGS power blocks, it is most optimal to use multi-stage axial machines. In conclusion, the predictions of the LCOE model that showed a supercritical cycle based on the new fluid to be most advantageous for geothermal power production at a resource temperature of ~ 200C have been experimentally validated. It was found that the cycle based on the new fluid is lower in LCOE and higher in net power output (for the same boundary conditions). The project, therefore has found a new optimal configuration for low temperature geothermal power production in the form of a su

Zia, Jalal [GE Global Research; Sevincer, Edip; Chen, Huijuan; Hardy, Ajilli; Wickersham, Paul; Kalra, Chiranjeev; Laursen, Anna Lis; Vandeputte, Thomas

2013-06-29T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


201

Enhanced IGCC regulatory control and coordinated plant-wide control strategies for improving power ramp rates  

SciTech Connect (OSTI)

As part of ongoing R&D activities at the National Energy Technology Laboratory’s (NETL) Advanced Virtual Energy Simulation Training & Research (AVESTAR™) Center, this paper highlights strategies for enhancing low-level regulatory control and system-wide coordinated control strategies implemented in a high-fidelity dynamic simulator for an Integrated Gasification Combined Cycle (IGCC) power plant with carbon capture. The underlying IGCC plant dynamic model contains 20 major process areas, each of which is tightly integrated with the rest of the power plant, making individual functionally-independent processes prone to routine disturbances. Single-loop feedback control although adequate to meet the primary control objective for most processes, does not take into account in advance the effect of these disturbances, making the entire power plant undergo large offshoots and/or oscillations before the feedback action has an opportunity to impact control performance. In this paper, controller enhancements ranging from retuning feedback control loops, multiplicative feed-forward control and other control techniques such as split-range control, feedback trim and dynamic compensation, applicable on various subsections of the integrated IGCC plant, have been highlighted and improvements in control responses have been given. Compared to using classical feedback-based control structure, the enhanced IGCC regulatory control architecture reduces plant settling time and peak offshoots, achieves faster disturbance rejection, and promotes higher power ramp-rates. In addition, improvements in IGCC coordinated plant-wide control strategies for “Gasifier-Lead”, “GT-Lead” and “Plantwide” operation modes have been proposed and their responses compared. The paper is concluded with a brief discussion on the potential IGCC controller improvements resulting from using advanced process control, including model predictive control (MPC), as a supervisory control layer.

Mahapatra, P.; Zitney, S.

2012-01-01T23:59:59.000Z

202

Investigation of adsorbent-based warm carbon dioxide capture technology for IGCC system  

E-Print Network [OSTI]

Integrated gasification combined cycle with CO? capture and sequestration (IGCC-CCS) emerges as one of the most promising technologies for reducing CO? emission from coal power plant without reducing thermal efficiency ...

Liu, Zan, Ph. D. Massachusetts Institute of Technology

2014-01-01T23:59:59.000Z

203

Evaluation of sorbents for the cleanup of coal-derived synthesis gas at elevated temperatures  

E-Print Network [OSTI]

Integrated Gasification Combined Cycle (IGCC) with carbon dioxide capture is a promising technology to produce electricity from coal at a higher efficiency than with traditional subcritical pulverized coal (PC) power plants. ...

Couling, David Joseph

2012-01-01T23:59:59.000Z

204

DOE Signing Paves the Way for Funding, Construction of Innovative...  

Energy Savers [EERE]

and world reserves. Integrated gasification combined-cycle technology will be at the heart of FutureGen, a 1 billion prototype power plant that will integrate a suite of...

205

tampa body  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Tampa Electric Tampa Electric Integrated Gasification Combined-Cycle Project An Update TOPICAL REPORT NUMBER 19 JULY 2000 TOPICAL REPORT NUMBER 19 A report on a project conducted jointly under a cooperative agreement between: The U.S. Department of Energy and Tampa Electric Company July 2000 The Tampa Electric Integrated Gasification Combined-Cycle Project An Update Cover image: The Polk Power Plant site as seen from across the lake in early evening. Photography courtesy of Lee Schmoe, Bechtel Power Corporation. The Tampa Electric Integrated Gasification Combined-Cycle Project Executive Summary ........................................................................................... 1 Background ........................................................................................................

206

Analysis of syngas formation and ecological efficiency for the system of treating biomass waste and other solid fuels with CO2 recuperation based on integrated gasification combined cycle with diesel engine  

Science Journals Connector (OSTI)

Biomass combustion is a more complex process and its model solving is difficult than combustion of traditional liquid fuels. At the same...2...] to obtain the data for operating regimes of ICE with syngas-based d...

A. Y. Pilatau; H. A. Viarshyna…

2014-10-01T23:59:59.000Z

207

A methodology to estimate greenhouse gases emissions in Life Cycle Inventories of wastewater treatment plants  

SciTech Connect (OSTI)

The main objective of this paper is to present the Direct Emissions Estimation Model (DEEM), a model for the estimation of CO{sub 2} and N{sub 2}O emissions from a wastewater treatment plant (WWTP). This model is consistent with non-specific but widely used models such as AS/AD and ASM no. 1 and presents the benefits of simplicity and application over a common WWTP simulation platform, BioWin Registered-Sign , making it suitable for Life Cycle Assessment and Carbon Footprint studies. Its application in a Spanish WWTP indicates direct N{sub 2}O emissions to be 8 times larger than those associated with electricity use and thus relevant for LCA. CO{sub 2} emissions can be of similar importance to electricity-associated ones provided that 20% of them are of non-biogenic origin. - Highlights: Black-Right-Pointing-Pointer A model has been developed for the estimation of GHG emissions in WWTP. Black-Right-Pointing-Pointer Model was consistent with both ASM no. 1 and AS/AD. Black-Right-Pointing-Pointer N{sub 2}O emissions are 8 times more relevant than the one associated with electricity. Black-Right-Pointing-Pointer CO{sub 2} emissions are as important as electricity if 20% of it is non-biogenic.

Rodriguez-Garcia, G., E-mail: gonzalo.rodriguez.garcia@usc.es [Department of Chemical Engineering, University of Santiago de Compostela, Rua Lope Gomez de Marzoa, S/N, 15782, Santiago de Compostela (Spain); Hospido, A., E-mail: almudena.hospido@usc.es [Department of Chemical Engineering, University of Santiago de Compostela, Rua Lope Gomez de Marzoa, S/N, 15782, Santiago de Compostela (Spain); Bagley, D.M., E-mail: bagley@uwyo.edu [Department of Chemical and Petroleum Engineering, University of Wyoming, 82072 Laramie, WY (United States); Moreira, M.T., E-mail: maite.moreira@usc.es [Department of Chemical Engineering, University of Santiago de Compostela, Rua Lope Gomez de Marzoa, S/N, 15782, Santiago de Compostela (Spain); Feijoo, G., E-mail: gumersindo.feijoo@usc.es [Department of Chemical Engineering, University of Santiago de Compostela, Rua Lope Gomez de Marzoa, S/N, 15782, Santiago de Compostela (Spain)

2012-11-15T23:59:59.000Z

208

Economic comparison between coal-fired and liquefied natural gas combined cycle power plants considering carbon tax: Korean case  

Science Journals Connector (OSTI)

Economic growth is main cause of environmental pollution and has been identified as a big threat to sustainable development. Considering the enormous role of electricity in the national economy, it is essential to study the effect of environmental regulations on the electricity sector. This paper aims at making an economic analysis of Korea's power plant utilities by comparing electricity generation costs from coal-fired power plants and liquefied natural gas (LNG) combined cycle power plants with environmental consideration. In this study, the levelized generation cost method (LGCM) is used for comparing economic analysis of power plant utilities. Among the many pollutants discharged during electricity generation, this study principally deals with control costs related only to CO2 and NO2, since the control costs of SO2 and total suspended particulates (TSP) are already included in the construction cost of utilities. The cost of generating electricity in a coal-fired power plant is compared with such cost in a LNG combined cycle power plant. Moreover, a sensitivity analysis with computer simulation is performed according to fuel price, interest rates and carbon tax. In each case, these results can help in deciding which utility is economically justified in the circumstances of environmental regulations.

Suk-Jae Jeong; Kyung-Sup Kim; Jin-Won Park; Dong-soon Lim; Seung-moon Lee

2008-01-01T23:59:59.000Z

209

Advanced regulatory control and coordinated plant-wide control strategies for IGCC targeted towards improving power ramp-rates  

SciTech Connect (OSTI)

As part of ongoing R&D activities at the National Energy Technology Laboratory's (NETL) Advanced Virtual Energy Simulation Training & Research (AVESTAR™) Center, this paper highlights strategies for enhancing low-level regulatory control and system-wide coordinated control strategies implemented in a high-fidelity dynamic simulator for an Integrated Gasification Combined Cycle (IGCC) power plant with carbon capture. The underlying IGCC plant dynamic model contains 20 major process areas, each of which is tightly integrated with the rest of the power plant, making individual functionally-independent processes prone to routine disturbances. Single-loop feedback control although adequate to meet the primary control objective for most processes, does not take into account in advance the effect of these disturbances, making the entire power plant undergo large offshoots and/or oscillations before the feedback action has an opportunity to impact control performance. In this paper, controller enhancements ranging from retuning feedback control loops, multiplicative feed-forward control and other control techniques such as split-range control, feedback trim and dynamic compensation, applicable on various subsections of the integrated IGCC plant, have been highlighted and improvements in control responses have been given. Compared to using classical feedback-based control structure, the enhanced IGCC regulatory control architecture reduces plant settling time and peak offshoots, achieves faster disturbance rejection, and promotes higher power ramp-rates. In addition, improvements in IGCC coordinated plant-wide control strategies for “Gasifier-Lead”, “GT-Lead” and “Plantwide” operation modes have been proposed and their responses compared. The paper is concluded with a brief discussion on the potential IGCC controller improvements resulting from using advanced process control, including model predictive control (MPC), as a supervisory control layer.

Mahapatra, P.; Zitney, S.

2012-01-01T23:59:59.000Z

210

High-potential Working Fluids for Next Generation Binary Cycle Geothermal Power Plants  

Broader source: Energy.gov [DOE]

DOE Geothermal Peer Review 2010 - Presentation. Project objective: Find optimized working fluid/advanced cycle combination for EGS applications.

211

Recovery Act: Brea California Combined Cycle Electric Generating Plant Fueled by Waste Landfill Gas  

SciTech Connect (OSTI)

The primary objective of the Project was to maximize the productive use of the substantial quantities of waste landfill gas generated and collected at the Olinda Landfill near Brea, California. An extensive analysis was conducted and it was determined that utilization of the waste gas for power generation in a combustion turbine combined cycle facility was the highest and best use. The resulting Project reflected a cost effective balance of the following specific sub-objectives: • Meeting the environmental and regulatory requirements, particularly the compliance obligations imposed on the landfill to collect, process and destroy landfill gas • Utilizing proven and reliable technology and equipment • Maximizing electrical efficiency • Maximizing electric generating capacity, consistent with the anticipated quantities of landfill gas generated and collected at the Olinda Landfill • Maximizing equipment uptime • Minimizing water consumption • Minimizing post-combustion emissions • The Project produced and will produce a myriad of beneficial impacts. o The Project created 360 FTE construction and manufacturing jobs and 15 FTE permanent jobs associated with the operation and maintenance of the plant and equipment. o By combining state-of-the-art gas clean up systems with post combustion emissions control systems, the Project established new national standards for best available control technology (BACT). o The Project will annually produce 280,320 MWh’s of clean energy o By destroying the methane in the landfill gas, the Project will generate CO2 equivalent reductions of 164,938 tons annually. The completed facility produces 27.4 MWnet and operates 24 hours a day, seven days a week.

Galowitz, Stephen

2012-12-31T23:59:59.000Z

212

What should the government do to encourage technical change in the energy sector?  

E-Print Network [OSTI]

, and storage; (4) clean coal technologies, such as the Integrated Coal Gasification Combined Cycle; and (5

Deutch, John

213

EIS-0431: DOE Notice of Availability of Draft Environmental Impact Statement  

Broader source: Energy.gov [DOE]

Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA

214

EIS-0431: Extension of public comment period; Notice of public hearing; Correction  

Broader source: Energy.gov [DOE]

Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, CA

215

The importance of combined cycle generating plants in integrating large levels of wind power generation  

SciTech Connect (OSTI)

Integration of high wind penetration levels will require fast-ramping combined cycle and steam cycles that, due to higher operating costs, will require proper pricing of ancillary services or other forms of compensation to remain viable. Several technical and policy recommendations are presented to help realign the generation mix to properly integrate the wind. (author)

Puga, J. Nicolas

2010-08-15T23:59:59.000Z

216

System study of an MHD/gas turbine combined-cycle baseload power plant. HTGL report No. 134  

SciTech Connect (OSTI)

The MHD/gas turbine combined-cycle system has been designed specifically for applications where the availability of cooling water is very limited. The base case systems which were studied consisted of an MHD plant with a gas turbine bottoming plant, and required no cooling water. The gas turbine plant uses only air as its working fluid and receives its energy input from the MHD exhaust gases by means of metal tube heat exchangers. In addition to the base case systems, vapor cycle variation systems were considered which included the addition of a vapor cycle bottoming plant to improve the thermal efficiency. These systems required a small amount of cooling water. The MHD/gas turbine systems were modeled with sufficient detail, using realistic component specifications and costs, so that the thermal and economic performance of the system could be accurately determined. Three cases of MHD/gas turbine systems were studied, with Case I being similar to an MHD/steam system so that a direct comparison of the performances could be made, with Case II being representative of a second generation MHD system, and with Case III considering oxygen enrichment for early commercial applications. The systems are nominally 800 MW/sub e/ to 1000 MW/sub e/ in size. The results show that the MHD/gas turbine system has very good thermal and economic performances while requiring either little or no cooling water. Compared to the MHD/steam system which has a cooling tower heat load of 720 MW, the Base Case I MHD/gas turbine system has a heat rate which is 13% higher and a cost of electricity which is only 7% higher while requiring no cooling water. Case II results show that an improved performance can be expected from second generation MHD/gas turbine systems. Case III results show that an oxygen enriched MHD/gas turbine system may be attractive for early commercial applications in dry regions of the country.

Annen, K.D.

1981-08-01T23:59:59.000Z

217

Specific features of the schematic solutions adopted in the steam turbine units produced by the Ural Turbine Works and used as part of combined-cycle plants  

Science Journals Connector (OSTI)

Specific features of the schematic solutions adopted in the steam turbine units designed and produced by the Ural Turbine Works for use as part of combined-cycle plants are considered.

A. A. Gol’dberg; T. L. Shibaev; H. C. Paneque Aguilera…

2013-08-01T23:59:59.000Z

218

Determining the maximal capacity of a combined-cycle plant operating with afterburning of fuel in the gas conduit upstream of the heat-recovery boiler  

Science Journals Connector (OSTI)

The effect gained from afterburning of fuel in the gas conduit upstream of the heat-recovery boiler used as part of a PGU-450T combined-cycle plant is considered. The results obtained from ... electric and therma...

V. M. Borovkov; N. M. Osmanova

2011-01-01T23:59:59.000Z

219

MULTIPARAMETER OPTIMIZATION STUDIES ON GEOTHERMAL ENERGY CYCLES  

E-Print Network [OSTI]

of Practical Cycles for Geothermal Power Plants." GeneralDesign and Optimize Geothermal Power Cycles." Presented atof Practical Cycles for Geothermal Power Plants." General

Pope, W.L.

2011-01-01T23:59:59.000Z

220

THE TRANSPOSED CRITICAL TEMPERATURE RANKINE THERMODYNAMIC CYCLE  

E-Print Network [OSTI]

Process Program for Geothermal Power Plant Cycles,'*for a Rankine Cycle Geothermal Power Plant," Proceedings,Design and Optimize Geothermal Power Cycles," presented at

Pope, William L.

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


221

Investigation of plant control strategies for the supercritical C0{sub 2}Brayton cycle for a sodium-cooled fast reactor using the plant dynamics code.  

SciTech Connect (OSTI)

The development of a control strategy for the supercritical CO{sub 2} (S-CO{sub 2}) Brayton cycle has been extended to the investigation of alternate control strategies for a Sodium-Cooled Fast Reactor (SFR) nuclear power plant incorporating a S-CO{sub 2} Brayton cycle power converter. The SFR assumed is the 400 MWe (1000 MWt) ABR-1000 preconceptual design incorporating metallic fuel. Three alternative idealized schemes for controlling the reactor side of the plant in combination with the existing automatic control strategy for the S-CO{sub 2} Brayton cycle are explored using the ANL Plant Dynamics Code together with the SAS4A/SASSYS-1 Liquid Metal Reactor (LMR) Analysis Code System coupled together using the iterative coupling formulation previously developed and implemented into the Plant Dynamics Code. The first option assumes that the reactor side can be ideally controlled through movement of control rods and changing the speeds of both the primary and intermediate coolant system sodium pumps such that the intermediate sodium flow rate and inlet temperature to the sodium-to-CO{sub 2} heat exchanger (RHX) remain unvarying while the intermediate sodium outlet temperature changes as the load demand from the electric grid changes and the S-CO{sub 2} cycle conditions adjust according to the S-CO{sub 2} cycle control strategy. For this option, the reactor plant follows an assumed change in load demand from 100 to 0 % nominal at 5 % reduction per minute in a suitable fashion. The second option allows the reactor core power and primary and intermediate coolant system sodium pump flow rates to change autonomously in response to the strong reactivity feedbacks of the metallic fueled core and assumed constant pump torques representing unchanging output from the pump electric motors. The plant behavior to the assumed load demand reduction is surprising close to that calculated for the first option. The only negative result observed is a slight increase in the intermediate inlet sodium temperatures by about 10 C. This temperature rise could presumably be precluded or significantly reduced through fine adjustment of the control rods and pump motors. The third option assumes that the reactor core power and primary and intermediate system flow rates are ideally reduced linearly in a programmed fashion that instantaneously matches the prescribed load demand. The calculated behavior of this idealized case reveals a number of difficulties because the control strategy for the S-CO{sub 2} cycle overcools the reactor potentially resulting in the calculation of sodium bulk freezing and the onset of sodium boiling. The results show that autonomous SFR operation may be viable for the particular assumed load change transient and deserves further investigation for other transients and postulated accidents.

Moisseytsev, A.; Sienicki, J. (Nuclear Engineering Division)

2011-04-12T23:59:59.000Z

222

Optimization and the effect of steam turbine outlet quality on the output power of a combined cycle power plant  

Science Journals Connector (OSTI)

Abstract A narrow path exists to a sustainable solution which passes through careful steps of efficiency improvement (resource management) and provides environmental friendly energies. Thermal power plants are more common in many power production sites around the world. Therefore, in this current research study a comprehensive thermodynamic modeling of a combined cycle power plant with dual pressure heat recovery steam generator is presented. Since the steam turbine outlet quality is a restrictive parameter, optimization of three cases with different steam quality are conducted and discussed. In other hand, energy and exergy analysis of each components for these three different cases estimated and compared. Obtained results show that it is really important to keep the quality of the vapor at turbine outlet constant in 88% for the results to be more realistic and also optimization and data are more technically feasible and applicable.

A. Ganjehkaviri; M.N. Mohd Jaafar; S.E. Hosseini

2015-01-01T23:59:59.000Z

223

Organic Rankine Cycle Systems for Waste Heat Recovery in Refineries and Chemical Process Plants  

E-Print Network [OSTI]

. A product package and recommended division of responsibilities between purchaser, A&E company and supplier is presented for installations in refineries and process plants. The product package covers the electrical power range from 3/4 to 5 MW...

Meacher, J. S.

1981-01-01T23:59:59.000Z

224

Optimizing the start-up operations of combined cycle power plants using soft computing methods  

Science Journals Connector (OSTI)

......megawatts. Industrial turbines produce high-quality...recovered to improve the efficiency of power generation...steam and drive a steam turbine in a combined-cycle...either gas or steam turbine alone because it performs...generation by their high efficiency and possibility to operate......

Ilaria Bertini; Matteo De Felice; Alessandro Pannicelli; Stefano Pizzuti

2012-08-01T23:59:59.000Z

225

The cost of integration of zero emission power plants—A case study for the island of Cyprus  

Science Journals Connector (OSTI)

In this work, a technical, economic and environmental analysis is carried out for the estimation of the optimal option scenario for the Cyprus's future power generation system. A range of power generation technologies integrated with carbon capture and storage (CCS) were examined as candidate options and compared with the business as usual scenario. Based on the input data and the assumptions made, the simulations indicated that the integrated gasification combined cycle (IGCC) technology with pre-combustion CCS integration is the least cost option for the future expansion of the power generation system. In particular, the results showed that for a natural gas price of 7.9US$/GJ the IGCC technology with pre-combustion CCS integration is the most economical choice, closely followed by the pulverized coal technology with post-combustion CCS integration. The combined cycle technology can, also, be considered as alternative competitive technology. The combined cycle technologies with pre- or post-combustion CCS integration yield more expensive electricity unit cost. In addition, a sensitivity analysis has been also carried out in order to examine the effect of the natural gas price on the optimum planning. For natural gas prices greater than 6.4US$/GJ the least cost option is the use of IGCC technology with CCS integration. It can be concluded that the Cyprus's power generation system can be shifted slowly towards the utilization of CCS technologies in favor of the existing steam power plants in order not only to lower the environmental emissions and fulfilling the recent European Union Energy Package requirements but also to reduce the associated electricity unit cost.

Andreas Poullikkas; Ioannis Hadjipaschalis; Costas Christou

2009-01-01T23:59:59.000Z

226

Emerging Energy-Efficiency and Greenhouse Gas Mitigation Technologies for the Pulp and Paper Industry  

E-Print Network [OSTI]

gasification with combined cycles biological oxygen demandsintegrated gasification combined cycle Intergovernmentalbe integrated with combined-cycle (CC) technology (BLGCC),

Kong, Lingbo

2014-01-01T23:59:59.000Z

227

COMPARATIVE COSTS OF CALIFORNIA CENTRAL STATION ELECTRICITY  

E-Print Network [OSTI]

of such efforts based substantially on empirical data collected from operating facilities. The combined cycle, alternative technologies, combined cycle, simple cycle, integrated gasification combined cycle, coal cost and simple cycle costs are the result of a comprehensive survey of actual costs from the power plant

228

Nitrogen cycling, plant biomass, and carbon dioxide evolution in a subsurface flow wetland  

E-Print Network [OSTI]

to ascertain the fate of nitrogen in a constructed wetland and the rate of bioremediation as indicated by carbon dioxide evolution. Research included a study of nitrogen uptake by plants and nitrification. A tracer isotope of nitrogen,¹?N, was used to follow...

Lane, Jeffrey J

2012-06-07T23:59:59.000Z

229

Optimizing the start-up operations of combined cycle power plants using soft computing methods  

Science Journals Connector (OSTI)

......Energy, New technologies and sustainable Economic development Agency...Detection in Gas Turbines using Fuzzy...fusion for gas turbine power plants...Research Development Center Technical...Energy, New technologies and sustainable Economic development Agency...combination of a gas turbine and a steam......

Ilaria Bertini; Matteo De Felice; Alessandro Pannicelli; Stefano Pizzuti

2012-08-01T23:59:59.000Z

230

Modeling of the rock bed thermal energy storage system of a combined cycle solar thermal power plant in South Africa  

Science Journals Connector (OSTI)

Abstract A thermocline-based rock bed thermal energy storage system potentially offers a cheap and simple way of achieving dispatchability in an air-cooled central receiver CSP plant. In order to efficiently match heliostat field size, storage dimensions, back-up fuel consumption and turbine sizes for non-stop power generation and economic feasibility, year-long power plant simulations have to be run. This paper focuses on the storage as the center of in- and outgoing thermal energy. The derived storage model has one spatial dimension which is justified by the high tube-to-particle diameter ratio and because yearly aggregated – and not momentary – values are of interest. A validation of the correlations with data from the literature shows acceptable agreement. Sensitivity analyses indicate that, due to low costs of the storage system, above certain minimum storage dimensions, the influence on energetic and monetary performance indicators is marginal. The calculated LCOE is in the range of 0.11–0.18 EUR/kW h and in agreement with other studies on combined cycle CSP plants.

Lukas Heller; Paul Gauché

2013-01-01T23:59:59.000Z

231

The Cost of Carbon Capture and Storage for Natural Gas Combined Cycle Power Plants  

Science Journals Connector (OSTI)

Historically, natural gas has been used to provide peak-load power at a relatively high cost per kilowatt-hour during the daytime intervals when electricity demands peak and cannot be supplied wholly by baseload generators. ... (1) This share is projected to grow to 47% by 2035, with natural gas accounting for 60% of new generating capacity additions between 2010 and 2035 in the Department of Energy’s reference case scenario. ... To answer this question we use the LCOE results above to generate a probabilistic difference in cost, recognizing that some parameters should have the same value for plants with and without CCS, such as the power block capital cost, natural gas price, and the plant labor rate. ...

Edward S. Rubin; Haibo Zhai

2012-02-14T23:59:59.000Z

232

Steam Oxidation of Fossil Power Plant Materials: Collaborative Research to Enable Advanced Steam Power Cycles  

DOE Public Access Gateway for Energy & Science Beta (PAGES Beta)

Research into improved materials systems and associated manufacturing and reliability issues is a major part of initiatives to produce cleaner and cheaper energy systems in the UK and the USA. Under the auspices of a Memorandum of Understanding on Energy R&D, a work programme concerned with steam oxidation has been conducted. The focus was on the generation of definitive information regarding the oxidation behaviour in steam of current and developmental ferritic steels, austenitic steels, and nickelbased alloys required to enable advanced steam power cycles. The results were intended to provide a basis for quantifying the rate of metal loss expected under advanced steam cycle conditions, as well as understanding of the evolution of oxide scale morphologies with time and temperature to identify features that could influence scale exfoliation characteristics. This understanding and acquired data were used to develop and validate models of oxide growth and loss by exfoliation. This paper provides an overview of the activity and highlights a selection of the results coming from the programme.

A. T. Fry; I. G Wright; N. J Simms; B. McGhee; G. R. Holcomb

2013-11-19T23:59:59.000Z

233

Energy and Economic Analysis of the CO2 Capture from Flue Gas of Combined Cycle Power Plants  

Science Journals Connector (OSTI)

Abstract Carbon capture and storage is considered as one of the key strategies for reducing the emissions of carbon dioxide from power generation facilities. Although post-combustion capture via chemical absorption is now a mature technology, the separation of CO2 from flue gases shows many issues, including the solvent degradation and the high regeneration energy requirement, that in turn reduces the power plant performances. Focusing on a triple pressure and reheat combined cycle with exhaust gas recirculation, this paper aims to evaluate the potential impacts of integrating a post-combustion capture system, based on an absorption process with monoethanolamine solvent. Energy and economic performances of the integrated system are evaluated varying the exhaust gas recirculation fraction and the CO2 capture ratio. The different configurations examined are then compared in terms of efficiency and rated capacity of the integrated system, as well as considering the cost of electricity generated and the cost of CO2 avoided.

Maura Vaccarelli; Roberto Carapellucci; Lorena Giordano

2014-01-01T23:59:59.000Z

234

Cost and Performance Baseline for Fossil Energy Plants; Volume 3c: Natural Gas Combined Cycle at Elevation  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Baseline for Fossil Energy Plants Volume 3c: Natural Gas Combined Cycle at Elevation March 2011 DOE/NETL-2010/1396 Disclaimer This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference therein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States

235

Contribution of Clinch River Breeder Reactor plant design and development to the LMFBR fuel cycle  

SciTech Connect (OSTI)

This paper describes how the CRBRP development and CRBRP focus of the LMFBR base technology program have led to advances in the state of the art in physics, thermal-hydraulics, structural analysis, core restraint, seismic analysis, and analysis of hypothetical core-disruptive accident energetics, all of which have been incorporated through disciplined engineering into the final CRBRP design. The total development in the US of fuels and materials, the analytical advances made on CRBRP design, and the incorporation of the latest experimental results into that design have put the US technology in general and the CRBRP design in particular at the forefront of technology. This has placed the US in a position to develop the most favorable LMFBR fuel cycle.

Riley, D.R.; Dickson, P.W.

1981-01-01T23:59:59.000Z

236

Integration of the steam cycle and CO2 capture process in a decarbonization power plant  

Science Journals Connector (OSTI)

Abstract A new integrated system with power generation and CO2 capture to achieve higher techno-economic performance is proposed in this study. In the new system, three measures are adopted to recover the surplus energy from the CO2 capture process. The three measures are as follows: (1) using a portion of low-pressure steam instead of high-pressure extracted steam by installing the steam ejector, (2) mixing a portion of flash-off water with the extracted steam to utilize the superheat degree of the extracted steam, and (3) recycling the low-temperature waste heat from the CO2 capture process to heat the condensed water. As a result, the power output of the new integrated system is 107.61 MW higher than that of a decarbonization power plant without integration. The efficiency penalty of CO2 capture is expected to decrease by 4.91%-points. The increase in investment produced by the new system is 3.25 M$, which is only 0.88% more than the total investment of a decarbonization power plant without integration. Lastly, the cost of electricity and CO2 avoided is 15.14% and 33.1% lower than that of a decarbonization power generation without integration, respectively. The promising results obtained in this study provide a new approach for large-scale CO2 removal with low energy penalty and economic cost.

Gang Xu; Yue Hu; Baoqiang Tang; Yongping Yang; Kai Zhang; Wenyi Liu

2014-01-01T23:59:59.000Z

237

Base-Load and Peak Electricity from a Combined Nuclear Heat and Fossil Combined-Cycle Plant  

SciTech Connect (OSTI)

A combined-cycle power plant is proposed that uses heat from a high-temperature reactor and fossil fuel to meet base-load and peak electrical demands. The high-temperature gas turbine produces shaft power to turn an electric generator. The hot exhaust is then fed to a heat recovery steam generator (HRSG) that provides steam to a steam turbine for added electrical power production. A simplified computational model of the thermal power conversion system was developed in order to parametrically investigate two different steady-state operation conditions: base load nuclear heat only from an Advanced High Temperature Reactor (AHTR), and combined nuclear heat with fossil heat to increase the turbine inlet temperature. These two cases bracket the expected range of power levels, where any intermediate power level can result during electrical load following. The computed results indicate that combined nuclear-fossil systems have the potential to offer both low-cost base-load electricity and lower-cost peak power relative to the existing combination of base-load nuclear plants and separate fossil-fired peak-electricity production units. In addition, electric grid stability, reduced greenhouse gases, and operational flexibility can also result with using the conventional technology presented here for the thermal power conversion system coupled with the AHTR.

Conklin, Jim [ORNL; Forsberg, Charles W [ORNL

2007-01-01T23:59:59.000Z

238

Base-Load and Peak Electricity from a Combined Nuclear Heat and Fossil Combined-Cycle Plant  

SciTech Connect (OSTI)

A combined-cycle power plant is proposed that uses heat from a high-temperature reactor and fossil fuel to meet base-load and peak electrical demands. The high temperature gas turbine produces shaft power to turn an electric generator. The hot exhaust is then fed to a heat recovery steam generator (HRSG) that provides steam to a steam turbine for added electrical power production. A simplified computational model of the thermal power conversion system was developed in order to parametrically investigate two different steady-state operation conditions: base load nuclear heat only from an Advanced High Temperature Reactor (AHTR), and combined nuclear heat with fossil heat to increase the turbine inlet temperature. These two cases bracket the expected range of power levels, where any intermediate power level can result during electrical load following. The computed results indicate that combined nuclear-fossil systems have the potential to offer both low-cost base-load electricity and lower-cost peak power relative to the existing combination of base-load nuclear plants and separate fossil-fired peak-electricity production units. In addition, electric grid stability, reduced greenhouse gases, and operational flexibility can also result with using the conventional technology presented here for the thermal power conversion system coupled with the AHTR. (authors)

Conklin, James C.; Forsberg, Charles W. [Oak Ridge National Laboratory, P.O. Box 2008, Oak Ridge, TN 37831 (United States)

2007-07-01T23:59:59.000Z

239

Retrofitting the Strogino district heat supply station with construction of a 260-MW combined-cycle power plant (Consisting of two PGU-130 combined-cycle power units)  

Science Journals Connector (OSTI)

The retrofitting carried out at the Strogino district heat supply station and the specific features of works accomplished in the course of constructing the thermal power station based on a combined-cycle power pl...

V. F. Aleksandrov

2010-02-01T23:59:59.000Z

240

1 Copyright 2012 by ASME Proceedings of ASME Turbo Expo 2012  

E-Print Network [OSTI]

cycles for three interesting coal fired, gasification based, plants with CO2 capture: a Fischer Tropsch synthesis processes with once-through reactor (CTL-OT-CCS), and an integrated gasification combined cycle systems typically comprise a Heat Recovery Steam Cycle (HRSC) fed with waste heat from gas turbines and

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


241

Thermo economic evaluation of oxy fuel combustion cycle in Kazeroon power plant considering enhanced oil recovery revenues  

Science Journals Connector (OSTI)

Oxy fuel combustion and conventional cycle (currently working cycle ... for enhanced oil recovery in the various oil price indices is conducted and indices net present ... models reveal that gross efficiency of t...

Ehsan Torabnejad; Ramin Haghighi-Khoshkhoo…

2014-03-01T23:59:59.000Z

242

Virtually simulating the next generation of clean energy technologies: NETL's AVESTAR Center is dedicated to the safe, reliable and efficient operation of advanced energy plants with carbon capture  

SciTech Connect (OSTI)

Imagine using a real-time virtual simulator to learn to fly a space shuttle or rebuild your car's transmission without touching a piece of equipment or getting your hands dirty. Now, apply this concept to learning how to operate and control a state-of-the-art, electricity-producing power plant capable of carbon dioxide (CO{sub 2}) capture. That's what the National Energy Technology Laboratory's (NETL) Advanced Virtual Energy Simulation Training and Research (AVESTAR) Center (www.netl.doe.gov/avestar) is designed to do. Established as part of the Department of Energy's (DOE) initiative to advance new clean energy technology for power generation, the AVESTAR Center focuses primarily on providing simulation-based training for process engineers and energy plant operators, starting with the deployment of a first-of-a-kind operator training simulator for an integrated gasification combined cycle (IGCC) power plant with CO{sub 2} capture. The IGCC dynamic simulator builds on, and reaches beyond, conventional power plant simulators to merge, for the first time, a 'gasification with CO{sub 2} capture' process simulator with a 'combined-cycle' power simulator. Based on Invensys Operations Management's SimSci-Esscor DYNSIM software, the high-fidelity dynamic simulator provides realistic training on IGCC plant operations, including normal and faulted operations, as well as plant start-up, shutdown and power demand load changes. The highly flexible simulator also allows for testing of different types of fuel sources, such as petcoke and biomass, as well as co-firing fuel mixtures. The IGCC dynamic simulator is available at AVESTAR's two locations, NETL (Figure 1) and West Virginia University's National Research Center for Coal and Energy (www.nrcce.wvu.edu), both in Morgantown, W.Va. By offering a comprehensive IGCC training program, AVESTAR aims to develop a workforce well prepared to operate, control and manage commercial-scale gasification-based power plants with CO{sub 2} capture. The facility and simulator at West Virginia University promotes NETL's outreach mission by offering hands-on simulator training and education to researchers and university students.

Zitney, S.

2012-01-01T23:59:59.000Z

243

Results of heat tests of the TGE-435 main boiler in the PGU-190/220 combined-cycle plant of the Tyumen' TETs-2 cogeneration plant  

SciTech Connect (OSTI)

Special features of operation of a boiler operating as a combined-cycle plant and having its own furnace and burner unit are descried. The flow of flue gases on the boiler is increased due to feeding of exhaust gases of the GTU into the furnace, which intensifies the convective heat exchange. In addition, it is not necessary to preheat air in the convective heating surfaces (the boiler has no air preheater). The convective heating surfaces of the boiler are used for heating the feed water, thus replacing the regeneration extractions of the steam turbine (HPP are absent in the circuit) and partially replacing the preheating of condensate (the LPP in the circuit of the unit are combined with preheaters of delivery water). Regeneration of the steam turbine is primarily used for the district cogeneration heating purposes. The furnace and burner unit of the exhaust-heat boiler (which is a new engineering solution for the given project) ensures utilization of not only the heat of the exhaust gases of the GTU but also of their excess volume, because the latter contains up to 15% oxygen that oxidizes the combustion process in the boiler. Thus, the gas temperature at the inlet to the boiler amounts to 580{sup o}C at an excess air factor a = 3.50; at the outlet these parameters are utilized to T{sub out} = 139{sup o}C and a{sub out} = 1.17. The proportions of the GTU/boiler loads that can actually be organized at the generating unit (and have been checked by testing) are presented and the proportions of loads recommended for the most efficient operation of the boiler are determined. The performance characteristics of the boiler are presented for various proportions of GTU/boiler loads. The operating conditions of the superheater and of the convective trailing heating surfaces are presented as well as the ecological parameters of the generating unit.

A.V. Kurochkin; A.L. Kovalenko; V.G. Kozlov; A.I. Krivobok [Engineering Center of the Ural Power Industry (Russian Federation)

2007-01-15T23:59:59.000Z

244

Power generation plants with carbon capture and storage: A techno-economic comparison between coal combustion and gasification technologies  

Science Journals Connector (OSTI)

Abstract Worldwide energy production requirements could not be fully satisfied by nuclear and renewables sources. Therefore a sustainable use of fossil fuels (coal in particular) will be required for several decades. In this scenario, carbon capture and storage (CCS) represents a key solution to control the global warming reducing carbon dioxide emissions. The integration between CCS technologies and power generation plants currently needs a demonstration at commercial scale to reduce both technological risks and high capital and operating cost. This paper compares, from the technical and economic points of view, the performance of three coal-fired power generation technologies: (i) ultra-supercritical (USC) plant equipped with a conventional flue gas treatment (CGT) process, (ii) USC plant equipped with SNOX technology for a combined removal of sulphur and nitrogen oxides and (iii) integrated gasification combined cycle (IGCC) plant based on a slurry-feed entrained-flow gasifier. Each technology was analysed in its configurations without and with CO2 capture, referring to a commercial-scale of 1000 MWth. Technical assessment was carried out by using simulation models implemented through Aspen Plus and Gate-Cycle tools, whereas economic assessment was performed through a properly developed simulation model. USC equipped with CGT systems shows an overall efficiency (43.7%) comparable to IGCC (43.9%), whereas introduction of SNOX technology increases USC efficiency up to 44.8%. Being the CCS energy penalties significantly higher for USC (about 10.5% points vs. about 8.5 for IGCC), the IGCC with CCS is more efficient (35.3%) than the corresponding CO2-free USC (34.2% for the SNOX-based configuration). Whereas, for the case study, USC is most profitable than IGCC (with a net present value, NPV, of 190 M€ vs. 54 M€) for a conventional configuration, CO2-free IGCC shows a higher NPV (?673 M€) than USC (?711 M€). In any cases, the NPV of all the CO2-free configurations is strongly negative: this means that, with the current market conditions, the introduction of a CCS system cannot be economically justified without a significant incentive.

Vittorio Tola; Alberto Pettinau

2014-01-01T23:59:59.000Z

245

An Overview of Coal based  

E-Print Network [OSTI]

An Overview of Coal based Integrated Gasification Combined Cycle (IGCC) Technology September 2005. LFEE 2005-002 WP #12;#12;Table of Contents 1 Integrated Gasification Combined Cycle (IGCC

246

Technical-economic evaluation of O2/CO2 recycle combustion power plant based on life-cycle  

Science Journals Connector (OSTI)

In this study, a detailed technical-economic analysis on a O2/CO2 recycle combustion power plant (Oxy-combustion plant) retrofitted from the existing coal-fired plant (with a capacity of 2×300...2 emissions, inve...

Yun Wang; YongChun Zhao; JunYing Zhang…

2010-12-01T23:59:59.000Z

247

Geothermal power plant R and D: an analysis of cost-performance tradeoffs and the Heber Binary-Cycle Demonstration Project  

SciTech Connect (OSTI)

A study of advancements in power plant designs for use at geothermal resources in the low to moderate (300 to 400F) temperature range is reported. In 3 case studies, the benefits of R and D to achieve these advancements are evaluated in terms of expected increases in installed geothermal generating capacity over the next 2 decades. A parametric sensitivity study is discussed which analyzes differential power development for combinations of power plant efficiency and capitol cost. Affordable tradeoffs between plant performance and capital costs are illustrated. The independent review and analysis of the expected costs of construction, operation and maintenance of the Heber Binary Cycle Geothermal Power Demonstration Plant are described. Included in this assessment is an analysis of each of the major cost components of the project, including (1) construction cost, (2) well field development costs, (3) fluid purchase costs, and (4) well field and power plant operation and maintenance costs. The total cost of power generated from the Heber Plant (in terms of mills per kWh) is then compared to the cost of power from alternative fossil-fueled base load units. Also evaluated are the provisions of both: (a) the Cooperative Agreement between the federal government and San Diego Gas and Electric (SDG and E); and (b) the Geothermal Heat Sales Contract with Union Oil Company.

Cassel, T.A.V.; Amundsen, C.B.; Blair, P.D.

1983-06-30T23:59:59.000Z

248

Connecting the second exhaust-heat boiler to the operating first one under the conditions of flow circuits of combined-cycle plants with two gas-turbine units and one steam turbine  

Science Journals Connector (OSTI)

Problems arising with connecting the second exhaust-heat boiler to the first exhaust-heat boiler under load in the case of flow circuits of combined-cycle plants of type PGU-450 are considered. Similar problem...

Yu. A. Radin; I. A. Grishin; T. S. Kontorovich…

2006-03-01T23:59:59.000Z

249

Climate change and health costs of air emissions from biofuels and gasoline  

Science Journals Connector (OSTI)

...plant materials and wastes. Because plants...analysis on current industry data, with natural...for an integrated gasification combined-cycle...projections for the industry in 2020...connect . J Air and Waste Manage Assoc 56 : 709 – 742...is applied, an industry-weighted average...

Jason Hill; Stephen Polasky; Erik Nelson; David Tilman; Hong Huo; Lindsay Ludwig; James Neumann; Haochi Zheng; Diego Bonta

2009-01-01T23:59:59.000Z

250

Advanced virtual energy simulation training and research: IGCC with CO2 capture power plant  

SciTech Connect (OSTI)

In this presentation, we highlight the deployment of a real-time dynamic simulator of an integrated gasification combined cycle (IGCC) power plant with CO{sub 2} capture at the Department of Energy's (DOE) National Energy Technology Laboratory's (NETL) Advanced Virtual Energy Simulation Training and Research (AVESTARTM) Center. The Center was established as part of the DOE's accelerating initiative to advance new clean coal technology for power generation. IGCC systems are an attractive technology option, generating low-cost electricity by converting coal and/or other fuels into a clean synthesis gas mixture in a process that is efficient and environmentally superior to conventional power plants. The IGCC dynamic simulator builds on, and reaches beyond, conventional power plant simulators to merge, for the first time, a 'gasification with CO{sub 2} capture' process simulator with a 'combined-cycle' power simulator. Fueled with coal, petroleum coke, and/or biomass, the gasification island of the simulated IGCC plant consists of two oxygen-blown, downward-fired, entrained-flow, slagging gasifiers with radiant syngas coolers and two-stage sour shift reactors, followed by a dual-stage acid gas removal process for CO{sub 2} capture. The combined cycle island consists of two F-class gas turbines, steam turbine, and a heat recovery steam generator with three-pressure levels. The dynamic simulator can be used for normal base-load operation, as well as plant start-up and shut down. The real-time dynamic simulator also responds satisfactorily to process disturbances, feedstock blending and switchovers, fluctuations in ambient conditions, and power demand load shedding. In addition, the full-scope simulator handles a wide range of abnormal situations, including equipment malfunctions and failures, together with changes initiated through actions from plant field operators. By providing a comprehensive IGCC operator training system, the AVESTAR Center is poised to develop a workforce well-prepared to operate and control commercial-scale gasification-based power plants capable of 90% pre-combustion CO{sub 2} capture and compression, as well as low sulfur, mercury, and NOx emissions. With additional support from the NETL-Regional University Alliance (NETL-RUA), the Center will educate and train engineering students and researchers by providing hands-on 'learning by operating' experience The AVESTAR Center also offers unique collaborative R&D opportunities in high-fidelity dynamic modeling, advanced process control, real-time optimization, and virtual plant simulation. Objectives and goals are aimed at safe and effective management of power generation systems for optimal efficiency, while protecting the environment. To add another dimension of realism to the AVESTAR experience, NETL will introduce an immersive training system with innovative three-dimensional virtual reality technology. Wearing a stereoscopic headset or eyewear, trainees will enter an interactive virtual environment that will allow them to move freely throughout the simulated 3-D facility to study and learn various aspects of IGCC plant operation, control, and safety. Such combined operator and immersive training systems go beyond traditional simulation and include more realistic scenarios, improved communication, and collaboration among co-workers.

Zitney, S.; Liese, E.; Mahapatra, P.; Bhattacharyya, D.; Provost, G.

2011-01-01T23:59:59.000Z

251

EIS-0318: EPA Notice of Availability of the Final Environmental Impact  

Broader source: Energy.gov (indexed) [DOE]

EIS-0318: EPA Notice of Availability of the Final Environmental EIS-0318: EPA Notice of Availability of the Final Environmental Impact Statement EIS-0318: EPA Notice of Availability of the Final Environmental Impact Statement Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project Notice of Availability for the Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project, Constructing and Operating a 540 megawatt-electric Plant, Clean Coal Technology Program, Clark County, KY. Environmental Protection Agency Notice of Availability of the Kentucky Pioneer Integrated Gasification Combined Cycle Demonstration Project Final Environmental Impact Statement, DOE/EIS-0318 (December 2002) (67 FR 76740) More Documents & Publications EIS-0325: EPA Notice of Availability of the Final Environmental Impact

252

EIS-0409: EPA Notice of Availability of the Final Environmental Impact  

Broader source: Energy.gov (indexed) [DOE]

409: EPA Notice of Availability of the Final Environmental 409: EPA Notice of Availability of the Final Environmental Impact Statement EIS-0409: EPA Notice of Availability of the Final Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Kemper County, Mississippi Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Construction and Operation of Advanced Power Generation Plant, U.S. Army COE Section 404 Permit, Kemper County, Mississippi Notice of Availability for the Final Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Kemper County, Mississippi(DOE/EIS-0409)(05/21/2010)(75FR28612) More Documents & Publications EIS-0456: EPA Notice of Availability of the Final Environmental Impact Statement EIS-0409: EPA Notice of Availability of the Draft Environmental Impact

253

EIS-0409: EPA Notice of Availability of the Final Environmental Impact  

Broader source: Energy.gov (indexed) [DOE]

Final Environmental Final Environmental Impact Statement EIS-0409: EPA Notice of Availability of the Final Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Kemper County, Mississippi Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Construction and Operation of Advanced Power Generation Plant, U.S. Army COE Section 404 Permit, Kemper County, Mississippi Notice of Availability for the Final Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Kemper County, Mississippi(DOE/EIS-0409)(05/21/2010)(75FR28612) More Documents & Publications EIS-0456: EPA Notice of Availability of the Final Environmental Impact Statement EIS-0409: EPA Notice of Availability of the Draft Environmental Impact

254

Sensor placement algorithm development to maximize the efficiency of acid gas removal unit for integrated gasifiction combined sycle (IGCC) power plant with CO2 capture  

SciTech Connect (OSTI)

Future integrated gasification combined cycle (IGCC) power plants with CO{sub 2} capture will face stricter operational and environmental constraints. Accurate values of relevant states/outputs/disturbances are needed to satisfy these constraints and to maximize the operational efficiency. Unfortunately, a number of these process variables cannot be measured while a number of them can be measured, but have low precision, reliability, or signal-to-noise ratio. In this work, a sensor placement (SP) algorithm is developed for optimal selection of sensor location, number, and type that can maximize the plant efficiency and result in a desired precision of the relevant measured/unmeasured states. In this work, an SP algorithm is developed for an selective, dual-stage Selexol-based acid gas removal (AGR) unit for an IGCC plant with pre-combustion CO{sub 2} capture. A comprehensive nonlinear dynamic model of the AGR unit is developed in Aspen Plus Dynamics® (APD) and used to generate a linear state-space model that is used in the SP algorithm. The SP algorithm is developed with the assumption that an optimal Kalman filter will be implemented in the plant for state and disturbance estimation. The algorithm is developed assuming steady-state Kalman filtering and steady-state operation of the plant. The control system is considered to operate based on the estimated states and thereby, captures the effects of the SP algorithm on the overall plant efficiency. The optimization problem is solved by Genetic Algorithm (GA) considering both linear and nonlinear equality and inequality constraints. Due to the very large number of candidate sets available for sensor placement and because of the long time that it takes to solve the constrained optimization problem that includes more than 1000 states, solution of this problem is computationally expensive. For reducing the computation time, parallel computing is performed using the Distributed Computing Server (DCS®) and the Parallel Computing® toolbox from Mathworks®. In this presentation, we will share our experience in setting up parallel computing using GA in the MATLAB® environment and present the overall approach for achieving higher computational efficiency in this framework.

Paul, P.; Bhattacharyya, D.; Turton, R.; Zitney, S.

2012-01-01T23:59:59.000Z

255

Life cycle considerations of the flue gas desulphurization system at a lignite-fired power plant in Thailand  

Science Journals Connector (OSTI)

The Flue Gas Desulphurization (FGD) system has been installed at the biggest lignite-fired power generation plant in Thailand to reduce the large...2...emission. In order to understand the costs and benefits, bot...

Sate Sampattagul; Seizo Kato…

2004-11-01T23:59:59.000Z

256

Integrating solar Organic Rankine Cycle into a coal-fired power plant with amine-based chemical absorption for CO2 capture  

Science Journals Connector (OSTI)

Abstract A novel system integrating solar Organic Rankine Cycle (ORC) into a power plant with amine-based chemical absorption for CO2 capture is proposed. The condensation heat of ORC provides the required heat for solvent regeneration, which avoids the energy penalty caused by the steam extraction traditionally. The cascade utilization of solar energy is realized through a combined supply of power generation and condensation heat. From the aspects of technology and economics, a performance analysis is presented to compare the proposed system and three other systems based on a 300 MWe power plant. The proposed system shows better performance than that of reference systems in the power generation and emission reductions. Economic evaluation was conducted in terms of levelized costs of electricity (LCOE) and cost of CO2 removed (COR). In order to achieve lower LCOE and COR compared to the power plant integrated with solar assisted post-combustion CO2 capture (PCC), the price of ORC has to be lower than 1284.46 USD/kW under the conditions that the price of the solar field is 120 USD/m2. It is believed that the proposed system has a satisfied potential to meet the thermal demand for the solvent regeneration in the power plant with PCC.

Li Zhao; Ruikai Zhao; Shuai Deng; Yuting Tan; Yinan Liu

2014-01-01T23:59:59.000Z

257

Multiple Rankine topping cycles  

SciTech Connect (OSTI)

The efficiency of a Rankine cycle is primarily determined by the temperatures of heat addition and rejection. However, no working fluid has been identified which will operate in a Rankine cycle over an extremely wide temperature range. Multiple Rankine topping cycles offer a technique for achieving high thermal efficiencies in power plants by allowing the use of several working fluids. This paper gives a history of Rankine topping cycles, presents an analysis for the calculation of the overall efficiency of a three-module multiple Rankine cycle, and presents results from a case study for a sodium-mercury-water cycle.

McWhirter, J.D. [Argonne National Lab., Idaho Falls, ID (United States). Engineering Div.]|[Idaho State Univ., Pocatello, ID (United States). Coll. of Engineering

1995-07-01T23:59:59.000Z

258

Combined cycle power plants: A comparison between two different dynamic models to evaluate transient behaviour and residual life  

Science Journals Connector (OSTI)

Abstract The deregulated energy market and the increasing quota of electrical capacity covered by non-predictable renewable sources require strongly irregular and discontinuous operation of thermoelectric plants to satisfy users demand and compensate the variability of renewable sources. As a consequence, due to thermo-mechanical fatigue, creep and corrosion, a lifetime reduction of the most critical components occurs. The availability of a procedure able to predict the residual life of plant devices is necessary to assist the management decisions about power plants’ operation and maintenance scheduling. The first step of this procedure is the capability of simulating the plant behaviour versus time by evaluating the trends of the main thermodynamic parameters that describe the plant operation during different transient periods. In this context, the main contribution of the present paper is to propose a complete procedure able to simulate the plant dynamic behaviour and estimate the residual life reduction of some components. Indeed, two different models, developed by two different research groups, of the same single pressure heat recovery steam generator unit are presented and utilized to characterize the dynamic behaviour of the above mentioned power plant. The main thermodynamic variables during different transient operation conditions are predicted and good correspondence between the two methods is obtained. It can be also noted that, when the geometry and size of the devices are considered, the thermal inertia related to heat exchangers tubes, pipes and other physical masses causes a delay in the system response. Moreover, a residual life estimation of the most stressed component is presented.

Alberto Benato; Anna Stoppato; Stefano Bracco

2014-01-01T23:59:59.000Z

259

A COMPUTATIONAL WORKBENCH ENVIRONMENT FOR VIRTUAL POWER PLANT SIMULATION  

SciTech Connect (OSTI)

In this report is described the work effort to develop and demonstrate a software framework to support advanced process simulations to evaluate the performance of advanced power systems. Integrated into the framework are a broad range of models, analysis tools, and visualization methods that can be used for the plant evaluation. The framework provides a tightly integrated problem-solving environment, with plug-and-play functionality, and includes a hierarchy of models, ranging from fast running process models to detailed reacting CFD models. The framework places no inherent limitations on the type of physics that can be modeled, numerical techniques, or programming languages used to implement the equipment models, or the type or amount of data that can be exchanged between models. Tools are provided to analyze simulation results at multiple levels of detail, ranging from simple tabular outputs to advanced solution visualization methods. All models and tools communicate in a seamless manner. The framework can be coupled to other software frameworks that provide different modeling capabilities. Three software frameworks were developed during the course of the project. The first framework focused on simulating the performance of the DOE Low Emissions Boiler System Proof of Concept facility, an advanced pulverized-coal combustion-based power plant. The second framework targeted simulating the performance of an Integrated coal Gasification Combined Cycle - Fuel Cell Turbine (IGCC-FCT) plant configuration. The coal gasifier models included both CFD and process models for the commercially dominant systems. Interfacing models to the framework was performed using VES-Open, and tests were performed to demonstrate interfacing CAPE-Open compliant models to the framework. The IGCC-FCT framework was subsequently extended to support Virtual Engineering concepts in which plant configurations can be constructed and interrogated in a three-dimensional, user-centered, interactive, immersive environment. The Virtual Engineering Framework (VEF), in effect a prototype framework, was developed through close collaboration with NETL supported research teams from Iowa State University Virtual Reality Applications Center (ISU-VRAC) and Carnegie Mellon University (CMU). The VEF is open source, compatible across systems ranging from inexpensive desktop PCs to large-scale, immersive facilities and provides support for heterogeneous distributed computing of plant simulations. The ability to compute plant economics through an interface that coupled the CMU IECM tool to the VEF was demonstrated, and the ability to couple the VEF to Aspen Plus, a commercial flowsheet modeling tool, was demonstrated. Models were interfaced to the framework using VES-Open. Tests were performed for interfacing CAPE-Open-compliant models to the framework. Where available, the developed models and plant simulations have been benchmarked against data from the open literature. The VEF has been installed at NETL. The VEF provides simulation capabilities not available in commercial simulation tools. It provides DOE engineers, scientists, and decision makers with a flexible and extensible simulation system that can be used to reduce the time, technical risk, and cost to develop the next generation of advanced, coal-fired power systems that will have low emissions and high efficiency. Furthermore, the VEF provides a common simulation system that NETL can use to help manage Advanced Power Systems Research projects, including both combustion- and gasification-based technologies.

Mike Bockelie; Dave Swensen; Martin Denison; Adel Sarofim; Connie Senior

2004-12-22T23:59:59.000Z

260

Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems  

E-Print Network [OSTI]

DL Chase and PT Kehoe, "GE Combined-Cycle Product Line andand W Stenze, "Combined Cycle Heat Recovery Optimization,"bottoming cycle FOR combined cycle power plants," Applied

Ho, Tony

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


261

Implications of near-term coal power plant retirement for SO2 and NOX, and life cycle GHG emissions  

E-Print Network [OSTI]

prices of electricity production Plant type Unit Price Nuclear ($/MWh) 16.51 Wind ($/MWh) 201 Hydro Top SO2 100 430 95 440 100 430 Top NOX 105 350 100 380 105 345 Small, inefficient 125 410 125 405 125) Manitoba Hydro Manitoba Hydro Undertaking # 57 http://www.pub.gov.mb.ca/exhibits/mh-83.pdf. (5) Sotkiewicz

Jaramillo, Paulina

262

Optimal control system design of an acid gas removal unit for an IGCC power plants with CO2 capture  

SciTech Connect (OSTI)

Future IGCC plants with CO{sub 2} capture should be operated optimally in the face of disturbances without violating operational and environmental constraints. To achieve this goal, a systematic approach is taken in this work to design the control system of a selective, dual-stage Selexol-based acid gas removal (AGR) unit for a commercial-scale integrated gasification combined cycle (IGCC) power plant with pre-combustion CO{sub 2} capture. The control system design is performed in two stages with the objective of minimizing the auxiliary power while satisfying operational and environmental constraints in the presence of measured and unmeasured disturbances. In the first stage of the control system design, a top-down analysis is used to analyze degrees of freedom, define an operational objective, identify important disturbances and operational/environmental constraints, and select the control variables. With the degrees of freedom, the process is optimized with relation to the operational objective at nominal operation as well as under the disturbances identified. Operational and environmental constraints active at all operations are chosen as control variables. From the results of the optimization studies, self-optimizing control variables are identified for further examination. Several methods are explored in this work for the selection of these self-optimizing control variables. Modifications made to the existing methods will be discussed in this presentation. Due to the very large number of candidate sets available for control variables and due to the complexity of the underlying optimization problem, solution of this problem is computationally expensive. For reducing the computation time, parallel computing is performed using the Distributed Computing Server (DCS®) and the Parallel Computing® toolbox from Mathworks®. The second stage is a bottom-up design of the control layers used for the operation of the process. First, the regulatory control layer is designed followed by the supervisory control layer. Finally, an optimization layer is designed. In this paper, the proposed two-stage control system design approach is applied to the AGR unit for an IGCC power plant with CO{sub 2} capture. Aspen Plus Dynamics® is used to develop the dynamic AGR process model while MATLAB is used to perform the control system design and for implementation of model predictive control (MPC).

Jones, D.; Bhattacharyya, D.; Turton, R.; Zitney, S.

2012-01-01T23:59:59.000Z

263

Storing carbon dioxide in saline formations : analyzing extracted water treatment and use for power plant cooling.  

SciTech Connect (OSTI)

In an effort to address the potential to scale up of carbon dioxide (CO{sub 2}) capture and sequestration in the United States saline formations, an assessment model is being developed using a national database and modeling tool. This tool builds upon the existing NatCarb database as well as supplemental geological information to address scale up potential for carbon dioxide storage within these formations. The focus of the assessment model is to specifically address the question, 'Where are opportunities to couple CO{sub 2} storage and extracted water use for existing and expanding power plants, and what are the economic impacts of these systems relative to traditional power systems?' Initial findings indicate that approximately less than 20% of all the existing complete saline formation well data points meet the working criteria for combined CO{sub 2} storage and extracted water treatment systems. The initial results of the analysis indicate that less than 20% of all the existing complete saline formation well data may meet the working depth, salinity and formation intersecting criteria. These results were taken from examining updated NatCarb data. This finding, while just an initial result, suggests that the combined use of saline formations for CO{sub 2} storage and extracted water use may be limited by the selection criteria chosen. A second preliminary finding of the analysis suggests that some of the necessary data required for this analysis is not present in all of the NatCarb records. This type of analysis represents the beginning of the larger, in depth study for all existing coal and natural gas power plants and saline formations in the U.S. for the purpose of potential CO{sub 2} storage and water reuse for supplemental cooling. Additionally, this allows for potential policy insight when understanding the difficult nature of combined potential institutional (regulatory) and physical (engineered geological sequestration and extracted water system) constraints across the United States. Finally, a representative scenario for a 1,800 MW subcritical coal fired power plant (amongst other types including supercritical coal, integrated gasification combined cycle, natural gas turbine and natural gas combined cycle) can look to existing and new carbon capture, transportation, compression and sequestration technologies along with a suite of extracting and treating technologies for water to assess the system's overall physical and economic viability. Thus, this particular plant, with 90% capture, will reduce the net emissions of CO{sub 2} (original less the amount of energy and hence CO{sub 2} emissions required to power the carbon capture water treatment systems) less than 90%, and its water demands will increase by approximately 50%. These systems may increase the plant's LCOE by approximately 50% or more. This representative example suggests that scaling up these CO{sub 2} capture and sequestration technologies to many plants throughout the country could increase the water demands substantially at the regional, and possibly national level. These scenarios for all power plants and saline formations throughout U.S. can incorporate new information as it becomes available for potential new plant build out planning.

Dwyer, Brian P.; Heath, Jason E.; Borns, David James; Dewers, Thomas A.; Kobos, Peter Holmes; Roach, Jesse D.; McNemar, Andrea; Krumhansl, James Lee; Klise, Geoffrey T.

2010-10-01T23:59:59.000Z

264

Proportionalintegral-plus (PIP) control of the ALSTOM gasifier problem  

E-Print Network [OSTI]

469 Proportional­integral-plus (PIP) control of the ALSTOM gasifier problem C J Taylor, A P Mc the gasifier system of an integrated gasification combined cycle (IGCC) power plant. In particular of the gasifier is found to yield good control of the bench- mark, meeting most of the specified performance

Sengun, Mehmet Haluk

265

The Phase Inversion-based Coal-CO2 Slurry (PHICCOS) Feeding System  

E-Print Network [OSTI]

Analysis, and Technoeconomic Assessment by Cristina Botero Dipl.-Ing., Chemical and Bioengineering fuels, chemicals, and for generating electricity in Integrated Gasification Combined Cycle (IGCC) power plants. The latter have also been proposed as an attractive platform for carbon dioxide capture

266

Global bioenergy potential from high-lignin agricultural residue  

Science Journals Connector (OSTI)

...black walnut nut industry, nut markets...by means of gasification process of...Agriculturaland wood waste potentials...Pilot-Plant gasification of olive stone...Bbiomass and Waste IX (Inst Gas...Integrated biomass gasification combined cycle...energy.gov/industry/distributedenergy...

Venugopal Mendu; Tom Shearin; J. Elliott Campbell; Jr; Jozsef Stork; Jungho Jae; Mark Crocker; George Huber; Seth DeBolt

2012-01-01T23:59:59.000Z

267

Copyright 2007 by ASME1 Laminar Flame Speeds and Strain Sensitivities of Mixtures of H2  

E-Print Network [OSTI]

to rich. [Keywords: Syngas, laminar flame speed, reactant preheat, CO2 dilution, N2 dilution] INTRODUCTION Technologies such as integrated gasification combined cycle (IGCC) plants enable combustion of coal, biomass emissions. Synthetic gas (syngas) fuels derived from coal are particularly promising in this regard. Syngas

Seitzman, Jerry M.

268

Solid-Fueled Pressurized Chemical Looping with Flue-Gas Turbine Combined Cycle for Improved Plant Efficiency and CO{sub 2} Capture  

SciTech Connect (OSTI)

The purpose of this document is to report the final result of techno-economic analysis for the proposed 550MWe integrated pressurized chemical looping combustion combined cycle process. An Aspen Plus based model is delivered in this report along with the results from three sensitivity scenarios including the operating pressure, excess air ratio and oxygen carrier performance. A process flow diagram and detailed stream table for the base case are also provided with the overall plant energy balance, carbon balance, sulfur balance and water balance. The approach to the process and key component simulation are explained. The economic analysis (OPEX and CAPX) on four study cases via DOE NETL Reference Case 12 are presented and explained.

Liu, Kunlei; Chen, Liangyong; Zhang, Yi; Richburg, Lisa; Simpson, James; White, Jay; Rossi, Gianalfredo

2013-12-31T23:59:59.000Z

269

THE TRANSPOSED CRITICAL TEMPERATURE RANKINE THERMODYNAMIC CYCLE  

E-Print Network [OSTI]

Combined Diesel-Organic Rankine Cycle Power Plant", in25OoC) closed simple organic Rankine cycle geothermal powerthe simple closed organic Rankine cycle for a given set of

Pope, William L.

2012-01-01T23:59:59.000Z

270

A Low-Carbon Fuel Standard for California, Part 1: Technical Analysis  

E-Print Network [OSTI]

Electricity Natural gas combined cycle and renewablecoal gasification combined cycle with carbon captureand storage Natural gas combined cycle Price change and

Farrell, Alexander E.; Sperling, Dan

2007-01-01T23:59:59.000Z

271

Reading the Tea Leaves: How Utilities in the West Are Managing Carbon Regulatory Risk in their Resource Plans  

E-Print Network [OSTI]

of a natural gas-fired combined cycle gas turbine (CCGT).integrated gasification combined cycle (IGCC) generationrate exceeding that of a combined-cycle natural gas unit.

Barbose, Galen

2008-01-01T23:59:59.000Z

272

A Low-Carbon Fuel Standard for California Part 1: Technical Analysis  

E-Print Network [OSTI]

Electricity Natural gas combined cycle and renewablecoal gasification combined cycle with carbon captureand storage Natural gas combined cycle Price change and

2007-01-01T23:59:59.000Z

273

La Spezia power plant: Conversion of units 1 and 2 to combined cycle with modification of steam turbines from cross compound to tandem compound  

SciTech Connect (OSTI)

Units 1 and 2 of ENEL's La Spezia power plant, rated 310 and 325 MW respectively, are going to be converted to combined cycle. This project will be accomplished by integrating components such as gas turbines and HRSGs with some of the existing components, particularly the steam turbines, which are of the cross compound type. Since the total power of each converted unit has to be kept at 335 MW because of permitting limitations, the power delivered by the steam turbine will be limited to about 115 MW. For this reason a study was carried out to verify the possibility of having only one shaft and modifying the turbine to tandem compound. As additional investments are required for this modification, a balance was performed that also took into account the incremental heat rate and, on the other hand, the benefits from decreased maintenance and increased availability and reliability calculated for the expected useful life. The result of this balance was in favor of the modification, and a decision was taken accordingly. The turbine modification will involve replacing the whole HP section with a new combined HP-IP section while retaining the corresponding LP rotor and cylinder and making the needed changes in the valve arrangements and piping. Work on the site began in the spring of 1997 by dismantling the existing boiler so as to have the space needed to install the GTs and HRSGs. The first synchronization of the converted unit 1 is scheduled for November 1999

Magneschi, P.; Gabiccini, S.; Bracaloni, N.; Fiaschi, C.

1998-07-01T23:59:59.000Z

274

Rankine cycle leak detection via continuous monitoring  

SciTech Connect (OSTI)

Rankine cycle power plants operate on a closed cycle in which heat is transferred from a high temperature reservoir to a low temperature sink while performing useful work. leaks in this cycle cause the loss of working fluid and/or corrosion of the power plant. Both of these constitute a loss of capital assets. A severe leak can reduce the efficiency of the cycle to the extent of creating an operating loss. PNL is undertaking the development of continuous monitoring techniques to protect rankine cycle plants from such losses. The location of these continuous monitors on an organic rankine cycle is described and shown schematically.

Kindle, Cecil H.

1982-10-08T23:59:59.000Z

275

NETL: Gasifipedia  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Power: IGCC Project Examples Power: IGCC Project Examples The Puertollano IGCC Plant ELCOGAS Puertollano IGCC Plant The Puertollano integrated gasification combined cycle (IGCC) Plant is a 300 MW net demonstration project in Spain designed to use a 50/50 mixture of high-ash coal and petroleum coke. The plant first went into operation in December of 1997 and the gas turbine was first fired with synthesis gas (syngas)-produced by the plant's gasifiers-in March of 1998. Integrated Gasification Combined Cycle (IGCC) - Design Considerations for High Availability, Volume 1: Lessons from Existing Operations [PDF-823KB] (2007) -by EPRI (Electric Power Research Institute) Project Participants ELCOGAS is a consortium of eight European utilities and three technology suppliers formed in 1992 to launch the Puertollano project with the goal of

276

How To Address Data Gaps in Life Cycle Inventories: A Case Study on Estimating CO2 Emissions from Coal-Fired Electricity Plants on a Global Scale  

Science Journals Connector (OSTI)

Our framework hypothesizes that emissions from coal power plants can be explained by plant-specific factors (predictors) that include steam pressure, total capacity, plant age, fuel type, and gross domestic product (GDP) per capita of the resident nations of those plants. ... For example, Wernet et al.(5) used neural networks to estimate the cumulative energy demand (CED) of chemicals based on their molecular properties. ...

Zoran J. N. Steinmann; Aranya Venkatesh; Mara Hauck; Aafke M. Schipper; Ramkumar Karuppiah; Ian J. Laurenzi; Mark A. J. Huijbregts

2014-04-21T23:59:59.000Z

277

Economic development through biomass system integration: Volume 1  

SciTech Connect (OSTI)

This report documents a feasibility study for an integrated biomass power system, where an energy crop (alfalfa) is the feedstock for a processing plant and a power plant (integrated gasification combined cycle) in a way that benefits the facility owners. Chapters describe alfalfa basics, production risks, production economics, transportation and storage, processing, products, market analysis, business analysis, environmental impact, and policy issues. 69 figs., 63 tabs.

DeLong, M.M. [Northern States Power Co., Minneapolis, MN (United States)

1995-10-01T23:59:59.000Z

278

A Low-Carbon Fuel Standard for California Part 1: Technical Analysis  

E-Print Network [OSTI]

and power via biomass gasification. Biomass and Bioenergyrenewables Integrated coal gasification combined cycle withLubricants Waxes Naptha Gasification Ethane, Benzene, and

2007-01-01T23:59:59.000Z

279

A Low-Carbon Fuel Standard for California, Part 1: Technical Analysis  

E-Print Network [OSTI]

and power via biomass gasification. Biomass and Bioenergyrenewables Integrated coal gasification combined cycle withLubricants Waxes Naptha Gasification Ethane, Benzene, and

Farrell, Alexander E.; Sperling, Dan

2007-01-01T23:59:59.000Z

280

EIS-0431: Amended Notice of Intent to Prepare an Environmental...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Involvement Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA DOE is publishing this Amended...

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


281

EIS-0431: Draft Environmental Impact Statement | Department of...  

Energy Savers [EERE]

Statement Hydrogen Energy California's (HECA) Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA This EIS evaluates the potential...

282

EIS-0431: DOE Notice of Availability of Draft Environmental Impact...  

Broader source: Energy.gov (indexed) [DOE]

Impact Statement Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA DOE announces the availability...

283

EIS-0431: Notice of Intent to Prepare an Environmental Impact...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Impact Statement Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA Notice of Intent to prepare an...

284

EIS-0431: Extension of public comment period; Notice of public...  

Broader source: Energy.gov (indexed) [DOE]

Correction Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, CA On Monday, August 26, 2013, DOE published a...

285

EIS-0431: EPA Notice of Availability of Draft Environmental Impact...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Impact Statement Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA EPA announces the availability...

286

portfolio | netl.doe.gov  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

developing hydrogen-fueled gas turbine technology for coal-based integrated gasification combined cycle (IGCC) power generation that will improve efficiency, reduce emissions,...

287

index | netl.doe.gov  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

hydrogen-fueled gas turbine technology for coal-based integrated gasification combined cycle (IGCC) power generation that will improve efficiency, reduce emissions, lower costs,...

288

Sawdust Pyrolysis and Petroleum Coke CO2 Gasification at High Heating Rates.  

E-Print Network [OSTI]

??Clean and efficient electricity can be generated using an Integrated Gasification Combined Cycle (IGCC). Although IGCC is typically used with coal, it can also be… (more)

Lewis, Aaron D.

2011-01-01T23:59:59.000Z

289

Effects of Reducing Conditions on the Properties of Molten Slag in an Entrained Bed Gasifier  

Science Journals Connector (OSTI)

The integrated gasification combined cycle (IGCC) system combines coal gasification with gas turbine and steam turbine power generation, is the most advanced technology for cleanly generating electricity from ...

Y. Wei; H. Li; N. Yamada; A. Sato; Y. Ninomiya…

2013-01-01T23:59:59.000Z

290

EIS-0409: EPA Notice of Availability of the Draft Environmental...  

Broader source: Energy.gov (indexed) [DOE]

of the Draft Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Mississippi Notice of Availability for the Draft...

291

EIS-0409: EPA Notice of Availability of the Final Environmental...  

Broader source: Energy.gov (indexed) [DOE]

of the Final Environmental Impact Statement Kemper County Integrated Gasification Combined-Cycle (IGCC) Project, Kemper County, Mississippi Kemper County Integrated...

292

ADVANCED RESEARCH PROJECTS AGENCY - ENERGY ...  

Office of Environmental Management (EM)

WA (DOEEIS-0467) FOSSIL ENERGY 13. Hydrogen Energy California's Integrated Gasification Combined Cycle Project, CA (DOEEIS-0431) NATIONAL NUCLEAR SECURITY ADMINISTRATION 14....

293

EIS-0409: Notice of Intent to Prepare an Environmental Impact...  

Broader source: Energy.gov (indexed) [DOE]

an environmental impact statement for the proposed Kemper County Integrated Gasification Combined Cycle Project in Kemper County, Mississippi to assess the potential environmental...

294

EIS-0382: DOE Notice of Availability of the Draft Environmental...  

Broader source: Energy.gov (indexed) [DOE]

design and one-year operational demonstration of a coal-based, Integrated Gasification Combined Cycle (IGCC) electric generating facility on the Iron Range of northern...

295

Albany, OR * Archorage, AK * Morgantown...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

of products, including heat and specialty chemicals. Advanced integrated gasification combined cycle schemes require the production of clean hydrogen to fuel innovative...

296

EIS-0409: Record of Decision and Statement of Findings | Department...  

Broader source: Energy.gov (indexed) [DOE]

impact statement associated with a proposed project using Integrated Gasification Combined Cycle Technology in Kemper County, Mississippi. Record of Decision and Statement...

297

de-fe0013064 | netl.doe.gov  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

a membrane reactor (MR) with hydrogen recovery for CO2 capture in integrated gasification combined cycle (IGCC) power systems. The process utilizes previously developed hydrogen...

298

September 2014.xls  

Broader source: Energy.gov (indexed) [DOE]

WA (DOEEIS-0467) FOSSIL ENERGY 13. Hydrogen Energy California's Integrated Gasification Combined Cycle Project, CA (DOEEIS-0431) NATIONAL NUCLEAR SECURITY ADMINISTRATION 14....

299

Clean coal technology using process integration : a focus on the IGCC.  

E-Print Network [OSTI]

?? The integrated gasification combined cycle (IGCC) is the most environmentally friendly coal-fired power generation technology that offers near zero green house gas emissions. This… (more)

Madzivhandila, Vhutshilo

2011-01-01T23:59:59.000Z

300

Life-Cycle Assessment in Pesticide Product Development:? Methods and Case Study on Two Plant-Growth Regulators from Different Product Generations  

Science Journals Connector (OSTI)

Life-cycle assessment (LCA) enables a more comprehensive evaluation by additionally assessing the impacts of pesticide production and application (e.g. ... Also, the break-even point depends strongly on the yield increase data determined in field trials, which are specific to the use of growth regulators in intensive agriculture. ...

Georg Geisler; Stefanie Hellweg; Thomas B. Hofstetter; Konrad Hungerbuehler

2005-03-04T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


301

Major Demonstrations | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

Major Demonstrations Major Demonstrations Major Demonstrations A state-of-the-art integrated coal gasification combined-cycle (IGCC) power plant, Tampa Electric's Polk Power Station produces enough electricity to serve 75,000 homes. A state-of-the-art integrated coal gasification combined-cycle (IGCC) power plant, Tampa Electric's Polk Power Station produces enough electricity to serve 75,000 homes. The Office of Fossil Energy is co-funding large-scale demonstrations of clean coal technologies to hasten their adoption into the commercial marketplace. Through the year 2030, electricity consumption in the United States is expected to grow by about 1 percent per year. The ability of coal-fired generation to help meet this demand could be limited by concerns over greenhouse gas emissions. While the Major Demonstrations performed to date

302

STATEMENT OF CONSIDERATIONS REQUEST BY AIR PRODUCTS & CHEMICALS, INC. FOR AN ADVANCE  

Broader source: Energy.gov (indexed) [DOE]

& CHEMICALS, INC. FOR AN ADVANCE & CHEMICALS, INC. FOR AN ADVANCE WAIVER OF DOMESTIC AND FOREIGN INVENTION RIGHTS UNDER DOE COOPERATIVE AGREEMENT NO. DE-FC26-98FT40343; W(A)-99-017, CH-1018 The Petitioner, Air Products, & Chemicals, Inc. (APCI), was awarded this cooperative agreement for the performance of work entitled, "Development of an ITM Oxygen Technology for Integration in IGCC and Other Advanced Power Generator Systems". Under the cooperative agreement, APCI is to develop Ionic Transport Membrane (ITM Oxygen) technology for stand-alone plants for producing oxygen in tonnage quantities, and for integration of ITM Oxygen plants with Integrated Gasification Combined Cycle (IGCC) and other power generation systems. The Department of Energy's Integrated Gasification Combined Cycle

303

Page not found | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

21 - 6830 of 29,416 results. 21 - 6830 of 29,416 results. Download CX-001641: Categorical Exclusion Determination Scale-Up of Hydrogen Transport Membranes (HTM) for Integrated Gasification Combined Cycle (IGCC) and FutureGen Coal-to-Hydrogen Plants (Kingsport) CX(s) Applied: B3.6 Date: 04/23/2010 Location(s): Kingsport, Tennessee Office(s): Fossil Energy, National Energy Technology Laboratory http://energy.gov/nepa/downloads/cx-001641-categorical-exclusion-determination Download CX-001643: Categorical Exclusion Determination Scale-Up of Hydrogen Transport Membranes (HTM) for Integrated Gasification Combined Cycle (IGCC) and FutureGen Coal-to-Hydrogen Plants (Boulder) CX(s) Applied: B3.6 Date: 04/23/2010 Location(s): Boulder, Colorado Office(s): Fossil Energy, National Energy Technology Laboratory

304

U.S. DOE Office of Energy Efficiency and Renewable Energy Categorical Exclusion Determination Form  

Broader source: Energy.gov (indexed) [DOE]

Office of Energy Efficiency and Renewable Energy: Office of Energy Efficiency and Renewable Energy: Phase III Xlerator Program Funding Opportunity Number DE-FOA-0000397 Applicant Name: Mikro Systems Inc. Location: Charlottesville, VA Project Title Rapid Commercialization of Advanced Turbine Blades for Integrated Gasification Combined-Cycle Plants Proposed Action or Project Description American Recovery and Reinvestment Act: Mikro Systems, Inc., proposes a 3-year project to accelerate the commercialization of its advanced Tomo- Lithographic-Molding (TOMO) core production process though a complete development cycle for two distinct Integrated Gasification Combined-Cycle (IGCC) Row 1 turbine blades with an Original Equipment Manufacturer (OEM) partner - Siemens Energy. While Mikro's Commercialization Plan is for core

305

CX-004154: Categorical Exclusion Determination | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

4: Categorical Exclusion Determination 4: Categorical Exclusion Determination CX-004154: Categorical Exclusion Determination Rapid Commercialization of Advanced Turbine Blades for Integrated Gasification Combined-Cycle Plants CX(s) Applied: B3.6, B5.1 Date: 09/17/2010 Location(s): Charlottesville, Virginia Office(s): Energy Efficiency and Renewable Energy Mikro Systems, Inc., proposes a 3-year project to accelerate the commercialization of its advanced TomoLithographic-Molding (TOMO) core production process though a complete development cycle for two distinct Integrated Gasification Combined-Cycle (IGCC) Row 1 turbine blades with an Original Equipment Manufacturer (OEM) partner - Siemens Energy. While Mikro?s Commercialization Plan is for core production, the Phase III project would go from design through manufacture of ?test set? blade

306

High Temperature Syngas Cleanup Technology Scale-up  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

RECOVERY ACT: Scale-Up of RECOVERY ACT: Scale-Up of High-Temperature Syngas Cleanup Technology Background Coal gasification generates a synthesis gas (syngas)-predominantly a mixture of carbon monoxide (CO) and hydrogen (H 2 )-that can be used for chemical production of hydrogen, methanol, substitute natural gas (SNG), and many other industrial chemicals, or for electric power generation. Conventional integrated gasification combined cycle (IGCC) power plants use this syngas as a fuel for a combustion

307

Regional University Alliance  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Alliance Alliance Developed by the National Energy Technology Laboratory in collaboration with NETL-Regional University Alliance WVU National Research Center for Coal and Energy Fossil Consulting Services, Inc. The AVESTAR(tm) Center provides a state-of- the-art, highly realistic, dynamic simulator for a coal-fired power plant using Integrated Gasification Combined Cycle (IGCC) technology with CO 2 capture. The system is based on Invensys' DYNSIM ® software

308

Economic evaluations of coal-based combustion and gasification power plants with post-combustion CO2 capture using calcium looping cycle  

Science Journals Connector (OSTI)

Abstract Coal-based power generation sector is facing important changes to implement energy efficient carbon capture technologies to comply with emission reduction targets for transition to low carbon economy. This paper assesses CaL (Calcium Looping) as one of the innovative carbon capture options able to deliver low energy and cost penalties. The work evaluates how the integration of post-combustion calcium looping influences the economics of power plants providing up-dated techno-economic indicators. Coal-based combustion plants operated in both sub- and super-critical steam conditions were evaluated, as well as coal gasification plant using an oxygen-blown entrained-flow gasifier. As benchmark options used to quantify the carbon capture energy and cost penalties, the same power generation technologies were evaluated without CCS (Carbon capture and storage). The power plant concepts investigated in the paper generates around 545–560 MW net power with at least 90% carbon capture rate. Introduction of CaL technology for CO2 capture results in a 24–42% increase of specific capital investment, the O&M costs are increasing with 24–30% and the electricity cost with 39–48% (all compared to non-CCS cases). As the techno-economic results suggest, CaL has good application potential in combustion-based power generation.

Calin-Cristian Cormos

2014-01-01T23:59:59.000Z

309

Biogeochemical cycling in an organic-rich coastal marine basin. 9. Sources and accumulation rates of vascular plant-derived organic material  

SciTech Connect (OSTI)

The sources, degradation and burial of vascular plant debris deposited over the past several decades in the lagoonal sediments of Cape Lookout Bight, North Carolina, are quantified using alkaline cupric oxide lignin oxidation product (LOP) analysis. Non-woody angiosperms, accounting for 92 {plus minus} 32% of the recognizable sedimentary vascular plant debris, are calculated to contribute 23 {plus minus} 17% of the total organic carbon buried over the past decade. When combined with a previously established sedimentary organic carbon budget for this site a vascular plant derived carbon burial rate of 26 {plus minus}20 mole C m{sup {minus}2} yr{sup {minus}1} is calculated for this same time interval. The refractory nature and invariant depth distributions of the lignin oxidation products (LOP), when coupled with evidence for constant degradation rates of metabolizable materials, indicate that sediment accumulation at this site has been a steady state process with respect to source and burial of organic carbon since its conversion from an inner-continental shelf to a lagoonal environment during the late 1960's. Thus systematic down-core decreases in labile organic matter result from early diagenetic processes rather than input rate variations.

Haddad, R.I.; Martens, C.S. (Univ. of North Carolina, Chapel Hill (USA))

1987-11-01T23:59:59.000Z

310

Cell cycle nucleic acids, polypeptides and uses thereof  

DOE Patents [OSTI]

The invention provides isolated nucleic acids and their encoded proteins that are involved in cell cycle regulation. The invention further provides recombinant expression cassettes, host cells, transgenic plants, and antibody compositions. The present invention provides methods and compositions relating to altering cell cycle protein content, cell cycle progression, cell number and/or composition of plants.

Gordon-Kamm, William J. (Urbandale, IA); Lowe, Keith S. (Johnston, IA); Larkins, Brian A. (Tucson, AZ); Dilkes, Brian R. (Tucson, AZ); Sun, Yuejin (Westfield, IN)

2007-08-14T23:59:59.000Z

311

Natural Gas Combined Cycle  

E-Print Network [OSTI]

The “Coal Ash Corrosion Resistant Materials Testing Program ” is being conducted by B&W at Reliant Energy’s Niles plant in Niles, Ohio. The total estimated cost of $1,864,603 is co-funded by DOE contributing 37.5%, OCDO providing 33.3 % and B&W providing 17%. The remaining 12 % is in-kind contributions by Reliant Energy and tubing suppliers. Materials development is important to the power industry, and to the use of coal. Figure 1 compares the cost of electricity for subcritical and supercritical coal-fired plants with a natural gas combined cycle (NGCC) plant based on an 85 % capacity factor. This shows that at $1.20/MBtu for fuel, coal is competitive with NGCC when gas is at $3.40/MBtu or higher. An 85 % capacity factor is realistic for a coal-fired plant, but NGCC plants are currently only achieving about 60%. This gives coal an advantage if compared on the basis of cost per kW generated per year. When subcritical and supercritical plants are compared,

Dennis K. Mcdonald; Subcritical Coal Plant; Supercritical Coal Plant

312

Albany, OR * Anchorage, AK * Morgantown, WV * Pittsburgh, PA * Sugar Land, TX  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Scoping Studies to Evaluate the Benefits Scoping Studies to Evaluate the Benefits of an Advanced Dry Feed System on the Use of Low Rank Coal in Integrated Gasification Combined Cycle Background Gasification of coal or other solid feedstocks (biomass, petroleum coke, etc.) produces synthesis gas (syngas), which can be cleaned and used to produce electricity and a variety of commercial products that support the U.S. economy, decrease U.S. dependence on oil imports, and meet current and future environmental emission standards. The major challenge is cost, which needs to be reduced to make integrated gasification combined cycle (IGCC) technology competitive. An IGCC plant combines a combustion turbine operating on a gasified fuel stream--syngas--with a steam turbine to capture what would otherwise be waste heat. Currently, the estimated cost of power from IGCC is higher than

313

Cycle cover with short cycles Nicole Immorlica  

E-Print Network [OSTI]

Introduction Given a graph and a subset of marked elements (nodes, edges, or some combination thereof), a cycleCycle cover with short cycles Nicole Immorlica£ Mohammad Mahdian£ Vahab S. Mirrokni£ Abstract Cycle for variants of cycle covering problems which bound the size and/or length of the covering cycles

Immorlica, Nicole

314

Reading Comprehension - The Water Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

The Water Cycle The Water Cycle Evaporation, Condensation and Precipitation The _________ moon sun water clouds evaporates _________ fish oceans rain water from lakes and oceans. As the air rises, it cools. The water vapor condenses into tiny droplets of _________ evaporation clouds water sunshine . The droplets crowd together and form a _________ cloud lake storm precipitation . Wind blows the _________ rain sun droplet cloud towards the land. The tiny droplets join together and fall as precipitation to the _________ river lake ground cloud . The water soaks into the ground and collects in _________ rivers and lakes oceans and clouds jars and cups plants and animals . The _________ storm cycle river house that never ends has started again! A water cycle diagram. Use the diagram to identify the different parts of the water cycle:

315

An introduction to the Kalina cycle  

SciTech Connect (OSTI)

This paper is intended as a primer on the Kalina cycle--a novel, efficient power cycle that uses an ammonia-water mixture as the working fluid. The reader needs no more than a basic understanding of conventional water based Rankine cycle power plants to comprehend the basic thermodynamics, principles and arrangements of Kalina cycle power plants presented in this paper. The Kalina cycle is principally a modified Rankine cycle. The transformation starts with an important process change to the Rankine cycle--changing the working fluid in the cycle from a pure component (typically water) to a mixture of ammonia and water. The modifications that complete the transformation of the cycle from Rankine to Kalina consist of proprietary system designs that specifically exploit the virtues of the ammonia-water working fluid. These special designs, either applied individually or integrated together in a number of different combinations, comprise a family of unique Kalina cycle systems. This is somewhat analogous to the Rankine cycle which, in fact, has many design options such as reheat, regenerative heating, supercritical pressure, dual pressure, etc. all of which can be applied in a number of different combinations in a particular plant.

Micak, H.A.

1996-12-31T23:59:59.000Z

316

Thermodynamic and economic optimizations of a waste heat to power plant driven by a subcritical ORC (Organic Rankine Cycle) using pure or zeotropic working fluid  

Science Journals Connector (OSTI)

Abstract This paper carried out the thermodynamic and economic optimizations of a subcritical ORC (Organic Rankine Cycle) using a pure or a zeotropic mixture working fluid. Two pure organic compounds, i.e. n-pentane and R245fa, and their mixtures with various concentrations were used as ORC working fluid for this study. Two optimizations, i.e. exergy efficiency maximization and LCOE (Levelized Cost of Electricity) minimization, were performed to find out the optimum operating conditions of the system and to determine the best working fluid from the studied media. Hot water at temperature of 150 °C and pressure of 5 bars was used to simulate the heat source medium. Whereas, cooling water at temperature of 20 °C was considered to be the heat sink medium. The mass flow rate of heat source is fixed at 50 kg/s for the optimizations. According to the results, the n-pentane-based ORC showed the highest maximized exergy efficiency (53.2%) and the lowest minimized LCOE (0.0863 $/kWh). Regarding \\{ORCs\\} using zeotropic working fluids, 0.05 and 0.1 \\{R245fa\\} mass fraction mixtures present the comparable economic features and thermodynamic performances to the system using n-pentane at minimum LCOE. The ORC using \\{R245fa\\} represents the least profitable system.

Van Long Le; Abdelhamid Kheiri; Michel Feidt; Sandrine Pelloux-Prayer

2014-01-01T23:59:59.000Z

317

Coal Gasification Report.indb  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Integrated Coal Integrated Coal Gasification Combined Cycle: Market Penetration Recommendations and Strategies Produced for the Department of Energy (DOE)/ National Energy Technology Laboratory (NETL) and the Gasification Technologies Council (GTC) September 2004 Coal-Based Integrated Gasification Combined Cycle: Market Penetration Strategies and Recommendations Final Report Study Performed by:

318

BNL | Carbon Cycle Science  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

The Carbon Cycle Science & Technology Group aims to increase understanding The Carbon Cycle Science & Technology Group aims to increase understanding of the impacts of global change on managed and unmanaged ecosystems and improve knowledge of possible global change mitigation approaches. The group has three main focus areas. FACE Climate Change Experimental Facility Design and Management The CCS&T group is an internationally recognized leader in the development of Free Air CO2 Enrichment (FACE) research facilities. We are interested in the design and management of manipulative experiments that examine the effects of carbon dioxide, ozone, other atmospheric pollutants, temperature and precipitation on natural and managed ecosystems. FACE Plant Physiology and High Throughput Biochemical Phenotyping At FACE facilities we have studied the mechanisms that underlie the

319

PowerPoint Presentation Template  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Photo Photo Economic Analysis of Ultrasupercritical PC Plants George Booras Manager, Technology Assessment Science & Technology Division Combustion Technology University Alliance Columbus, Ohio August 4, 2003 2 Combustion Technology University Alliance Workshop, August 4, 2003, Columbus, OH Presentation Outline * Economic Analysis Methodology - Capital Cost Estimating Basis - Revenue Requirement Methodology - EPRI PC Plant Cost & Performance Model * Assessment of Competing Technologies - Conventional Pulverized Coal Plants - Integrated Gasification Combined Cycle * Breakeven Capital Cost for USC Plants * Sensitivity Analysis * Conclusions 3 Combustion Technology University Alliance Workshop, August 4, 2003, Columbus, OH Economic Analysis Methodology * USC plants offer very high efficiencies

320

Carbon Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Carbon Cycle Carbon Cycle Latest Global Carbon Budget Estimates Including CDIAC Estimates Terrestrial Carbon Management Data Sets and Analyses Carbon Dioxide Emissions from Fossil-Fuel Consumption and Cement Manufacture, (2011) Annual Fossil-Fuel CO2 Emissions: Mass of Emissions Gridded by One Degree Latitude by One Degree Longitude (2012) Monthly Fossil-Fuel CO2 Emissions: Mass of Emissions Gridded by One Degree Latitude by One Degree Longitude (2012) Annual Fossil-Fuel CO2 Emissions: Global Stable Carbon Isotopic Signature (2012) Monthly Fossil-Fuel CO2 Emissions: Isomass (δ 13C) of Emissions Gridded by One Degree Latitude by One Degree Longitude (2012) AmeriFlux - Terrestrial Carbon Dioxide, Water Vapor, and Energy Balance Measurements Estimates of Monthly CO2 Emissions and Associated 13C/12C Values

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


321

Geothermal Life Cycle Calculator  

SciTech Connect (OSTI)

This calculator is a handy tool for interested parties to estimate two key life cycle metrics, fossil energy consumption (Etot) and greenhouse gas emission (ghgtot) ratios, for geothermal electric power production. It is based solely on data developed by Argonne National Laboratory for DOE’s Geothermal Technologies office. The calculator permits the user to explore the impact of a range of key geothermal power production parameters, including plant capacity, lifetime, capacity factor, geothermal technology, well numbers and depths, field exploration, and others on the two metrics just mentioned. Estimates of variations in the results are also available to the user.

Sullivan, John

2014-03-11T23:59:59.000Z

322

Kalina combined cycle performance and operability  

SciTech Connect (OSTI)

Gas turbine combined cycles using Rankine bottoming cycles have gained broad market acceptance. The favorable plant economics derive from their high efficiency, short construction cycles and excellent environmental performance. The responsive operating characteristics of combined cycles is another key advantage for customers. Duty cycles cover the spectrum from daily start stop (DSS) to base load. Performance and economics of combined cycles have progressed with advances in gas turbine technology as well as the introduction of increasingly efficient multi-pressure Rankine bottoming cycles. Further advances in gas turbine technology and Rankine bottoming cycle performance are becoming incrementally more difficult and costly to achieve. The availability of the Kalina cycle presents a clear path toward improved combined-cycle system performance and reduced cost of electricity. This paper presents detailed performance and operating characteristics of a STAG 207FA combined cycle employing the Kalina bottoming cycle. These characteristics are compared to a conventional three-pressure reheat Rankine bottoming cycle. The Kalina cycle is shown to have performance and operability advantages throughout the range of site conditions and operating regimes, such as base load, load following, DSS duty, wet and dry cooling tower applications and unattended operation. These advantages derive from a single-pressure once-through heat recovery system, above atmospheric working fluid pressure throughout the system, above atmospheric working fluid pressure throughout the system, very high thermal efficiency ({approximately}2.0 to 2.5 percentage points better than the best Rankine), and compatibility with sub-freezing ambient conditions.

Smith, R.W.; Ranasinghe, J.; Stats, D.; Dykas, S.

1996-12-31T23:59:59.000Z

323

ENERGY UTILIZATION AND ENVIRONMENTAL CONTROL TECHNOLOGIES IN THE COAL-ELECTRIC CYCLE  

E-Print Network [OSTI]

Fluidized-Bed Steam-Electric Steam-Electric Combined-CycleCombined-Cycle Current (1974) Future Future a Source:steam plants. The combined-cycle versions of advanced

Ferrell, G.C.

2010-01-01T23:59:59.000Z

324

DOE Hydrogen Analysis Repository: Biomass Integrated Gasification  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Biomass Integrated Gasification Combined-Cycle Power Systems Biomass Integrated Gasification Combined-Cycle Power Systems Project Summary Full Title: Cost and Performance Analysis of Biomass-Based Integrated Gasification Combined-Cycle (BIGCC) Power Systems Project ID: 106 Principal Investigator: Margaret Mann Brief Description: This project examines the cost and performance potential of three biomass-based integrated gasification combined cycle (IGCC) systems--high-pressure air blown, low-pressure air blown, and low-pressure indirectly heated. Purpose Examine the cost and performance potential of three biomass-based integrated gasification combined cycle (IGCC) systems - a high pressure air-blown, a low pressure indirectly heated, and a low pressure air-blown. Performer Principal Investigator: Margaret Mann

325

Multiple Rankine topping cycles offer high efficiency  

SciTech Connect (OSTI)

The efficiency of a Rankine cycle is primarily determined by the temperatures of heat addition and heat rejection. However, no working fluid has been identified that will operate in a Rankine cycle over an extremely wide temperature range. Multiple Rankine topping cycles offer a technique for achieving high thermal efficiencies in power plants by allowing the use of several working fluids to span larger temperature ranges.

McWhirter, J.D. [Idaho State Univ., Pocatello, ID (United States)

1997-10-01T23:59:59.000Z

326

Use of experience curves to estimate the future cost of power plants with CO2 capture  

E-Print Network [OSTI]

economics of the combined cycle gas turbine—an experiencePC) and natural gas combined cycle (NGCC) plants with post-integrated gasi?cation combined cycle (IGCC) plants with

Rubin, Edward S.; Yeh, Sonia; Antes, Matt; Berkenpas, Michael; Davison, John

2007-01-01T23:59:59.000Z

327

Extension of the supercritical carbon dioxide brayton cycle to low reactor power operation: investigations using the coupled anl plant dynamics code-SAS4A/SASSYS-1 liquid metal reactor code system.  

SciTech Connect (OSTI)

Significant progress has been made on the development of a control strategy for the supercritical carbon dioxide (S-CO{sub 2}) Brayton cycle enabling removal of power from an autonomous load following Sodium-Cooled Fast Reactor (SFR) down to decay heat levels such that the S-CO{sub 2} cycle can be used to cool the reactor until decay heat can be removed by the normal shutdown heat removal system or a passive decay heat removal system such as Direct Reactor Auxiliary Cooling System (DRACS) loops with DRACS in-vessel heat exchangers. This capability of the new control strategy eliminates the need for use of a separate shutdown heat removal system which might also use supercritical CO{sub 2}. It has been found that this capability can be achieved by introducing a new control mechanism involving shaft speed control for the common shaft joining the turbine and two compressors following reduction of the load demand from the electrical grid to zero. Following disconnection of the generator from the electrical grid, heat is removed from the intermediate sodium circuit through the sodium-to-CO{sub 2} heat exchanger, the turbine solely drives the two compressors, and heat is rejected from the cycle through the CO{sub 2}-to-water cooler. To investigate the effectiveness of shaft speed control, calculations are carried out using the coupled Plant Dynamics Code-SAS4A/SASSYS-1 code for a linear load reduction transient for a 1000 MWt metallic-fueled SFR with autonomous load following. No deliberate motion of control rods or adjustment of sodium pump speeds is assumed to take place. It is assumed that the S-CO{sub 2} turbomachinery shaft speed linearly decreases from 100 to 20% nominal following reduction of grid load to zero. The reactor power is calculated to autonomously decrease down to 3% nominal providing a lengthy window in time for the switchover to the normal shutdown heat removal system or for a passive decay heat removal system to become effective. However, the calculations reveal that the compressor conditions are calculated to approach surge such that the need for a surge control system for each compressor is identified. Thus, it is demonstrated that the S-CO{sub 2} cycle can operate in the initial decay heat removal mode even with autonomous reactor control. Because external power is not needed to drive the compressors, the results show that the S-CO{sub 2} cycle can be used for initial decay heat removal for a lengthy interval in time in the absence of any off-site electrical power. The turbine provides sufficient power to drive the compressors. Combined with autonomous reactor control, this represents a significant safety advantage of the S-CO{sub 2} cycle by maintaining removal of the reactor power until the core decay heat falls to levels well below those for which the passive decay heat removal system is designed. The new control strategy is an alternative to a split-shaft layout involving separate power and compressor turbines which had previously been identified as a promising approach enabling heat removal from a SFR at low power levels. The current results indicate that the split-shaft configuration does not provide any significant benefits for the S-CO{sub 2} cycle over the current single-shaft layout with shaft speed control. It has been demonstrated that when connected to the grid the single-shaft cycle can effectively follow the load over the entire range. No compressor speed variation is needed while power is delivered to the grid. When the system is disconnected from the grid, the shaft speed can be changed as effectively as it would be with the split-shaft arrangement. In the split-shaft configuration, zero generator power means disconnection of the power turbine, such that the resulting system will be almost identical to the single-shaft arrangement. Without this advantage of the split-shaft configuration, the economic benefits of the single-shaft arrangement, provided by just one turbine and lower losses at the design point, are more important to the overall cycle performance. Therefore, the single-shaft

Moisseytsev, A.; Sienicki, J. J. (Nuclear Engineering Division)

2012-05-10T23:59:59.000Z

328

Aluto-Langano Geotermal Power Plant | Open Energy Information  

Open Energy Info (EERE)

System - Ethiopian Rift Valley Plant Information Facility Type Binary Cycle Power Plant, ORC Owner Ethiopian Electric Power Corporation Developer Ethiopian Electric Power...

329

June 2005 Pub_v2  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

June 2005 June 2005 *Sequestration in the News *Recent Publications *Events and Announcements *Legislative Activity Sequestration in the News New York Times, "Dirty Secret: Coal Plants Could Be Much Cleaner." Article discusses integrated coal gasification combined cycle (IGCC) technology. No new IGCC power plants have been built in the U.S. since the Tampa Electric plant was commissioned nearly a decade ago, and nine out of ten coal-fired power plants in the planning stages will use combustion technology. The National Commission on Energy Policy, an independent, bipartisan advisory body, has recommended that the federal government spend an additional $4 billion over 10 years to speed the power industry's

330

Conservation Screening Curves to Compare Efficiency Investments to Power Plants  

E-Print Network [OSTI]

yr) Combustion Turbine Combined- Cycle Oil Coal Steam A B oJ I J J J GAS TURBINE COMBINED-CYCLE (OIL) BASELOAD COAL I JB. Intermediate Combined-Cycle Oil This plant represents an

Koomey, J.G.

2008-01-01T23:59:59.000Z

331

Multi-Criteria Decision Analysis of Concentrated Solar Power with Thermal Energy Storage and Dry Cooling  

Science Journals Connector (OSTI)

For comparison, the ratio of life cycle GHG emissions to LCOE for pulverized coal (PC), integrated gasification combined cycle (IGCC), natural gas combined cycle (NGCC), PC with carbon capture and storage (CCS), IGCC with CCS, and NGCC with CCS are 31, 19, 12, 3, 2, and 2 kgCO2eq/$, respectively (Supporting Information Table S4, p S10). ... Poullikkas, A.Economic analysis of power generation from parabolic trough solar thermal plants for the Mediterranean region—A case study for the island of Cyprus Renewable Sustainable Energy Rev. 2009, 13 ( 9) 2474– 2484 ...

Sharon J. W. Klein

2013-11-18T23:59:59.000Z

332

Modeling and Performance Prediction of a Solar Powered Rankin Cycle/Gas Turbine Cycle  

Science Journals Connector (OSTI)

The present study is dealing with the development and implementation of an integrated solar combined cycle power plant in which heat ... its energy from the waste heat of a gas turbine unit in additional to solar

Mohammed A. Elhaj; Kassim K. Matrawy…

2007-01-01T23:59:59.000Z

333

Wood Burning Combined Cycle Power Plant  

E-Print Network [OSTI]

ESL-IE-84-04-136 Proceedings from the Sixth Annual Industrial Energy Technology Conference Volume II, Houston, TX, April 15-18, 1984 _ HEAT EXCHANGER RETURN AIR mlM SPILL FLOW INNER PIPE INSULATiON 1737'F HEATSHIELD Illlll'F \\ ...~.......- 826... ESL-IE-84-04-136 Proceedings from the Sixth Annual Industrial Energy Technology Conference Volume II, Houston, TX, April 15-18, 1984 _ HEAT EXCHANGER RETURN AIR mlM SPILL FLOW INNER PIPE INSULATiON 1737'F HEATSHIELD Illlll'F \\ ...~.......- 826...

Culley, J. W.; Bourgeois, H. S.

1984-01-01T23:59:59.000Z

334

approximately 200 megawatts (MWs) of power from TCEP, making  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

approximately 200 megawatts (MWs) of power from TCEP, making approximately 200 megawatts (MWs) of power from TCEP, making it the first U.S. purchase by a utility of low-carbon power from a commercial-scale, coal-based power plant with carbon capture. The 400-MW TCEP plant is a first-of-its-kind integrated gasification combined cycle (IGCC) poly-generation facility capable of capturing 90 percent of the carbon dioxide (CO 2 ) it produces. The $2.4-billion plant was a third round selection under DOE's Clean Coal Power Initiative

335

Comparison of Pratt and Whitney Rocketdyne IGCC and commercial IGCC performance  

SciTech Connect (OSTI)

This report compares the performance and cost of commercial Integrated Gasification Combined Cycle (IGCC) plants using General Electric Energy (GEE) and Shell gasifiers with conceptual IGCC plant designs using the Pratt and Whitney Rocketdyne (PWR) compact gasifier. the PWR gasifier is also compared with the GEEE gasifier in hydrogen production and carbon capture mode. With the exception of the PWR gasifier, the plants are designed with commercially available equipment to be operational in approximately 2010. All results should be considered preliminary and dictated in large part by the selected design basis. 10 refs., 54 exhibits

Jeffrey Hoffmann; Jenny Tennant; Gary J. Stiegel [Office of Systems Analysis and Planning (United States)

2006-06-15T23:59:59.000Z

336

Cycle Track Lessons Learned  

E-Print Network [OSTI]

Cycle Track Lessons Learned #12;Presentation Overview · Bicycling trends · Cycle track lessons learned · What is a "Cycle track"? · Essential design elements of cycle tracks Separation Width Crossing driveways & low-volume streets Signalized intersections #12;Trend in kilometers cycled per year

Bertini, Robert L.

337

Photovoltaics Life Cycle Analysis  

E-Print Network [OSTI]

Metrics of Life-Cycle Performance Energy Payback Times (EPBT) Greenhouse Gas Emissions (GHG) Toxic Gases #12;6 Life Cycle GHG Emissions ­EuropeLife Cycle GHG Emissions ­Europe Insolation: 1700 kwh/m2-yr 0 10 #12;7 Life Cycle GHG Emissions ­Comparison with Conventional Technologies Life Cycle GHG Emissions

338

An Assessment of Industrial Cogeneration Potential in Pennsylvania  

E-Print Network [OSTI]

such as atmospheric fluidized bed combustion, coal-gasification combined cycles, fuel cells and bottoming cycles were analyzed in addition to the economic assessment of conventional cogeneration systems; Industry-specific rates of market penetration were developed...

Hinkle, B. K.; Qasim, S.; Ludwig, E. V., Jr.

1983-01-01T23:59:59.000Z

339

Offshore Rankine Cycles.  

E-Print Network [OSTI]

?? The title of the thesis - "Offshore Rankine Cycles" - is very general and cover a large range of engineering fields, e.g. thermodynamic cycles… (more)

Brandsar, Jo

2012-01-01T23:59:59.000Z

340

The Organic Rankine Cycle  

Science Journals Connector (OSTI)

Chap. 3 is dedicated to Rankine cycles with organic fluids: the so-called organic Rankine cycles (ORC), which in recent years have ... of the use of...

Costante Mario Invernizzi

2013-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


341

SENSIBLE HEAT STORAGE FOR A SOLAR THERMAL POWER PLANT  

E-Print Network [OSTI]

Power Plant Solar Power Ideal Gas Turbine Topping Braytonefficiency of a solar power plant with gas-turbine toppingfor a solar power plant with Brayton-cycle gas turbine

Baldwin, Thomas F.

2011-01-01T23:59:59.000Z

342

Optimization of Air Conditioning Cycling  

E-Print Network [OSTI]

Benchmark – Long Cycle .............................................................................................. 95 5.46 System Pressures and Temperatures – Valve Part Cycle Vs Benchmark – Long Cycle...

Seshadri, Swarooph

2012-10-19T23:59:59.000Z

343

ECONOMIC EVALUATION OF CO2 STORAGE AND SINK ENHANCEMENT OPTIONS  

SciTech Connect (OSTI)

This project developed life-cycle costs for the major technologies and practices under development for CO{sub 2} storage and sink enhancement. The technologies evaluated included options for storing captured CO{sub 2} in active oil reservoirs, depleted oil and gas reservoirs, deep aquifers, coal beds, and oceans, as well as the enhancement of carbon sequestration in forests and croplands. The capture costs for a nominal 500 MW{sub e} integrated gasification combined cycle plant from an earlier study were combined with the storage costs from this study to allow comparison among capture and storage approaches as well as sink enhancements.

Bert Bock; Richard Rhudy; Howard Herzog; Michael Klett; John Davison; Danial G. De La Torre Ugarte; Dale Simbeck

2003-02-01T23:59:59.000Z

344

Power Plant Power Plant  

E-Print Network [OSTI]

Basin Center for Geothermal Energy at University of Nevada, Reno (UNR) 2 Nevada Geodetic LaboratoryStillwater Power Plant Wabuska Power Plant Casa Diablo Power Plant Glass Mountain Geothermal Area Lassen Geothermal Area Coso Hot Springs Power Plants Lake City Geothermal Area Thermo Geothermal Area

Tingley, Joseph V.

345

A Flashing Binary Combined Cycle For Geothermal Power Generation | Open  

Open Energy Info (EERE)

Flashing Binary Combined Cycle For Geothermal Power Generation Flashing Binary Combined Cycle For Geothermal Power Generation Jump to: navigation, search GEOTHERMAL ENERGYGeothermal Home Journal Article: A Flashing Binary Combined Cycle For Geothermal Power Generation Details Activities (0) Areas (0) Regions (0) Abstract: The performance of a flashing binary combined cycle for geothermal power generation is analysed. It is proposed to utilize hot residual brine from the separator in flashing-type plants to run a binary cycle, thereby producing incremental power. Parametric variations were carried out to determine the optimum performance of the combined cycle. Comparative evaluation with the simple flashing plant was made to assess its thermodynamic potential and economic viability. Results of the analyses indicate that the combined cycle can generate 13-28% more power than the

346

NPP and the Global Carbon Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

the Global Carbon Cycle the Global Carbon Cycle Introduction Photosynthetic carbon fixation comprises a major component of the global carbon cycle. Data on net primary productivity (NPP) may be sparse, but a consistent NPP data set may be used to calibrate, parameterize and evaluate models of terrestrial carbon cycling, as well as for validation of remote sensing data and other applications (identifying trends, investigating biogeochemical processes, etc.). It is also useful to place such data within the context of carbon cycling and carbon storage worldwide. For example: How much carbon exists in the biosphere, and where exactly is it stored? How much is in fossil fuels (coal, oil, gas), and how large are current fossil-fuel emissions? How much is in living biomass (plants/ animals/ humans)?

347

EIS-0431: Notice of Intent to Prepare an Environmental Impact Statement |  

Broader source: Energy.gov (indexed) [DOE]

1: Notice of Intent to Prepare an Environmental Impact 1: Notice of Intent to Prepare an Environmental Impact Statement EIS-0431: Notice of Intent to Prepare an Environmental Impact Statement Hydrogen Energy California's Integrated Gasification Combined Cycle and Carbon Capture and Sequestration Project, Kern County, CA Notice of Intent to prepare an environmental impact statement for providing financial assistance for the construction and operation of an integrated gasification combined cycle project proposed by Hydrogen Energy California LLC in Kern County, California. Hydrogen Energy California's Integrated Gasification Combined Cycle Project, Kern County, California, EIS-0431 (April 2010) (75 FR 17397) More Documents & Publications EIS-0431: Amended Notice of Intent to Prepare an Environmental Impact

348

Cell Cycle-regulated Gene Expression in Arabidopsis* Received for publication, July 26, 2002  

E-Print Network [OSTI]

Cell Cycle-regulated Gene Expression in Arabidopsis* Received for publication, July 26, 2002¨rich, Switzerland Regulated gene expression is an important mecha- nism for controlling cell cycle progression regulation de- pendent on cell cycle position. Analysis of cell cycle processes in plants has been hampered

Murray, J.A.H.

349

Combined Cycle (CC) and Combined Heat and Power (CHP) Systems: An Introduction  

Science Journals Connector (OSTI)

Combined Cycle (CC)...is a power plant system in which two types of turbines, namely a gas turbine and a steam turbine, are used to generate electricity. Moreover the turbines are combined in one cycle

Andrzej W. Ordys MScEE; PhD; A. W. Pike…

1994-01-01T23:59:59.000Z

350

Nutrient Management Module No. 3 Nitrogen Cycling,  

E-Print Network [OSTI]

, it is important to first understand the various transformations that N undergoes within the soil. Nitrogen Cycling to be the sum of ammonium and nitrate, although urea, a type of organic N, may also be plant available. Nitrogen a fraction) by dry yield (in lb/ac). It's useful to compare actual uptake rates to N fertilizer rates

Lawrence, Rick L.

351

Advanced binary cycles: Optimum working fluids  

SciTech Connect (OSTI)

A computer model (Cycle Analysis Simulation Tool, CAST) and a methodology have been developed to perform value analysis for small, low- to moderate-temperature binary geothermal power plants. The value analysis method allows for incremental changes in the levelized electricity cost (LEC) to be determined between a baseline plant and a modified plant. Thermodynamic cycle analyses and component sizing are carried out in the model followed by economic analysis which provides LEC results. The emphasis of the present work is on evaluating the effect of mixed working fluids instead of pure fluids on the LEC of a geothermal binary plant that uses a simple Organic Rankine Cycle. Four resources were studied spanning the range of 265 F to 375 F. A variety of isobutane and propane based mixtures, in addition to pure fluids, were used as working fluids. This study shows that the use of propane mixtures at a 265 F resource can reduce the LEC by 24% when compared to a base case value that utilizes commercial isobutane as its working fluid. The cost savings drop to 6% for a 375 F resource, where an isobutane mixture is favored. Supercritical cycles were found to have the lowest cost at all resources.

Gawlik, K.; Hassani, V. [National Renewable Energy Lab., Golden, CO (United States)

1997-12-31T23:59:59.000Z

352

Quantifying Carbon Cycle Feedbacks  

Science Journals Connector (OSTI)

Perturbations to the carbon cycle could constitute large feedbacks on future changes in atmospheric CO2 concentration and climate. This paper demonstrates how carbon cycle feedback can be expressed in formally similar ways to climate feedback, ...

J. M. Gregory; C. D. Jones; P. Cadule; P. Friedlingstein

2009-10-01T23:59:59.000Z

353

Edgeworth cycles revisited  

E-Print Network [OSTI]

Some gasoline markets exhibit remarkable price cycles, where price spikes are followed by a series of small price declines: a pattern consistent with a model of Edgeworth cycles described by Maskin and Tirole. We extend ...

Doyle, Joseph J.

354

The combined cycle  

Science Journals Connector (OSTI)

Any combination of at least two cyclic processes converting thermal energy (‘heat’) to work forms a combined cycle. In principle, the potential number of ... number of options reduces to a variety of cycles consi...

R. U. Pitt

1995-01-01T23:59:59.000Z

355

Water Cycle Pilot Study  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

1 Water Cycle Pilot Study To learn more about Earth's water cycle, the U.S. Department of Energy (DOE) has established a multi-laboratory science team representing five DOE...

356

Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems  

E-Print Network [OSTI]

Systems for Industrial Waste Heat Recovery. c DanielCycle for Cement Kiln Waste Heat Recovery Power Plants. ”and high temperature waste heat reclamation and solar

Ho, Tony

2012-01-01T23:59:59.000Z

357

mathematics single cycle  

E-Print Network [OSTI]

47 mathematics education single cycle master's study programme #12;48 single cycle master's study program in Mathematics Education #12;49 single cycle master's study program in Mathematics Education MATHEMATICS EDUCATION The program is in tune with the principles of the Bologna Declaration. · Academic title

Â?umer, Slobodan

358

Maintaining plant safety margins  

SciTech Connect (OSTI)

The Final Safety Analysis Report Forms the basis of demonstrating that the plant can operate safely and meet all applicable acceptance criteria. In order to assure that this continues through each operating cycle, the safety analysis is reexamined for each reload core. Operating limits are set for each reload core to assure that safety limits and applicable acceptance criteria are not exceeded for postulated events within the design basis. These operating limits form the basis for plant operation, providing barriers on various measurable parameters. The barriers are refereed to as limiting conditions for operation (LCO). The operating limits, being influenced by many factors, can change significantly from cycle to cycle. In order to be successful in demonstrating safe operation for each reload core (with adequate operating margin), it is necessary to continue to focus on ways to maintain/improve existing safety margins. Existing safety margins are a function of the plant type (boiling water reactor/pressurized water reactor (BWR/PWR)), nuclear system supply (NSSS) vendor, operating license date, core design features, plant design features, licensing history, and analytical methods used in the safety analysis. This paper summarizes the experience at Yankee Atomic Electric Company (YAEC) in its efforts to provide adequate operating margin for the plants that it supports.

Bergeron, P.A.

1989-01-01T23:59:59.000Z

359

Cycle to Cycle Manufacturing Process Control  

E-Print Network [OSTI]

Most manufacturing processes produce parts that can only be correctly measured after the process cycle has been completed. Even if in-process measurement and control is possible, it is often too expensive or complex to ...

Hardt, David E.

360

Ecosystem development explained by competition within and between material cycles  

Science Journals Connector (OSTI)

...productivities, plant and decomposer biomasses, and ecosystem cycling e ciency...increasing ecosystem productivity, biomass and cycling e ciency, thus...loblolly pine (Pinus taeda L.) plantation ecosystems: the rsttwenty...Biol. 136, 337^356. Wood, T., Bormann, F. H...

1998-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


361

Slag-washing water of blast furnace power station with supercritical organic Rankine cycle  

Science Journals Connector (OSTI)

Organic Rankine cycle (ORC) power plant operating with supercritical ... of a supercritical power plant. Two typical organic fluids with sufficiently low critical parameters were ... study the efficiency of the s...

Song Xiao ??; Shu-ying Wu ???; Dong-sheng Zheng ???

2013-03-01T23:59:59.000Z

362

Multiple reheat helium Brayton cycles for sodium fast reactors  

SciTech Connect (OSTI)

Sodium fast reactors (SFR) traditionally adopt the steam Rankine cycle for power conversion. The resulting potential for water-sodium reaction remains a continuing concern which at least partly delays the SFR technology commercialization and is a contributor to higher capital cost. Supercritical CO2 provides an alternative, but is also capable of sustaining energetic chemical reactions with sodium. Recent development on advanced inert-gas Brayton cycles could potentially solve this compatibility issue, increase thermal efficiency, and bring down the capital cost close to light water reactors. In this paper, helium Brayton cycles with multiple reheat and intercooling states are presented for SFRs with reactor outlet temperatures in the range of 510°C to 650°C. The resulting thermal efficiencies range from 39% and 47%, which is comparable with supercritical recompression CO2 cycles (SCO2 cycle). A systematic comparison between multiple reheat helium Brayton cycle and the SCO2 cycle is given, considering compatibility issues, plant site cooling temperature effect on plant efficiency, full plant cost optimization, and other important factors. The study indicates that the multiple reheat helium cycle is the preferred choice over SCO2 cycle for sodium fast reactors.

Haihua Zhao; Per F. Peterson

2008-07-01T23:59:59.000Z

363

Albany, OR * Anchorage, AK * Morgantown, WV * Pittsburgh, PA * Sugar Land, TX  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Thermal Conductivity, High Thermal Conductivity, High Durability Thermal Barrier Coatings for IGCC Environments-University of Connecticut Background Improved turbine materials are needed to withstand higher component surface temperatures and water vapor content for successful development and deployment of integrated gasification combined cycle (IGCC) power plants. Thermal barrier coatings (TBCs) in particular are required to have higher surface temperature capability, lower thermal conductivity, and resistance to attack at high temperature by contaminants such as calcium-magnesium-alumina-silicate (CMAS) and water vapor. There is also a concurrent need to address cost and availability issues associated with rare earth elements used in all low thermal conductivity TBCs.

364

Albany, OR * Anchorage, AK * Morgantown, WV * Pittsburgh, PA * Sugar Land, TX  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Cooling for IGCC Turbine Cooling for IGCC Turbine Blades-Mikro Systems Background Turbine blade and vane survivability at higher operating temperatures is the key to improving turbine engine performance for integrated gasification combined cycle (IGCC) power plants. Innovative cooling approaches are a critical enabling technology to meet this need. Mikro Systems, Inc. is applying their patented Tomo-Lithographic Molding (TOMO) manufacturing technology to produce turbine blades with significantly improved internal cooling geometries that go beyond the current manufacturing state-of-the-art to enable higher operating temperatures. This project addresses two important aspects. First is the need to increase the quality and reliability of the core manufacturing process capability to

365

Wabash inside  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

0 0 SEPTEMBER 2000 The Wabash River Coal Gasification Repowering Project An Update TOPICAL REPORT NUMBER 20 SEPTEMBER 2000 The Wabash River Coal Gasification Repowering Project A report on a project conducted jointly under a cooperative agreement between: The U.S. Department of Energy and Wabash River Coal Gasification Project Joint Venture A 262 MWe Commercial Scale Integrated Gasification Combined Cycle Power Plant An Update View of the Wabash River Coal Gasification Repowering project with the Wabash River and the flat terrain of west central Indiana in the background. Cover image: The Wabash River Coal Gasification Repowering Project Executive Summary ........................................................................................... 1 Background ........................................................................................................

366

Pinon Pine Power Project. Annual report, January--December 1994  

SciTech Connect (OSTI)

This annual report has been prepared to present the status of the Pinon Pine Project, a nominal 107 MWe (gross) integrated gasification combined-cycle (IGCC) power plant addition to Sierra Pacific Power Company`s (SPPCo) system. This project is a demonstration project cost-shared by the US Department of Energy (DOE) and SPPCo under DOE`s Clean Coal Technology (CCT) Program. The goal of the CCT Program is to demonstrate advanced coal utilization technologies that are energy efficient and reliable and that are able to achieve substantial reductions in emissions as compared with existing coal technologies.

NONE

1995-01-01T23:59:59.000Z

367

Deployment Models for Commercialized Carbon Capture and Storage  

Science Journals Connector (OSTI)

Deployment Models for Commercialized Carbon Capture and Storage† ... Several proposed integrated gasification-combined cycle and postcombustion coal CO2 capture projects are teaming with oil companies for use of the captured CO2 in EOR. ...

Richard A. Esposito; Larry S. Monroe; Julio S. Friedman

2010-08-19T23:59:59.000Z

368

Methodology for technology evaluation under uncertainty and its application in advanced coal gasification processes  

E-Print Network [OSTI]

Integrated gasification combined cycle (IGCC) technology has attracted interest as a cleaner alternative to conventional coal-fired power generation processes. While a number of pilot projects have been launched to ...

Gong, Bo, Ph. D. Massachusetts Institute of Technology

2011-01-01T23:59:59.000Z

369

Fundamental studies in hydrogen-rich combustion : instability mechanisms and dynamic mode selection  

E-Print Network [OSTI]

Hydrogen-rich alternative fuels are likely to play a significant role in future power generation systems. The emergence of the integrated gasification combined cycle (IGCC) as one of the favored technologies for incorporating ...

Speth, Raymond L., 1981-

2010-01-01T23:59:59.000Z

370

The suitability of coal gasification in India's energy sector  

E-Print Network [OSTI]

Integrated Gasification Combined Cycle (IGCC), an advanced coal-based power generation technology, may be an important technology to help India meet its future power needs. It has the potential to provide higher generating ...

Simpson, Lori Allison

2006-01-01T23:59:59.000Z

371

Energy: A Geoscience Perspective:  

Science Journals Connector (OSTI)

...2007). Integrated gasification combined cycle (IGCC...high-level nuclear waste. The nuclear industry has existed for over...solution for nuclear waste, though most experts...will likely deter the industry from a large expansion...

Allison M. Macfarlane

372

Hydrogen Energy Technology Geoff Dutton  

E-Print Network [OSTI]

Integrated gasification combined cycle (IGCC) Pyrolysis Water electrolysis Reversible fuel cell Hydrogen Hydrogen-fuelled internal combustion engines Hydrogen-fuelled turbines Fuel cells Hydrogen systems Overall expensive. Intermediate paths, employing hydrogen derived from fossil fuel sources, are already used

Watson, Andrew

373

Design for, and Evaluation of Life Cycle Performance  

E-Print Network [OSTI]

?. DESIGN FOR, AND EVALUATION OF LIFE CYCLE PERFORMANCE David J. Ahner Eldon W. Hall GENERAL ELECTRIC COMPANY SCHENECTADY, NEW YORK ABSTRACT EQUIPMENT DEGRADATION Project evaluation necessarily requires performance estimates over..., operating procedures, equipment availabilities, etc. This paper discusses the general nature, and the ther mal interaction of power plant components as individual equipment degradation occurs, describing overall plant performance trends and quant...

Ahner, D. J.; Hall, E. W.

374

NREL: TroughNet - Parabolic Trough Power Plant System Technology  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Parabolic Trough Power Plant System Technology Parabolic Trough Power Plant System Technology A parabolic trough solar power plant uses a large field of collectors to supply thermal energy to a conventional power plant. Because they use conventional power cycles, parabolic trough power plants can be hybridized-other fuels can be used to back up the solar power. Like all power cycles, trough power plants also need a cooling system to transfer waste heat to the environment. Parabolic trough power plant technologies include: Direct steam generation Fossil-fired (hybrid) backup Operation and maintenance Power cycles Steam Rankine Organic Rankine Combined Wet and dry cooling Power Cycles A photo of an aerial view of a power plant in the middle of a solar field with rows and rows of parabolic troughs tracking. The cooling towers can be seen with the water plume rising into the air. The white water tanks can be seen in the background.

375

Life Cycle Cost Estimate  

Broader source: Directives, Delegations, and Requirements [Office of Management (MA)]

Life-cycle costs (LCCs) are all the anticipated costs associated with a project or program alternative throughout its life. This includes costs from pre-operations through operations or to the end of the alternative.This chapter discusses life cycle costs and the role they play in planning.

1997-03-28T23:59:59.000Z

376

Overview of the nuclear fuel cycle  

SciTech Connect (OSTI)

The use of nuclear reactors to provide electrical energy has shown considerable growth since the first nuclear plant started commercial operation in the mid 1950s. Although the main purpose of this paper is to review the fuel cycle capabilities in the United States, the introduction is a brief review of the types of nuclear reactors in use and the world-wide nuclear capacity.

Leuze, R.E.

1982-01-01T23:59:59.000Z

377

Development of the merchant plant  

SciTech Connect (OSTI)

The co-authors of this paper are currently involved in over 1500 megawatts of merchant plant developments in the US. This paper will discuss the latest in combined cycle steam reheat ``H and G'' technology. Big improvements in heat rates along with substantial drop in installed cost will make this power cycle the leading merchant plant of the future. This paper will compare the actual present day performance and clearing price of a state-of-the-art merchant plant versus utility dispatch cost duration curves, known as ``system lambda''. Deregulation of the power market will ultimately provide an open market for these efficient plants to compete effectively against aging utility plants. Comparison of utility system heat rates versus merchant plant heat rates along with an increase need for generation capacity and forecasts of stable gas prices supports to the potential for a large scale building program of these high efficiency generators. This paper will also review the capacity crunch in the Northeast and Wisconsin and how problems with nuclear plants may accelerate the need for merchant plants. This paper will compare the required capacity for the population growth in the SERC Region and in Florida and how this will produce a potential ``hot bed'' for merchant plant development.

Wolfinger, R.; Gilliss, M.B.

1998-07-01T23:59:59.000Z

378

AVESTAR® - Smart Plant  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Plant Plant In the area of smart plant operations, AVESTAR's dynamic simulators enable researchers to analyze plant-wide performance over a wide range of operating scenarios, including plant startup (cold, warm, hot), shutdown, fuel switchovers, on-load cycling, high-load operations of 90-120% of rated capacity, and high frequency megawatt changes for automatic generation control. The dynamic simulators also let researchers analyze the plant's response to disturbances and malfunctions. The AVESTAR team is also using dynamic simulators to develop effective strategies for the operation and control of pre-combustion capture technology capable of removing at least 90% of the CO2 emissions. Achieving operational excellence can have significant impact on the extent and the rate at which commercial-scale capture processes will be scaled-up, deployed, and used in the years to come. If deployment of new CO2 capture technologies is to be accelerated, power generators must be confident in ensuring efficient, flexible, reliable, environmentally-friendly, and profitable plant operations.

379

MHD Integrated Topping Cycle Project  

SciTech Connect (OSTI)

The overall objective of the project is to design and construct prototypical hardware for an integrated MHD topping cycle, and conduct long duration proof-of-concept tests of integrated system at the US DOE Component Development and Integration Facility in Butte, Montana. The results of the long duration tests will augment the existing engineering design data base on MHD power train reliability, availability, maintainability, and performance, and will serve as a basis for scaling up the topping cycle design to the next level of development, an early commercial scale power plant retrofit. The components of the MHD power train to be designed, fabricated, and tested include: A slagging coal combustor with a rated capacity of 50 MW thermal input, capable of operation with an Eastern (Illinois {number sign}6) or Western (Montana Rosebud) coal, a segmented supersonic nozzle, a supersonic MHD channel capable of generating at least 1.5 MW of electrical power, a segmented supersonic diffuser section to interface the channel with existing facility quench and exhaust systems, a complete set of current control circuits for local diagonal current control along the channel, and a set of current consolidation circuits to interface the channel with the existing facility inverter.

Not Available

1992-01-01T23:59:59.000Z

380

Power Plant Analyser -- A computer code for power plant operation studies  

SciTech Connect (OSTI)

This paper describes Power Plant Analyser (PPA), a computer code for power plant dynamic and steady-state performance analysis. Power Plant Analyser simulates fossil power plant systems, such as drum-type, once-through, gas turbine, and combined cycle plants in a user-friendly manner. It provides a convenient tool for power engineers to understand the complex and interrelated thermodynamic processes and operating characteristics of the plant. It can also be used for conceptual training of power plant operators, and as a test bed for control and operating strategies.

Lu, S.; Hogg, B.W. [Queen`s Univ. of Belfast, Northern Ireland (United Kingdom). Dept. of Electrical and Electronic Engineering] [Queen`s Univ. of Belfast, Northern Ireland (United Kingdom). Dept. of Electrical and Electronic Engineering

1996-12-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


381

The Carbon Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

The Carbon Cycle The Carbon Cycle The global carbon cycle involves the carbon in and exchanging between the earth's atmosphere, fossil fuels, the oceans, and the vegetation and soils of the earth's terrestrial ecosystems. image Each year, the world's terrestrial ecosystems withdraw carbon from the atmosphere through photosynthesis and add it again through respiration and decay. A more detailed look at the global carbon cycle for the 1990s is shown below. The main annual fluxes in GtC yr-1 are: pre-industrial "natural" fluxes in black and "anthropogenic" fluxes in red (modified from Sarmiento and Gruber, 2006, with changes in pool sizes from Sabine et al., 2004a). The net terrestrial loss of -39 GtC is inferred from cumulative fossil fuel emissions minus atmospheric increase minus ocean storage. The loss of

382

Wetland (peat) Carbon Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Wetland (peat) Carbon Cycle Methane (CH4) is an important greenhouse gas, twenty times more potent than CO2, but atmospheric concentrations of CH4 under future climate change are...

383

IFR fuel cycle  

SciTech Connect (OSTI)

The next major milestone of the IFR program is engineering-scale demonstration of the pyroprocess fuel cycle. The EBR-II Fuel Cycle Facility has just entered a startup phase, which includes completion of facility modifications and installation and cold checkout of process equipment. This paper reviews the development of the electrorefining pyroprocess, the design and construction of the facility for the hot demonstration, the design and fabrication of the equipment, and the schedule and initial plan for its operation.

Battles, J.E.; Miller, W.E. [Argonne National Lab., IL (United States); Lineberry, M.J.; Phipps, R.D. [Argonne National Lab., Idaho Falls, ID (United States)

1992-04-01T23:59:59.000Z

384

Malone cycle refrigerator development  

SciTech Connect (OSTI)

This paper describes the progress made in demonstrating a Malone Cycle Refrigerator/Freezer. The Malone cycle is similar to the Stirling cycle but uses a supercritical fluid in place of real gas. In the approach, solid-metal diaphragms are used to seal and sweep the working volumes against the high working fluid pressures required in Malone cycle machines. This feature eliminates the friction and leakage that accounted for nearly half the losses in the best piston-defined Malone cycle machines built to date. The authors successfully built a Malone cycle refrigerator that: (1) used CO{sub 2} as the working fluid, (2) operated at pressures up to 19.3 Mpa (2,800 psi), (3) achieved a cold end metal temperatures of {minus}29 C ({minus}20 F), and (4) produced over 400 Watts of cooling at near ambient temperatures. The critical diaphragm components operated flawlessly throughout characterization and performance testing, supporting the conclusion of high reliability based on analysis of fatigue date and actual strain measurements.

Shimko, M.A.; Crowley, C.J.

1999-07-01T23:59:59.000Z

385

Design and Exergy Analysis of Combined Rankine Cycle Using LNG Cold Energy  

Science Journals Connector (OSTI)

Abstract In this study, a 90 MWe combined Rankine cycle utilizing LNG cold exergy was proposed. Utilizing LNG cold exergy and waste heat from the conventional steam cycle, this process was able to generate additional power in the CO2 organic Rankine cycle (ORC). A conventional steam cycle generates only 42 MW electric power; this combined Rankine cycle produced more than twice as much power as the conventional steam cycle while consuming the same amount of fossil fuel. Through parameter sensitivity analysis and exergy analysis, the optimum design and operating conditions were also determined. Finally, reduction of the power plant de-rate by introducing a CO2 capture process was also analyzed.

Ung Lee; Chonghun Han

2014-01-01T23:59:59.000Z

386

David_and_Herzog.PDF  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

COST OF CARBON CAPTURE COST OF CARBON CAPTURE Jeremy David and Howard Herzog Massachusetts Institute of Technology (MIT), Cambridge, MA, USA ABSTRACT We have conducted a detailed analysis of costs associated with today's technology for CO 2 separation and capture at three types of power plants: integrated coal gasification combined cycles (IGCC), pulverized coal-fired simple cycles (PC), and natural gas-fired combined cycles (NGCC). The analysis was based on studies from the literature that analyzed the economics of capturing CO 2 emitted at power plants. In this paper, we present a composite cost model and perform a sensitivity analysis to identify the cost-drivers for capture. We conclude that with new developments, CO 2 capture and sequestration can become a cost-effective mitigation pathway.

387

Helium process cycle  

DOE Patents [OSTI]

A unique process cycle and apparatus design separates the consumer (cryogenic) load return flow from most of the recycle return flow of a refrigerator and/or liquefier process cycle. The refrigerator and/or liquefier process recycle return flow is recompressed by a multi-stage compressor set and the consumer load return flow is recompressed by an independent consumer load compressor set that maintains a desirable constant suction pressure using a consumer load bypass control valve and the consumer load return pressure control valve that controls the consumer load compressor's suction pressure. The discharge pressure of this consumer load compressor is thereby allowed to float at the intermediate pressure in between the first and second stage recycle compressor sets. Utilizing the unique gas management valve regulation, the unique process cycle and apparatus design in which the consumer load return flow is separate from the recycle return flow, the pressure ratios of each recycle compressor stage and all main pressures associated with the recycle return flow are allowed to vary naturally, thus providing a naturally regulated and balanced floating pressure process cycle that maintains optimal efficiency at design and off-design process cycle capacity and conditions automatically.

Ganni, Venkatarao (Yorktown, VA)

2008-08-12T23:59:59.000Z

388

Helium process cycle  

DOE Patents [OSTI]

A unique process cycle and apparatus design separates the consumer (cryogenic) load return flow from most of the recycle return flow of a refrigerator and/or liquefier process cycle. The refrigerator and/or liquefier process recycle return flow is recompressed by a multi-stage compressor set and the consumer load return flow is recompressed by an independent consumer load compressor set that maintains a desirable constant suction pressure using a consumer load bypass control valve and the consumer load return pressure control valve that controls the consumer load compressor's suction pressure. The discharge pressure of this consumer load compressor is thereby allowed to float at the intermediate pressure in between the first and second stage recycle compressor sets. Utilizing the unique gas management valve regulation, the unique process cycle and apparatus design in which the consumer load return flow is separate from the recycle return flow, the pressure ratios of each recycle compressor stage and all main pressures associated with the recycle return flow are allowed to vary naturally, thus providing a naturally regulated and balanced floating pressure process cycle that maintains optimal efficiency at design and off-design process cycle capacity and conditions automatically.

Ganni, Venkatarao (Yorktown, VA)

2007-10-09T23:59:59.000Z

389

MHD power plant instrumentation and control  

SciTech Connect (OSTI)

The Electric Power Research Institute (EPRI) has awarded a contract to the MHD Development Corporation (MDC) to develop instrumentation and control requirements and strategies for commercial MHD power plants. MDC subcontracted MSE to do the technical development required. MSE is being assisted by Montana State University (MSU) for the topping cycle development. A computer model of a stand-alone MHD/steam plant is being constructed. The plant is based on the plant design set forth in the MDC proposal to the Federal Clean Coal Technology 5 solicitation. It consists of an MHD topping plant, a Heat Recovery Seed Recovery (HRSR) plant, and a steam turbo-generator. The model is based on the computer code used for a study of the Corette plant retrofitted with an MHD plant. Additional control strategies, based on MHD testing results and current steam bottoming plant control data, will be incorporated. A model will be devised and implemented for automatic control of the plant. Requirements regarding instrumentation and actuators will be documented. Instrumentation and actuators that are not commercially available will be identified. The role and desired characteristics of an expert system in the automated control scheme is being investigated. Start-up and shutdown procedures will be studied and load change dynamic performance will be evaluated. System response to abnormal topping cycle and off-design system operation will be investigated. This includes use of MHD topping cycle models which couple gasdynamic and electrical behavior for the study of controlling of the MHD topping cycle. A curvefitter, which uses cubic Hermitian spline interpolation functions in as many as five dimensions, allows much more accurate reproduction of nonlinear, multidimensional functions. This project will be the first to investigate plant dynamics and control using as many as seven independent variables or control inputs to the MHD topping cycle.

Lofftus, D.; Rudberg, D. [MSE Inc., Butte, MT (United States); Johnson, R.; Hammerstrom, D. [Montana State Univ., Bozeman, MT (United States)

1993-12-31T23:59:59.000Z

390

NETL: Gasifipedia  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Power Power IGCC Efficiency / Performance Consideration of efficiency and relative performance of current technology-based IGCC cycles has been made by NETL in ongoing studies.1 These include IGCC power plants based upon a few major gasification technologies, as depicted in Figure 1. Figure 1: IGCC Power Plant without CO2 Capture Figure 1. (click to enlarge) On these bases, estimated net efficiencies for near-term high efficiency ~625 MW-size (non-CC) integrated gasification combined cycle (IGCC) power plants, designed for Illinois No. 6 coal feed, without carbon dioxide (CO2) capture, range from:1 39.0% (HHV) for the GEE radiant-only plus quench gasification-based IGCC; 39.7% (HHV) for the CoP E-Gas(tm) two-stage gasification-based IGCC; 42.1% (HHV) for the Shell dry-feed gasification-based IGCC.

391

NETL: Gasification  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

CO2: CO2 Capture: Impacts on IGCC Plant Designs CO2: CO2 Capture: Impacts on IGCC Plant Designs Specific Impacts on IGCC Plant Designs from CO2 Capture In foregoing discussion, results of NETL's comprehensive study comparing the performance and cost of various fossil fuel-based power generation technologies with and without CO2 capture were reviewed. Of particular interest in that study was the companion set of integrated gasification combined cycle (IGCC) designs, using GE's gasification technology, which can be used to illustrate the design changes needed for CO2 capture. Current Technology - IGCC Plant Design Figure 1 shows a simplified block flow diagram (BFD) of a market-ready IGCC design without CO2 capture. As shown, the IGCC plant consists of the following processing islands, of which a more detailed description of each can be found in the cited NETL referenced report: 1

392

mathematical Study program cycle  

E-Print Network [OSTI]

TSW ECTS TSW Fundamentals of statistics 2 2 0 5 150 0 0 0 0 0 5 150 Probability 4 3 0 10 300 0 0 0 0 0127 mathematical statistics Master's study programms #12;128 #12;· Study program cycle: Second Statistics. In Slovenian: magister matematicne statistike (masculine), magistrica matematicne statistike

Â?umer, Slobodan

393

CLASS DESCRIPTIONS CYCLING SERIES  

E-Print Network [OSTI]

will utilize concepts from the 50-minute cycling class while going the distance to optimal health. Whether you're an avid cyclist, triathlete, or desire a longer class for a greater challenge, join us for this 75-minute AN URBANATHLETE Are you registered to compete in an adventure race like the Men's Health Urbanathlon, Warrior Dash

Pittendrigh, Barry

394

Changes in Root Surface Area, Nutrient Absorption Activity, and Root Carbohydrate Concentration during Crop Cycles of Rosa hybrida  

E-Print Network [OSTI]

Shields Ave., Davis, CA 95616, USA 2 Protected Horticulture Experiment Station National Horticulture over such crop cycles under conditions of high or low light. A sequential harvest experiment. Plant RSA did not change significantly during the high light crop cycle and averaged 14400 cm2 plant-1

Lieth, J. Heinrich

395

Developer Installed Treatment Plants  

E-Print Network [OSTI]

-installed treatment plants. These treatment plants are more commonly known as package wastewater treatment plants. 1

unknown authors

2008-01-01T23:59:59.000Z

396

Dynamic modeling of steam power cycles: Part II – Simulation of a small simple Rankine cycle system  

Science Journals Connector (OSTI)

This paper presents the second part of the work concerning the dynamic simulation of small steam cycle plants for power generation. The work is part of the preliminary study for a 600 kWe biomass fired steam power plant for which the complete open-loop, lumped parameter dynamic model of the steam cycle has been developed using the SimECS software described in Part I of this work. For these low-power plants, a dynamic simulation tool is especially useful because these systems must be designed to operate in transient mode for most of the time. The plant model presented here consists of the following components: feedwater pump, economizer, evaporator, superheater, impulse turbine, electrical generator and condenser. The primary heat source is modeled as a flue gas flow and no combustion models are incorporated yet to model the furnace. A description of the various components forming the complete steam cycle is given to illustrate the capabilities and modularity of the developed modeling technique. The model is first validated quantitatively against steady-state values obtained using a well known, reliable steady-state process modeling software. Subsequently, the dynamic validation is presented. Results can only be discussed based on the qualitative assessment of the observed trends because measurements are not available, being the plant in the preliminary design phase. The qualitative validation is based on four dynamic simulations involving three small step disturbances of different magnitude imposed on the pump rotational speed and on the flue gas mass flow and a single large ramp disturbance on the flue gas mass flow.

H. van Putten; P. Colonna

2007-01-01T23:59:59.000Z

397

High efficiency Brayton cycles using LNG  

DOE Patents [OSTI]

A modified, closed-loop Brayton cycle power conversion system that uses liquefied natural gas as the cold heat sink media. When combined with a helium gas cooled nuclear reactor, achievable efficiency can approach 68 76% (as compared to 35% for conventional steam cycle power cooled by air or water). A superheater heat exchanger can be used to exchange heat from a side-stream of hot helium gas split-off from the primary helium coolant loop to post-heat vaporized natural gas exiting from low and high-pressure coolers. The superheater raises the exit temperature of the natural gas to close to room temperature, which makes the gas more attractive to sell on the open market. An additional benefit is significantly reduced costs of a LNG revaporization plant, since the nuclear reactor provides the heat for vaporization instead of burning a portion of the LNG to provide the heat.

Morrow, Charles W. (Albuquerque, NM)

2006-04-18T23:59:59.000Z

398

A Carbon Dioxide Gas Turbine Direct Cycle with Partial Condensation for Nuclear Reactors  

SciTech Connect (OSTI)

A carbon dioxide gas turbine power generation system with a partial condensation cycle has been proposed for thermal and fast nuclear reactors, in which compression is done partly in the liquid phase and partly in the gas phase. This cycle achieves higher cycle efficiency than a He direct cycle mainly due to reduced compressor work of the liquid phase and of the carbon dioxide real gas effect, especially in the vicinity of the critical point. If this cycle is applied to a thermal reactor, efficiency of this cycle is about 55% at a reactor outlet temperature of 900 deg. C and pressure of 12.5 MPa, which is higher by about 10% than a typical helium direct gas turbine cycle plant (PBMR) at 900 deg. C and 8.4 MPa; this cycle also provides comparable cycle efficiency at the moderate core outlet temperature of 600 deg. C with that of the helium cycle at 900 deg. C. If this cycle is applied to a fast reactor, it is anticipated to be an alternative to liquid metal cooled fast reactors that can provide slightly higher cycle efficiency at the same core outlet temperature; it would eliminate safety problems, simplify the heat transport system and simplify plant maintenance. A passive decay heat removal system is realized by connecting a liquid carbon dioxide storage tank with the reactor vessel and by supplying carbon dioxide gasified from the tank to the core in case of depressurization event. (authors)

Yasuyoshi Kato; Takeshi Nitawaki; Yoshio Yoshizawa [Research Laboratory for Nuclear Reactors, Tokyo Institute of Technology, O-okayama, Meguro-ku, Tokyo, 152-8550 (Japan)

2002-07-01T23:59:59.000Z

399

D-Cycle - 4-Differential -Stroke Cycle | Department of Energy  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

-Stroke Cycle The D-Cycle offers the opportunity to use less fuel and gain more power while being able to be retrofit to an OEM and aftermarket engines deer09conti.pdf...

400

Power/desal plant evolves to meet changing needs  

SciTech Connect (OSTI)

This article reviews the design and operation of a dual purpose power/desalination plant in the Virgin Islands. The topics of the article include a description of the original plant design and operation, combined-cycle integration with existing power/desalination plant, system design, operating experience and incorporation of the St. Croix design at St. Thomas.

Atkins, T.E.; Rothgeb, G.

1993-08-01T23:59:59.000Z

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


401

Performance improvement options for the supercritical carbon dioxide brayton cycle.  

SciTech Connect (OSTI)

The supercritical carbon dioxide (S-CO{sub 2}) Brayton cycle is under development at Argonne National Laboratory as an advanced power conversion technology for Sodium-Cooled Fast Reactors (SFRs) as well as other Generation IV advanced reactors as an alternative to the traditional Rankine steam cycle. For SFRs, the S-CO{sub 2} Brayton cycle eliminates the need to consider sodium-water reactions in the licensing and safety evaluation, reduces the capital cost of the SFR plant, and increases the SFR plant efficiency. Even though the S-CO{sub 2} cycle has been under development for some time and optimal sets of operating parameters have been determined, those earlier development and optimization studies have largely been directed at applications to other systems such as gas-cooled reactors which have higher operating temperatures than SFRs. In addition, little analysis has been carried out to investigate cycle configurations deviating from the selected 'recompression' S-CO{sub 2} cycle configuration. In this work, several possible ways to improve S-CO{sub 2} cycle performance for SFR applications have been identified and analyzed. One set of options incorporates optimization approaches investigated previously, such as variations in the maximum and minimum cycle pressure and minimum cycle temperature, as well as a tradeoff between the component sizes and the cycle performance. In addition, the present investigation also covers options which have received little or no attention in the previous studies. Specific options include a 'multiple-recompression' cycle configuration, intercooling and reheating, as well as liquid-phase CO{sub 2} compression (pumping) either by CO{sub 2} condensation or by a direct transition from the supercritical to the liquid phase. Some of the options considered did not improve the cycle efficiency as could be anticipated beforehand. Those options include: a double recompression cycle, intercooling between the compressor stages, and reheating between the turbine stages. Analyses carried out as part of the current investigation confirm the possibilities of improving the cycle efficiency that have been identified in previous investigations. The options in this group include: increasing the heat exchanger and turbomachinery sizes, raising of the cycle high end pressure (although the improvement potential of this option is very limited), and optimization of the low end temperature and/or pressure to operate as close to the (pseudo) critical point as possible. Analyses carried out for the present investigation show that significant cycle performance improvement can sometimes be realized if the cycle operates below the critical temperature at its low end. Such operation, however, requires the availability of a heat sink with a temperature lower than 30 C for which applicability of this configuration is dependent upon the climate conditions where the plant is constructed (i.e., potential performance improvements are site specific). Overall, it is shown that the S-CO{sub 2} Brayton cycle efficiency can potentially be increased to 45 %, if a low temperature heat sink is available and incorporation of larger components (e.g.., heat exchangers or turbomachinery) having greater component efficiencies does not significantly increase the overall plant cost.

Moisseytsev, A.; Sienicki, J. J.; Nuclear Engineering Division

2008-07-17T23:59:59.000Z

402

Diesel organic Rankine bottoming-cycle powerplant program: Volume III. Appendices. Final report. [Using Fluorinol-85 as working fluid  

SciTech Connect (OSTI)

The final report on organic Rankine cycle power systems used to recover energy either from the waste heat of power-generating diesel engines or from waste heat from industrial plants has the following appendices which are included in this volume: major component specifications; test plan for the power conversion subsystem of the Diesel-Organic Rankine-Cycle Power Plant; environmental assessment of Fluorinol-85 which is the working fluid in the Rankine Cycle System; and applicable regulations and codes. (LCL)

Not Available

1981-10-01T23:59:59.000Z

403

S and H Cycle Engine  

SciTech Connect (OSTI)

Our thirst for energy is increasing at an astounding rate. World population growth is estimated to increase by 40% (to 8.5 billion) by 2050, with annual electrical energy usage estimated increase by 100% (to 25 terawatt-hours). We must find new means and fuels as well as significantly improve the efficiency of current power plants to accommodate this growing electrical energy demand. This demand is also growing in the field of space flight. Present energy and propulsion systems are limited in the amount of power (energy) that can be generated by today's technology. This limits the distance that can be safely traveled by manned and un-manned space systems. Space flight is primarily governed by two factors: time and energy. Increasing energy of space propulsion systems will decrease flight time or allow reaching farther out into space safely for manned exploration of our solar system. For example, a round trip manned mission to Mars would take about 400 days with a NERVA type thermal nuclear rocket. To reduce the 400 days to 80 days would require an increase of energy by a factor of five. We need to develop space propulsion systems with much greater energy capability than we have today to satisfy the expansion of space exploration. The S and H Cycle nuclear engine provides a revolutionary technological approach that can contribute significantly toward solving the World electrical energy and the space travel energy requirements. (authors)

Strobl, William C. [2906 Via Pepita, Carlsbad, Ca. 92009 (United States); Holland, Joe P. [10671 Jasper Ave., Redlands, Ca. 92374 (United States)

2002-07-01T23:59:59.000Z

404

NETL: Gasification Systems - Liquid Carbon Dioxide/Coal Slurry for Feeding  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Feed Systems Feed Systems Liquid Carbon Dioxide/Coal Slurry for Feeding Low-Rank Coal to Gasifiers Project Number: DE-FE0007977 There is increased interest in carbon capture and storage (CCS) for future coal-based power plants, and in a CCS integrated gasification plant, relatively pure, high pressure CO2 stream(s) will be available within the power plant. Electric Power Research Institute (EPRI) aims to help reduce the cost and improve the efficiency of integrated gasification combined cycle (IGCC) with CCS by using a portion of the high purity CO2 product stream as the carrier fluid to feed low rank coal (LRC) into the gasifier. EPRI proposes to confirm the potential advantages of LRC/liquid carbon dioxide (LCO2) slurries by: Conducting plant-wide technical and economic simulations.

405

HigHligHts Fossil Energy Techline, "DOE Announces Restructured FutureGen  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Announces Restructured FutureGen Announces Restructured FutureGen Approach to Demonstrate Carbon Capture and Storage Technology at Multiple Clean Coal Plants." On January 30, US Secretary of Energy Samuel W. Bodman announced a restructured approach to the FutureGen project, which involves the demonstration of carbon capture and storage (CCS) t e c h n o l o g y a t s e v e r a l commercial-scale Integrated Gasification Combined Cycle (IGCC) power plants. The US Department of Energy (DOE) said that the reorganized approach caps their financing at no more than the plant's CCS component, allowing for plants to be operational as early as 2015. Under this restructured approach, DOE believes that at least twice the amount of carbon dioxide

406

Filter system cost comparison for IGCC and PFBC power systems  

SciTech Connect (OSTI)

A cost comparison was conducted between the filter systems for two advanced coal-based power plants. The results from this study are presented. The filter system is based on a Westinghouse advanced particulate filter concept, which is designed to operate with ceramic candle filters. The Foster Wheeler second-generation 453 MWe (net) pressurized fluidized-bed combustor (PFBC) and the KRW 458 MWe (net) integrated gasification combined cycle (IGCC) power plants are used for the comparison. The comparison presents the general differences of the two power plants and the process-related filtration conditions for PFBC and IGCC systems. The results present the conceptual designs for the PFBC and IGCC filter systems as well as a cost summary comparison. The cost summary comparison includes the total plant cost, the fixed operating and maintenance cost, the variable operating and maintenance cost, and the effect on the cost of electricity (COE) for the two filter systems.

Dennis, R.A.; McDaniel, H.M.; Buchanan, T. [and others

1995-12-01T23:59:59.000Z

407

Fuel Cycle Subcommittee  

Broader source: Energy.gov (indexed) [DOE]

Report to NEAC Report to NEAC Fuel Cycle Subcommittee Meeting of April 23, 2013 Washington D.C. June 13, 2013 Burton Richter (Chair), Margaret Chu, Darleane Hoffman, Raymond Juzaitis, Sekazi K Mtingwa, Ronald P Omberg, Joy L Rempe, Dominique Warin 2 I Introduction and Summary The Fuel Cycle Subcommittee of NEAC met in Washington on April 23, 2013. The meeting focused on issues relating to the NE advanced reactor program (sections II, III, and IV), and on storage and transportation issues (section V) related to a possible interim storage program that is the first step in moving toward a new permanent repository as recommended by the Blue Ribbon Commission (BRC) and discussed in the recent response by DOE to Congress on the BRC report 1 . The agenda is given in

408

CANDU fuel cycle flexibility  

SciTech Connect (OSTI)

High neutron economy, on-power refuelling, and a simple bundle design provide a high degree of flexibility that enables CANDU (CANada Deuterium Uranium; registered trademark) reactors to be fuelled with a wide variety of fuel types. Near-term applications include the use of slightly enriched uranium (SEU), and recovered uranium (RU) from reprocessed spent Light Water Reactor (LWR) fuel. Plutonium and other actinides arising from various sources, including spent LWR fuel, can be accommodated, and weapons-origin plutonium could be destroyed by burning in CANDU. In the DUPIC fuel cycle, a dry processing method would convert spent Pressurized Water Reactor (PWR) fuel to CANDU fuel. The thorium cycle remains of strategic interest in CANDU to ensure long-term resource availability, and would be of specific interest to those countries possessing large thorium reserves, but limited uranium resources.

Torgerson, D.F.; Boczar, P.G. [Chalk River Lab., Ontario (Canada); Dastur, A.R. [AECL CANDU, Mississauga, Ontario (Canada)

1994-12-31T23:59:59.000Z

409

Rankine bottoming cycle safety analysis. Final report  

SciTech Connect (OSTI)

Vector Engineering Inc. conducted a safety and hazards analysis of three Rankine Bottoming Cycle Systems in public utility applications: a Thermo Electron system using Fluorinal-85 (a mixture of 85 mole % trifluoroethanol and 15 mole % water) as the working fluid; a Sundstrand system using toluene as the working fluid; and a Mechanical Technology system using steam and Freon-II as the working fluids. The properties of the working fluids considered are flammability, toxicity, and degradation, and the risks to both plant workers and the community at large are analyzed.

Lewandowski, G.A.

1980-02-01T23:59:59.000Z

410

USCEA fuel cycle '93  

SciTech Connect (OSTI)

The US Council for Energy Awareness sponsored the Fuel Cycle '93 conference in Dallas, Texas, on March 21-24, 1993. Over 250 participants attended, numerous papers were presented, and several panel discussions were held. The focus of most industry participants remains the formation of USEC and the pending US-Russian HEU agreement. Following are brief summaries of two key papers and the Fuel Market Issues panel discussion.

Not Available

1993-04-01T23:59:59.000Z

411

High efficiency carbonate fuel cell/turbine hybrid power cycle  

SciTech Connect (OSTI)

The hybrid power cycle studies were conducted to identify a high efficiency, economically competitive system. A hybrid power cycle which generates power at an LHV efficiency > 70% was identified that includes an atmospheric pressure direct carbonate fuel cell, a gas turbine, and a steam cycle. In this cycle, natural gas fuel is mixed with recycled fuel cell anode exhaust, providing water for reforming fuel. The mixed gas then flows to a direct carbonate fuel cell which generates about 70% of the power. The portion of the anode exhaust which is not recycled is burned and heat transferred through a heat exchanger (HX) to the compressed air from a gas turbine. The heated compressed air is then heated further in the gas turbine burner and expands through the turbine generating 15% of the power. Half the exhaust from the turbine provides air for the anode exhaust burner. All of the turbine exhaust eventually flows through the fuel cell cathodes providing the O2 and CO2 needed in the electrochemical reaction. Exhaust from the cathodes flows to a steam system (heat recovery steam generator, staged steam turbine generating 15% of the cycle power). Simulation of a 200 MW plant with a hybrid power cycle had an LHV efficiency of 72.6%. Power output and efficiency are insensitive to ambient temperature, compared to a gas turbine combined cycle; NOx emissions are 75% lower. Estimated cost of electricity for 200 MW is 46 mills/kWh, which is competitive with combined cycle where fuel cost is > $5.8/MMBTU. Key requirement is HX; in the 200 MW plant studies, a HX operating at 1094 C using high temperature HX technology currently under development by METC for coal gassifiers was assumed. A study of a near term (20 MW) high efficiency direct carbonate fuel cell/turbine hybrid power cycle has also been completed.

Steinfeld, G.; Maru, H.C. [Energy Research Corp., Danbury, CT (United States); Sanderson, R.A. [Sanderson (Robert) and Associates, Wethersfield, CT (United States)

1996-07-01T23:59:59.000Z

412

Preliminary thermodynamic study for an efficient turbo-blower external combustion Rankine cycle  

Science Journals Connector (OSTI)

This research paper presents a preliminary thermodynamic study of an innovative power plant operating under a Rankine cycle fed by an external combustion system with ... a heat exchanger, to a carbon dioxide Rankine

Manuel Romero Gómez; Javier Romero Gómez; Ramón Ferreiro Garcia…

2014-08-01T23:59:59.000Z

413

Succession of Internal Sulfur Cycles and Sulfur-Oxidizing Bacterial Communities in Microaerophilic Wastewater Biofilms  

Science Journals Connector (OSTI)

...cycle that occurs in wastewater biofilms. One of...activity in developing wastewater biofilms was analyzed...In addition, the mass balance for SO4 2, S0, and...effluent from a domestic wastewater treatment plant (Sapporo, Japan...

Satoshi Okabe; Tsukasa Ito; Kenichi Sugita; Hisashi Satoh

2005-05-01T23:59:59.000Z

414

Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems  

E-Print Network [OSTI]

Closed- Brayton-Cycle Solar Power Towers," ASME Journal ofNaF-NaBF4) cooled solar power tower plant is presented;high temperature solar power tower designs to date.

Ho, Tony

2012-01-01T23:59:59.000Z

415

Design and Optimization of a Pure Refrigerant Cycle for Natural Gas Liquefaction with Subcooling  

Science Journals Connector (OSTI)

Design and Optimization of a Pure Refrigerant Cycle for Natural Gas Liquefaction with Subcooling ... The world’s first commercial LNG plant uses the cascade process, which employs three different pure refrigerants: propane, ethane (or ethylene), and methane. ...

Inkyu Lee; Kyungjae Tak; Hweeung Kwon; Junghwan Kim; Daeho Ko; Il Moon

2014-05-14T23:59:59.000Z

416

Regulation of the Chlamydomonas Cell Cycle by a Stable, Chromatin-Associated Retinoblastoma Tumor Suppressor Complex  

Science Journals Connector (OSTI)

...Strategies and Techniques. (Cold Spring Harbor, NY: Cold Spring Harbor Laboratory Press), pp...transition: More than a cell cycle engine switch. Curr. Opin. Plant Biol...A Laboratory Manual. (Cold Spring Harbor, NY: Cold Spring Harbor...

Bradley J.S.C. Olson; Michael Oberholzer; Yubing Li; James M. Zones; Harjivan S. Kohli; Katerina Bisova; Su-Chiung Fang; Jill Meisenhelder; Tony Hunter; James G. Umen

2010-10-26T23:59:59.000Z

417

American business cycles and innovation  

E-Print Network [OSTI]

introduces the concepts of innovation and invention. The second section discusses the business cycles and highlights general causes of business cycles. The final section details the history of the iron, steel, aluminum, and pharmaceutical industries...

Hood, Michael

2013-02-22T23:59:59.000Z

418

AVESTAR® - Natural Gas Combined Cycle (NGCC) Dynamic Simulator  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Natural Gas Combined Cycle (NGCC) Dynamic Simulator Natural Gas Combined Cycle (NGCC) Dynamic Simulator A simulator that can provide future engineers with realistic, hands-on experience for operating advanced natural gas combined cycle (NGCC) power plants will soon be available at an innovative U.S. Department of Energy training center. Under a new cooperative research and development agreement signed by the Office of Fossil Energy's National Energy Technology Laboratory (NETL) and Invensys Operations Management, the partners will develop, test, and deploy a dynamic simulator and operator training system (OTS) for a generic NGCC power plant equipped for use with post-combustion carbon capture. NETL will operate the new dynamic simulator/OTS at the AVESTAR (Advanced Virtual Energy Simulation Training and Research) Center in Morgantown, W.Va.

419

Frozen plants  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Frozen plants Frozen plants Name: janicehu Status: N/A Age: N/A Location: N/A Country: N/A Date: Around 1993 Question: Why do some plants freeze and others do not? Replies: The main reason some plants freeze and others do not is that some plants do not have much water in them. Pine tree leaves have little water and are therefore difficult to freeze. Another reason is that some plants make chemicals to put into their fluids that reduce the freezing temperature. Salts and oils are some. The polyunsaturated fats found in many plants freeze at a lower temperature than the saturated fats found in many animals. Therefore plant fats are liquid (oils) at room temperature, and animal fats are solid. Plants could not use so many saturated fats as warm blooded animals do or they would freeze up solid at higher temperatures. I know little of plants but many animals can make ethylene glycol to keep themselves from freezing. Ethylene glycol is the active ingredient in car anti-freeze

420

STATEMENT OF CONSIDERATIONS REQUEST BY GENERAL ELECTRIC COMPANY, FOR AN ADVANCE WAIVER OF  

Broader source: Energy.gov (indexed) [DOE]

GENERAL ELECTRIC COMPANY, FOR AN ADVANCE WAIVER OF GENERAL ELECTRIC COMPANY, FOR AN ADVANCE WAIVER OF DOMESTIC AND FOREIGN INVENTION RIGHTS UNDER DOE COOPERATIVE AGREEMENT NO. DE-FC26-03NT41889; W(A)-04-020, CH-1189 The Petitioner, General Electric Company (GE), was awarded this cooperative agreement for the performance of work entitled, "System Study for Improved Gas Turbine Performance for Coal/IGCC Application". The purpose of the cooperative agreement is identify vital gas turbine parameters and quantify their influence in meeting the DOE Turbine Program's overall Integrated Gasification Combined Cycle (IGCC) plant goals of 50% net HHV (higher heating value) efficiency, $1000/kW capital cost, and low emissions. The study will analytically evaluate gas turbine conceptual cycle designs and quantify their influence on IGCC plant level performance. The study

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


421

Edinburgh Research Explorer Money Cycles  

E-Print Network [OSTI]

Edinburgh Research Explorer Money Cycles Citation for published version: Clausen, A & Strub, C 2014 'Money Cycles' Edinburgh School of Economics Discussion Paper Series. Link: Link to publication record date: 11. Dec. 2014 #12;Edinburgh School of Economics Discussion Paper Series Number 249 Money Cycles

Millar, Andrew J.

422

HEURISTIC SEARCH FOR HAMILTON CYCLES  

E-Print Network [OSTI]

by combining it with the remaining cycles. The following is the description of the main part of the algorithmHEURISTIC SEARCH FOR HAMILTON CYCLES IN CUBIC GRAPHS Janez ALES, Bojan MOHAR and Tomaz PISANSKI. A successful heuristic algorithm for nding Hamilton cycles in cubic graphs is described. Several graphs from

Mohar, Bojan

423

Life-Cycle Implications of Using Crop Residues for Various Energy Demands in China  

Science Journals Connector (OSTI)

The remaining 34.5% was accounted for by field burning and by a collection-loss component. ... P&Hdigestion represents a biogas power plant with gas turbines >1 MWelectr and with a conversion efficiency of 0.85 divided between electricity (0.40) and heat (0.45). ... Jia Youjian, Y. Z.; Chuangzhi, Wu. Life cycle assessment of a 4MWe biomass integrated gasification gas engines-steam turbine combined cycles power plant Acta Energiae Solaris Sin. ...

Wei Lu; Tianzhu Zhang

2010-04-28T23:59:59.000Z

424

Feasibility Study of a Multi-Purpose Computer Program for Optimizing Heat Rates in Power Cycles  

E-Print Network [OSTI]

and future needs of the power industry follows. The discussion is restricted to steam turbine cycles of fossil or nuclear power plants, although some ECC's can be employed to a wider range of applications, such as analysis of different heat sources... and future needs of the power industry follows. The discussion is restricted to steam turbine cycles of fossil or nuclear power plants, although some ECC's can be employed to a wider range of applications, such as analysis of different heat sources...

Menuchin, Y.; Singh, K. P.; Hirota, N.

1981-01-01T23:59:59.000Z

425

Carnivorous Plants  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Carnivorous Plants Carnivorous Plants Nature Bulletin No. 597-A March 27, 1976 Forest Preserve District of Cook County George W. Dunne, President Roland F. Eisenbeis, Supt. of Conservation CARNIVOROUS PLANTS Plants, generally, are eaten by insects or furnish other food for them. But there are a few families of strange plants that, instead, "eat" insects and other small animals. About 500 species are distributed over the world, from the arctic to the tropics. Most of them have peculiar leaves that not only attract insects but are equipped to trap and kill their victims. Even more remarkable is the fact that some have glands which secrete a digestive juice that softens and decomposes the animal until it is absorbed by the plant in much the same way as your stomach digests food.

426

Solar High Temperature Water-Splitting Cycle with Quantum Boost  

SciTech Connect (OSTI)

A sulfur family chemical cycle having ammonia as the working fluid and reagent was developed as a cost-effective and efficient hydrogen production technology based on a solar thermochemical water-splitting cycle. The sulfur ammonia (SA) cycle is a renewable and sustainable process that is unique in that it is an all-fluid cycle (i.e., with no solids handling). It uses a moderate temperature solar plant with the solar receiver operating at 800°C. All electricity needed is generated internally from recovered heat. The plant would operate continuously with low cost storage and it is a good potential solar thermochemical hydrogen production cycle for reaching the DOE cost goals. Two approaches were considered for the hydrogen production step of the SA cycle: (1) photocatalytic, and (2) electrolytic oxidation of ammonium sulfite to ammonium sulfate in aqueous solutions. Also, two sub-cycles were evaluated for the oxygen evolution side of the SA cycle: (1) zinc sulfate/zinc oxide, and (2) potassium sulfate/potassium pyrosulfate. The laboratory testing and optimization of all the process steps for each version of the SA cycle were proven in the laboratory or have been fully demonstrated by others, but further optimization is still possible and needed. The solar configuration evolved to a 50 MW(thermal) central receiver system with a North heliostat field, a cavity receiver, and NaCl molten salt storage to allow continuous operation. The H2A economic model was used to optimize and trade-off SA cycle configurations. Parametric studies of chemical plant performance have indicated process efficiencies of ~20%. Although the current process efficiency is technically acceptable, an increased efficiency is needed if the DOE cost targets are to be reached. There are two interrelated areas in which there is the potential for significant efficiency improvements: electrolysis cell voltage and excessive water vaporization. Methods to significantly reduce water evaporation are proposed for future activities. Electrolysis membranes that permit higher temperatures and lower voltages are attainable. The oxygen half cycle will need further development and improvement.

Taylor, Robin [SAIC] [SAIC; Davenport, Roger [SAIC] [SAIC; Talbot, Jan [UCSD] [UCSD; Herz, Richard [UCSD] [UCSD; Genders, David [Electrosynthesis Co.] [Electrosynthesis Co.; Symons, Peter [Electrosynthesis Co.] [Electrosynthesis Co.; Brown, Lloyd [TChemE] [TChemE

2014-04-25T23:59:59.000Z

427

Frostbite Theater - Monarch Butterflies - Life Cycle of the Monarch  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Measure the Diameter of the Sun! Measure the Diameter of the Sun! Previous Video (Let's Measure the Diameter of the Sun!) Frostbite Theater Main Index Next Video (Monarch Butterfly Pupation) Monarch Butterfly Pupation Life Cycle of the Monarch Butterfly Follow the life cycle of the Monarch butterfly from egg to adult! [ Show Transcript ] Announcer: Frostbite Theater presents... Cold Cuts! No baloney! Joanna and Steve: Just science! Joanna: Hi! I'm Joanna! Steve: And I'm Steve! Joanna: And this is a field that used to house a bunch of ugly trailers that were used for office space. A couple of years ago the Lab tore them down and in an effort to cut the cost of lawn maintanence, they planted a bunch of wild flowers in their place. Steve: Last year Joanna and I planted this plant. This is milkweed. It's a

428

n-step cycle inequalities - Optimization Online  

E-Print Network [OSTI]

also introduced the so-called cycle inequalities (called 1-step cycle inequalities in this ...... combination of the cycle detection strategy of Tarjan [16] and the ...

2014-07-02T23:59:59.000Z

429

Life-cycle Assessment of Semiconductors  

E-Print Network [OSTI]

life-cycle energy requirements (e total ) and global warmingtotal life-cycle global warming impacts. Chapter 3 Life-cycle Energy and Global

Boyd, Sarah B.

2009-01-01T23:59:59.000Z

430

DOE Hydrogen Analysis Repository: Life Cycle Analysis of Vehicles for  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Life Cycle Analysis of Vehicles for Canada Life Cycle Analysis of Vehicles for Canada Project Summary Full Title: Life Cycle Analysis of Vehicles Powered by a Fuel Cell and by Internal Combustion Engine for Canada Project ID: 117 Principal Investigator: Xianguo Li Purpose In this study, a full life cycle analysis of an internal combustion engine vehicle (ICEV) and a fuel cell vehicle (FCV) has been carried out. The impact of the material and fuel used in the vehicle on energy consumption and carbon dioxide emissions is analyzed for Canada. Four different methods of obtaining hydrogen were analyzed; using coal and nuclear power to produce electricity and extraction of hydrogen through electrolysis and via steam reforming of natural gas in a natural gas plant and in a hydrogen refueling station.

431

Solid looping cycles: A new technology for coal conversion  

SciTech Connect (OSTI)

This article examines both oxygen looping cycles (otherwise known as chemical looping combustion), and lime-based CO{sub 2} looping cycles, where calcined limestone is used for in situ CO{sub 2} capture. There has been a rapid rise in the amount of research carried out recently, and both technologies are likely to see practical application in the near future. However, these technologies urgently require demonstration at the large pilot-plant level - in the case of chemical looping cycles for use with high-pressure syngas of the type likely to be produced by current coal gasification technologies and in the case of CO{sub 2} looping cycles both for combustion and gasification applications with coal. Both approaches have potential for application in schemes for H{sub 2} production, but these have not been considered here, although such applications will also inevitably follow in the medium to long term.

Anthony, E.J. [CANMET Energy Technology Centre Ottawa, Ottawa, ON (Canada). Natural Resources Canada

2008-03-19T23:59:59.000Z

432

Quantum thermodynamic cooling cycle  

E-Print Network [OSTI]

The quantum-mechanical and thermodynamic properties of a 3-level molecular cooling cycle are derived. An inadequacy of earlier models is rectified in accounting for the spontaneous emission and absorption associated with the coupling to the coherent driving field via an environmental reservoir. This additional coupling need not be dissipative, and can provide a thermal driving force - the quantum analog of classical absorption chillers. The dependence of the maximum attainable cooling rate on temperature, at ultra-low temperatures, is determined and shown to respect the recently-established fundamental bound based on the second and third laws of thermodynamics.

Palao, J P; Gordon, J M; Palao, Jose P.; Kosloff, Ronnie; Gordon, Jeffrey M.

2001-01-01T23:59:59.000Z

433

Quantum thermodynamic cooling cycle  

E-Print Network [OSTI]

The quantum-mechanical and thermodynamic properties of a 3-level molecular cooling cycle are derived. An inadequacy of earlier models is rectified in accounting for the spontaneous emission and absorption associated with the coupling to the coherent driving field via an environmental reservoir. This additional coupling need not be dissipative, and can provide a thermal driving force - the quantum analog of classical absorption chillers. The dependence of the maximum attainable cooling rate on temperature, at ultra-low temperatures, is determined and shown to respect the recently-established fundamental bound based on the second and third laws of thermodynamics.

Jose P. Palao; Ronnie Kosloff; Jeffrey M. Gordon

2001-06-08T23:59:59.000Z

434

FUEL CELL/MICRO-TURBINE COMBINED CYCLE  

SciTech Connect (OSTI)

A wide variety of conceptual design studies have been conducted that describe ultra-high efficiency fossil power plant cycles. The most promising of these ultra-high efficiency cycles incorporate high temperature fuel cells with a gas turbine. Combining fuel cells with a gas turbine increases overall cycle efficiency while reducing per kilowatt emissions. This study has demonstrated that the unique approach taken to combining a fuel cell and gas turbine has both technical and economic merit. The approach used in this study eliminates most of the gas turbine integration problems associated with hybrid fuel cell turbine systems. By using a micro-turbine, and a non-pressurized fuel cell the total system size (kW) and complexity has been reduced substantially from those presented in other studies, while maintaining over 70% efficiency. The reduced system size can be particularly attractive in the deregulated electrical generation/distribution environment where the market may not demand multi-megawatt central stations systems. The small size also opens up the niche markets to this high efficiency, low emission electrical generation option.

Larry J. Chaney; Mike R. Tharp; Tom W. Wolf; Tim A. Fuller; Joe J. Hartvigson

1999-12-01T23:59:59.000Z

435

Optimum Heat Power Cycles for Process Industrial Plants  

E-Print Network [OSTI]

Electric power cogeneration is compared with direct mechanical drives emphasizing the technical aspects having the greatest impact on energy economics. Both steam and gas turbine applications are discussed and practical methods of developing...

Waterland, A. F.

1982-01-01T23:59:59.000Z

436

Power conversion unit studies for the next generation nuclear plant coupled to a high-temperature steam electrolysis facility  

E-Print Network [OSTI]

turbines and 4 compressors, a combined cycle with a Brayton top cycle and a Rankine bottoming cycle, and a reheated cycle with 3 stages of reheat were investigated. A high temperature steam electrolysis hydrogen production plant was coupled to the reactor...

Barner, Robert Buckner

2007-04-25T23:59:59.000Z

437

STATEMENT OF CONSIDERATIONS REQUEST BY GE ENERGY (USA) LLC, FOR AN ADVANCE WAIVER OF  

Broader source: Energy.gov (indexed) [DOE]

859; W(A)-2012-018 859; W(A)-2012-018 ; CH-1661 GE Energy (USA) LLC (GE), requests an advance waiver of domestic and foreign patent rights for all subject inventions made under the above cooperative agreement for work entitled , "Feasibility Studies to Improve Plant Availability and Reduce Total Installed Cost in IGCC Plants". Under this agreement, GE will evaluate several factors that make the cost of implementing integrated gasification combined cycle (IGCC) power production challenging . Specifically, GE will evaluate the effects on total installed cost and availability through deployment of a multi-faceted approach in three areas: Technology Evaluation ; Constructability; and , Design methodology. The end result is to reduce the time to technologica l maturity and enable plants to reach higher

438

NETL: LabNotes - March 2011  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

March 2011 March 2011 Push for Higher Efficiency Turbines Drives Innovation The National Energy Technology Laboratory (NETL) is developing technology to make coal-burning power plants more efficient and cleaner. Higher efficiencies will mean that less coal is burned, and thus, less greenhouse gases are generated. However, in order to reduce greenhouse gas emissions substantially, the power plants must also be designed to capture, rather than emit, CO2. To meet these challenges, research is underway on coal gasification, ways to separate the CO2 from a mixed gas stream (either before or after combustion) so it can be geologically sequestered, oxy-fuel pulverized coal (PC) combustion, and advanced turbines for integrated gasification combined cycle (IGCC) power plants.

439

DOE Selects Projects to Develop Pre-Combustion Carbon Capture Technologies  

Broader source: Energy.gov (indexed) [DOE]

Develop Pre-Combustion Carbon Capture Develop Pre-Combustion Carbon Capture Technologies for Coal-Based Gasification Plants DOE Selects Projects to Develop Pre-Combustion Carbon Capture Technologies for Coal-Based Gasification Plants June 11, 2009 - 1:00pm Addthis Washington, DC - The U.S. Department of Energy (DOE) today announced the selection of nine projects that will develop pre-combustion carbon capture technologies that can reduce CO2 emissions in future coal-based integrated gasification combined cycle (IGCC) power plants. The projects, totaling nearly $14.4 million, will be managed by the Office of Fossil Energy's National Energy Technology Laboratory. Pre-combustion processes convert fossil fuels into a gaseous mixture of hydrogen and CO2 prior to combustion. The CO2 is then separated and the

440

Page not found | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

31 - 22440 of 31,917 results. 31 - 22440 of 31,917 results. Download CX-008492: Categorical Exclusion Determination Carbon Dioxide Capture from Integrated Gasification Combined Cycle Gas Streams Using the Ammonium Carbonate-Ammonium Bicarbonate Process CX(s) Applied: A9 Date: 07/23/2012 Location(s): Texas Offices(s): National Energy Technology Laboratory http://energy.gov/nepa/downloads/cx-008492-categorical-exclusion-determination Event PV Power Plants Conference USA 2012 The 4th PV Power Plants conference will cover relevant topics for successful project development and sustainable business. This year's event will have an additional focus on certain distributed... http://energy.gov/indianenergy/events/pv-power-plants-conference-usa-2012 Article 2012 Transmission and Energy Storage Peer Review Presentations

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


441

An Update of the U.S. Clean Coal Technology Demonstration Program Office of Fossil Energy, U.S. Department of Energy  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Advanced Power Generation Future Bright Advanced Power Generation Future Bright With Coal Gasification-Combined Cycle Clean Coal Briefs Six Major Projects in DOE's CCT Program American Electric Power's (AEP) Tidd plant continues to break new ground in its performance as the Nation's first operating pressurized lluidized hcd combustion (PFBC) power plant. In rcccnt operations at Ohio Power Company's Brilliant, Ohio plant site, the unit reached a gross electric power output of 71 megawatts--its full power capacity. Two other milestones--a maximum bed height of 140 inches and a nrar- maximum bed temperature of I575 degrees F-were also attained during the tests. Power production in the U.S. is expected to increase rapidly during the next 20 years. Totalconsumption ofelectricity isexpectedtoriscfrom 2.7 trillionkilnvett-

442

DIFFUSION COATINGS FOR CORROSION RESISTANT COMPONENTS IN COAL GASIFICATION SYSTEMS  

SciTech Connect (OSTI)

Advanced electric power generation systems use a coal gasifier to convert coal to a gas rich in fuels such as H{sub 2} and CO. The gas stream contains impurities such as H{sub 2}S and HCl, which attack metal components of the coal gas train, causing plant downtime and increasing the cost of power generation. Corrosion-resistant coatings would improve plant availability and decrease maintenance costs, thus allowing the environmentally superior integrated gasification combined cycle plants to be more competitive with standard power-generation technologies. A startup meeting was held at the National Energy Technology Center, Pittsburgh, PA site on July 28, 2003. SRI staff described the technical approach of the project.

Gopala N. Krishnan

2004-05-01T23:59:59.000Z

443

Hybrid Cooling for Geothermal Power Plants: Final ARRA Project...  

Office of Scientific and Technical Information (OSTI)

(NREL) at www.nrel.govpublications. Executive Summary Many binary-cycle geothermal power plants use air as the heat rejection medium. An air-cooled condenser (ACC) system is...

444

Energy Department Report Calculates Emissions and Costs of Power Plant  

Broader source: Energy.gov (indexed) [DOE]

Report Calculates Emissions and Costs of Power Report Calculates Emissions and Costs of Power Plant Cycling Necessary for Increased Wind and Solar in the West Energy Department Report Calculates Emissions and Costs of Power Plant Cycling Necessary for Increased Wind and Solar in the West September 24, 2013 - 10:08am Addthis A new report released today by the Energy Department's National Renewable Energy Laboratory (NREL) examines the potential impacts of increasing wind and solar power generation on the operators of coal and gas plants in the West. To accommodate higher amounts of wind and solar power on the electric grid, utilities must ramp down and ramp up or stop and start conventional generators more frequently to provide reliable power for their customers - a practice called cycling. Grid operators typically cycle power plants to accommodate fluctuations in

445

Thermodynamic Cycle Selection for Distributed Natural Gas Liquefaction  

Science Journals Connector (OSTI)

Natural gas liquefaction plants with cooling capacities of approximately 100 kW are facilitating the development of a distributed LNG infrastructure. To be economically viable liquefiers of this scale must be able to operate on a variety of feed gases while offering relatively low capital costs short delivery time and good performance. This paper opens with a discussion of a natural gas liquefier design focusing on the refrigeration system. Linde cascade mixed refrigerant and modified?Brayton cycle refrigeration systems are then discussed in context of the overall plant design. Next a detailed comparison of the modified?Brayton and mixed refrigerant cycles is made including cycle selection’s impact on main system components like the recuperative heat exchanger and compressors. In most cases a reverse?Brayton or a mixed refrigerant cycle refrigerator is the best?suited available technology for local liquefaction. The mixed refrigerant cycle liquefier offers the potential of better real performance at lower capital costs but requires more know?how in the areas of two?phase flow and refrigerant composition management heat exchanger design and process control.

M. A. Barclay; D. F. Gongaware; K. Dalton; M. P. Skrzypkowski

2004-01-01T23:59:59.000Z

446

Open cycle thermoacoustics  

SciTech Connect (OSTI)

A new type of thermodynamic device combining a thermodynamic cycle with the externally applied steady flow of an open thermodynamic process is discussed and experimentally demonstrated. The gas flowing through this device can be heated or cooled in a series of semi-open cyclic steps. The combination of open and cyclic flows makes possible the elimination of some or all of the heat exchangers (with their associated irreversibility). Heat is directly exchanged with the process fluid as it flows through the device when operating as a refrigerator, producing a staging effect that tends to increase First Law thermodynamic efficiency. An open-flow thermoacoustic refrigerator was built to demonstrate this concept. Several approaches are presented that describe the physical characteristics of this device. Tests have been conducted on this refrigerator with good agreement with a proposed theory.

Reid, Robert Stowers

2000-01-01T23:59:59.000Z

447

Simulation for Year-Round Nutrient Uptake of Greenhouse Roses over Flowering Cycles  

E-Print Network [OSTI]

65 Simulation for Year-Round Nutrient Uptake of Greenhouse Roses over Flowering Cycles Wan-Soon Kim Protected Horticulture Experiment Station NHRI, RDA Busan 618-800 Korea Dept. of Plant Sciences University of roses, coupled with a whole-plant growth model based on light use efficiency (LUE). The study consisted

Lieth, J. Heinrich

448

Advanced regenerative absorption refrigeration cycles  

DOE Patents [OSTI]

Multi-effect regenerative absorption cycles which provide a high coefficient of performance (COP) at relatively high input temperatures. An absorber-coupled double-effect regenerative cycle (ADR cycle) (10) is provided having a single-effect absorption cycle (SEA cycle) (11) as a topping subcycle and a single-effect regenerative absorption cycle (1R cycle) (12) as a bottoming subcycle. The SEA cycle (11) includes a boiler (13), a condenser (21), an expansion device (28), an evaporator (31), and an absorber (40), all operatively connected together. The 1R cycle (12) includes a multistage boiler (48), a multi-stage resorber (51), a multisection regenerator (49) and also uses the condenser (21), expansion device (28) and evaporator (31) of the SEA topping subcycle (11), all operatively connected together. External heat is applied to the SEA boiler (13) for operation up to about 500 degrees F., with most of the high pressure vapor going to the condenser (21) and evaporator (31) being generated by the regenerator (49). The substantially adiabatic and isothermal functioning of the SER subcycle (12) provides a high COP. For higher input temperatures of up to 700 degrees F., another SEA cycle (111) is used as a topping subcycle, with the absorber (140) of the topping subcycle being heat coupled to the boiler (13) of an ADR cycle (10). The 1R cycle (12) itself is an improvement in that all resorber stages (50b-f) have a portion of their output pumped to boiling conduits (71a-f) through the regenerator (49), which conduits are connected to and at the same pressure as the highest pressure stage (48a) of the 1R multistage boiler (48).

Dao, Kim (14 Nace Ave., Piedmont, CA 94611)

1990-01-01T23:59:59.000Z

449

Life Cycle Assessment for Sustainable Metropolitan Water Systems Planning  

Science Journals Connector (OSTI)

Life Cycle Assessment (LCA) is useful as an information tool for the examination of alternative future scenarios for strategic planning. ... Water systems supply additional functions includ ing the following:? (1) nutrient recovery ? the treatment and land application of biosolids brings back the nutrients to the natural cycle in agriculture, horticulture, and forest systems, which can prevent the need for chemical fertilizers and thus avoid their production; (2) energy recovery ? which can include the generation of electricity or the cogeneration of thermal energy and electricity from biogas at sewage treat ment plants (STPs) or biosolids combustion off-site [This generation activity replaces the production of electrical and thermal energy from other energy sources.]; ...

Sven Lundie; Gregory M. Peters; Paul C. Beavis

2004-05-21T23:59:59.000Z

450

Carbon Cycle 2.0  

Broader source: Energy.gov (indexed) [DOE]

Carbon Cycle 2.0 Carbon Cycle 2.0 Pioneering science for sustainable energy solutions Artificial Photosynthesis Energy Storage Combustion Carbon Capture & Storage Developing World Efficiency Photovoltaics Biofuels Energy Analysis Climate Modeling Carbon Cycle 2.0 is... 1. A vision for * a global energy system integrated with the Earth's natural carbon cycles * an interactive Berkeley Lab environment with a shared sense of purpose 2. A program development plan that will allow us to deepen our capabilities and provide more opportunities to have impact 3. An attempt to integrate our basic research with applications using models of technology deployment constraints 4. Set of internal activities aimed at priming the effort

451

Building Life Cycle Cost Programs  

Broader source: Energy.gov [DOE]

The National Institute of Standards and Technology (NIST) developed the Building Life Cycle Cost (BLCC) Program to provide computational support for the analysis of capital investments in buildings.

452

Minimize Boiler Short Cycling Losses  

Broader source: Energy.gov [DOE]

This tip sheet on minimizing boiler short cycling losses provides how-to advice for improving industrial steam systems using low-cost, proven practices and technologies.

453

Virtuous Cycle Cycles of activity and software projects  

E-Print Network [OSTI]

Inspection #12;Programming Cycle - single bug Selected Bug Shared Code Fix Bug Continuous Integration ~8 cycle cvscheck compilation style checking testing javadocs documentation jumble quality of unit testing #12;NetValue Development cvscheck - Source Code Control and Build Shared Centralized Automatic

Pfahringer, Bernhard

454

Analysis of Inlet Air Cooling for IGCC Power Augmentation  

Science Journals Connector (OSTI)

Abstract Integrated Gasification Combined Cycles are energy systems mainly composed of a gasifier and a combined cycle power plant. Since the gasification process usually requires oxygen as an oxidant, an air separation unit is also part of the plant. Moreover, a producer gas cleaner unit is always present between the gasifier and the gas turbine. With respect to Natural Gas Combined Cycles, \\{IGCCs\\} are characterized by a consistent loss in the overall plant efficiency due to the conversion of the raw fuel in the gasifier and the electrical power parasitized for fuel production which considerably reduce the plant net electric power. Moreover, since these plants are based on gas-steam combined cycle power plants they suffer from a reduction in performance (a further net power decrease) when ambient temperature increases. Regarding this latter topic, different systems are currently used in gas turbine and combined cycle power plants in order to reduce gas turbine inlet air temperature, and, therefore, the impact of ambient conditions on performances. In this paper, a review of these systems is presented. Both systems based on water evaporative cooling and on refrigeration by means of absorption or mechanical/electrical chillers are described. Thermodynamic models of the systems are built within the framework of a commercial code for the simulation of energy conversion systems. A sensitivity analysis on the main parameters is presented. Finally, the models are applied to study the capabilities of the different systems by imposing the real temperature profiles of different sites for a whole year.

Andrea De Pascale; Francesco Melino; Mirko Morini

2014-01-01T23:59:59.000Z

455

Geothermal Water Use: Life Cycle Water Consumption, Water Resource Assessment, and Water Policy Framework  

SciTech Connect (OSTI)

This report examines life cycle water consumption for various geothermal technologies to better understand factors that affect water consumption across the life cycle (e.g., power plant cooling, belowground fluid losses) and to assess the potential water challenges that future geothermal power generation projects may face. Previous reports in this series quantified the life cycle freshwater requirements of geothermal power-generating systems, explored operational and environmental concerns related to the geochemical composition of geothermal fluids, and assessed future water demand by geothermal power plants according to growth projections for the industry. This report seeks to extend those analyses by including EGS flash, both as part of the life cycle analysis and water resource assessment. A regional water resource assessment based upon the life cycle results is also presented. Finally, the legal framework of water with respect to geothermal resources in the states with active geothermal development is also analyzed.

Schroeder, Jenna N.

2014-06-10T23:59:59.000Z

456

Thermal Analysis of the Z-Pinch Power Plant Concept  

SciTech Connect (OSTI)

In this work, a preliminary thermal model for the Z-Pinch Power Plant is presented. This power plant utilizes fusion energy to generate electric energy in the GW range. The Z-Pinch Technology consists of compressing high-density plasma to produce X-rays to indirectly heat to ignition a deuterium/tritium fusion capsule. This ignition releases a minimum of 3 GJ every 10 seconds. The thermal energy generated is absorbed by the primary cycle fluid, and it is later used to power a Brayton or Rankine cycle. An advanced heat exchanger is used as the interface between the two cycles. This heat exchanger plays an important role in power plant performance. Three fluids (Flibe, Pb-17Li, and Li) were used for the plant performance analysis. The thermodynamic properties of the selected fluids determine the maximum operating temperature of the power cycles. Model results show that high temperatures (over 1000 deg. C) are developed in the primary cycle as needed to efficiently run the secondary cycle. The results of the performance parametric study demonstrated that the Brayton cycle exhibits better performance characteristics than the Rankine cycle for this type of application.

Modesto, M.A.; Lindgren, E.R.; Morrow, C.W. [Sandia National Laboratories (United States)

2005-04-15T23:59:59.000Z

457

Life-cycle analysis results of geothermal systems in comparison to other power systems.  

SciTech Connect (OSTI)

A life-cycle energy and greenhouse gas emissions analysis has been conducted with Argonne National Laboratory's expanded Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation (GREET) model for geothermal power-generating technologies, including enhanced geothermal, hydrothermal flash, and hydrothermal binary technologies. As a basis of comparison, a similar analysis has been conducted for other power-generating systems, including coal, natural gas combined cycle, nuclear, hydroelectric, wind, photovoltaic, and biomass by expanding the GREET model to include power plant construction for these latter systems with literature data. In this way, the GREET model has been expanded to include plant construction, as well as the usual fuel production and consumption stages of power plant life cycles. For the plant construction phase, on a per-megawatt (MW) output basis, conventional power plants in general are found to require less steel and concrete than renewable power systems. With the exception of the concrete requirements for gravity dam hydroelectric, enhanced geothermal and hydrothermal binary used more of these materials per MW than other renewable power-generation systems. Energy and greenhouse gas (GHG) ratios for the infrastructure and other life-cycle stages have also been developed in this study per kilowatt-hour (kWh) of electricity output by taking into account both plant capacity and plant lifetime. Generally, energy burdens per energy output associated with plant infrastructure are higher for renewable systems than conventional ones. GHG emissions per kWh of electricity output for plant construction follow a similar trend. Although some of the renewable systems have GHG emissions during plant operation, they are much smaller than those emitted by fossil fuel thermoelectric systems. Binary geothermal systems have virtually insignificant GHG emissions compared to fossil systems. Taking into account plant construction and operation, the GREET model shows that fossil thermal plants have fossil energy use and GHG emissions per kWh of electricity output about one order of magnitude higher than renewable power systems, including geothermal power.

Sullivan, J. L.; Clark, C. E.; Han, J.; Wang, M.; Energy Systems

2010-10-11T23:59:59.000Z

458

Tap cogen-plant steam for process, NO[sub x] control  

SciTech Connect (OSTI)

This article describes the Monsanto's Indian Orchard plant gas-fired, combined-cycle cogeneration facility in Springfield, Massachusetts. The topics of the article include project configuration, the thermodynamic cycle, fuel selection, electrical distribution system, plant control, and air pollution control of NO[sub X], SO[sub 2], CO, particulates, non-methane hydrocarbons, opacity and ammonia.

Engel, W.J.; Haviland, R.W.; Devine, D.A.

1993-04-01T23:59:59.000Z

459

HIGH EFFICIENCY FOSSIL POWER PLANT (HEFPP) CONCEPTUALIZATION PROGRAM  

SciTech Connect (OSTI)

This study confirms the feasibility of a natural gas fueled, 20 MW M-C Power integrated pressurized molten carbonate fuel cell combined in a topping cycle with a gas turbine generator plant. The high efficiency fossil power plant (HEFPP) concept has a 70% efficiency on a LHV basis. The study confirms the HEFPP has a cost advantage on a cost of electricity basis over the gas turbine based combined cycle plants in the 20 MW size range. The study also identifies the areas of further development required for the fuel cell, gas turbine generator, cathode blower, inverter, and power module vessel. The HEFPP concept offers an environmentally friendly power plant with minuscule emission levels when compared with the combined cycle power plant.

J.L. Justice

1999-03-25T23:59:59.000Z

460

Appendix B: CArBon dioxide CApture teChnology SheetS  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

sorbents sorbents B-14 Pre-Combustion sorbents u.s. DePartment of energy aDvanCeD Carbon DioxiDe CaPture r&D Program: teChnology uPDate, may 2013 aDvanCeD Carbon DioxiDe CaPture teChnology for low-rank Coal integrateD gasifiCation CombineD CyCle (igCC) systems primary project goals TDA will investigate the technical and economic advantages of using an integrated carbon dioxide (CO 2 ) sorbent and water-gas shift (WGS) catalyst system in an integrated gasifi- cation combined cycle (IGCC) power plant, fueled with low-rank coal, and designed to capture more than 90% of the CO 2 emissions. technical goals * TDA will evaluate the physical mix of the sorbent and catalyst pellets within the same

Note: This page contains sample records for the topic "gasification-combined cycle plant" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


461

Benefits and concerns of a closed nuclear fuel cycle  

SciTech Connect (OSTI)

Nuclear power can play an important role in our energy future, contributing to increasing electricity demand while at the same time decreasing carbon dioxide emissions. However, the nuclear fuel cycle in the United States today is unsustainable. As stated in the 1982 Nuclear Waste Policy Act, the U.S. Department of Energy is responsible for disposing of spent nuclear fuel generated by commercial nuclear power plants operating in a “once-through” fuel cycle in the deep geologic repository located at Yucca Mountain. However, unyielding political opposition to the site has hindered the commissioning process to the extant that the current administration has recently declared the unsuitability of the Yucca Mountain site. In light of this the DOE is exploring other options, including closing the fuel cycle through recycling and reprocessing of spent nuclear fuel. The possibility of closing the fuel cycle is receiving special attention because of its ability to minimize the final high level waste (HLW) package as well as recover additional energy value from the original fuel. The technology is, however, still very controversial because of the increased cost and proliferation risk it can present. To lend perspective on the closed fuel cycle alternative, this presents the arguments for and against closing the fuel cycle with respect to sustainability, proliferation risk, commercial viability, waste management, and energy security.

Widder, Sarah H.

2010-11-17T23:59:59.000Z

462

Exergetic optimization of a refrigeration cycle for natural gas liquefaction  

Science Journals Connector (OSTI)

Abstract Natural gas is widely use in many industries as fuel and also as raw material. Although gas pipelines present less transportation losses they become impracticable when distances are too long or when demands are highly variable. The liquefaction of natural gas is then necessary to allow its transportation in great volumes, with little loss of material. This also enables its storage in a more stable way. Natural gas consumption is continuously growing worldwide and consequently, the number of exporter terminals (liquefaction industries) and importer terminals (regasification plants) will increase. The natural gas liquefaction process is based on a sequence of refrigeration cycles, which need to work in an optimized way. The exergetic analysis is a very useful thermodynamic tool to evaluate the efficiency of these cycles. This work aims at an exergetic analysis of a multistage cascade refrigeration cycle applied to a natural gas liquefaction process. Firstly, the process was simulated using commercial software and the results obtained from the simulations were validated with literature data, showing a good agreement. After that, different operational conditions, according to a complete factorial design of experiments, were studied, in order to verify the influence of pressure in six specific points of the cycle. The response variable analyzed is the rate of total exergy destroyed in the cycle. The results showed a new set of operational condition to the refrigeration cycle in which the destroyed exergy rate was reduced by approximately 48% in comparison with literature data.

Liza Cipolato; Maria C.A. Lirani; Thiago V. Costa; Francine M. Fábrega; José V.H. d'Angelo

2012-01-01T23:59:59.000Z

463

Life Cycle Asset Management  

Broader source: Directives, Delegations, and Requirements [Office of Management (MA)]

(The following directives are deleted or consolidated into this Order and shall be phased out as noted in Paragraph 2: DOE 1332.1A; DOE 4010.1A; DOE 4300.1C; DOE 4320.1B; DOE 4320.2A; DOE 4330.4B; DOE 4330.5; DOE 4540.1C; DOE 4700.1). This Order supersedes specific project management provisions within DOE O 430.1A, LIFE CYCLE ASSET MANAGEMENT. The specific paragraphs canceled by this Order are 6e(7); 7a(3); 7b(11) and (14); 7c(4),(6),(7),(11), and (16); 7d(4) and (8); 7e(3),(10), and (17); Attachment 1, Definitions (item 30 - Line Item Project, item 42 - Project, item 48 - Strategic System); and Attachment 2, Contractor Requirements Document (paragraph 1d regarding a project management system). The remainder of DOE O 430.1A remains in effect. Cancels DOE O 430.1. Canceled by DOE O 413.3.

1998-10-14T23:59:59.000Z

464

Nuclear fuel cycle information workshop  

SciTech Connect (OSTI)

This overview of the nuclear fuel cycle is divided into three parts. First, is a brief discussion of the basic principles of how nuclear reactors work; second, is a look at the major types of nuclear reactors being used and world-wide nuclear capacity; and third, is an overview of the nuclear fuel cycle and the present industrial capability in the US.

Not Available

1983-01-01T23:59:59.000Z

465

Working fluid for Rankine cycle  

SciTech Connect (OSTI)

A Rankine cycle working fluid is disclosed containing a mixture of 2,2,3,3tetrafluoropropanol and water, which is low toxic, incombustible, nonexplosive, noncorrosive and stable, and also has a high critical temperature and forms azeotropic-like composition. It is suited for use in a rankine cycle using heat source of low temperature.

Aomi, H.; Enjo, N.

1980-11-11T23:59:59.000Z

466

Extreme Financial cycles$ B. Candelonb,  

E-Print Network [OSTI]

Extreme Financial cycles$ B. Candelonb, , G. Gauliera , C. Hurlinb aUniversity Maastricht proposes a new approach to date extreme financial cycles. Elabo- rating on recent methods in extreme value theory, it elaborates an extension of the famous calculus rule to detect extreme peaks and troughs

Paris-Sud XI, Université de

467

NETL: Gasification - Development of Ion-Transport Membrane Oxygen  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Feed Systems Feed Systems Recovery Act: Development of Ion-Transport Membrane Oxygen Technology for Integration in IGCC and Other Advanced Power Generation Systems Air Products and Chemicals, Inc. Project Number: FC26-98FT40343 Project Description Air Products and Chemicals, Inc. is developing, scaling-up, and demonstrating a novel air separation technology for large-scale production of oxygen (O2) at costs that are approximately one-third lower than conventional cryogenic plants. An Ion Transport Membrane (ITM) Oxygen plant co-produces power and oxygen. A phased technology RD&D effort is underway to demonstrate all necessary technical and economic requirements for scale-up and industrial commercialization. The ITM Oxygen production technology is a radically different approach to producing high-quality tonnage oxygen and to enhance the performance of integrated gasification combined cycle and other advanced power generation systems. Instead of cooling air to cryogenic temperatures, oxygen is extracted from air at temperatures synergistic with power production operations. Process engineering and economic evaluations of integrated gasification combined cycle (IGCC) power plants comparing ITM Oxygen with a state-of-the-art cryogenic air separation unit are aimed to show that the installed capital cost of the air separation unit and the installed capital of IGCC facility are significantly lower compared to conventional technologies, while improving power plant output and efficiency. The use of low-cost oxygen in combustion processes would provide cost-effective emission reduction and carbon management opportunities. ITM Oxygen is an enabling module for future plants for producing coal derived shifted synthesis gas (a mixture of hydrogen [H2] and carbon dioxide [CO2]) ultimately for producing clean energy and fuels. Oxygen-intensive industries such as steel, glass, non-ferrous metallurgy, refineries, and pulp and paper may also realize cost and productivity benefits as a result of employing ITM Oxygen.

468

Why sequence Dothideomycetes plant pathogens?  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Dothideomycetes plant pathogens? Dothideomycetes plant pathogens? The largest and most diverse group of fungi, Dothideomycetes are found on every continent and play key roles in maintaining the local ecosystems by degrading biomass and contributing to regulating the carbon cycle. Many of these fungi are also tolerant of environmental extremes such as heat, humidity and cold. Among the members of this group are pathogens that infect nearly every major crop used for food, fiber or fuel. As crop rotations are being reduced, fewer crops are being grown on larger acreages, making them more susceptible to severe crop losses due to disease. Understanding the plant pathogens of these crops could reduce fertilizer use, which could in turn help reduce greenhouse gas emissions. To better understand the members of this group, the project calls for

469

CMVRTC: Heavy Truck Duty Cycle  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

heavy truck duty cycle (HTDC) project heavy truck duty cycle (HTDC) project OVERVIEW The Heavy Truck Duty Cycle (HTDC) Project was initiated in 2004 and is sponsored by the US Department of Energy's (DOE's) Office of FreedomCar and Vehicle Technologies Program. ORNL designed the research program to generate real-world-based duty cycle data from trucks operating in long-haul operations and was designed to be conducted in three phases: identification of parameters to be collected, instrumentation and pilot testing, identification of a real-world fleet, design of the data collection suite and fleet instrumentation, and data collection, analysis, and development of a duty cycle generation tool (DCGT). ANL logo dana logo michelin logo Schrader logo This type of data will be useful for supporting energy efficiency

470

Fuel cycle cost uncertainty from nuclear fuel cycle comparison  

SciTech Connect (OSTI)

This paper examined the uncertainty in fuel cycle cost (FCC) calculation by considering both model and parameter uncertainty. Four different fuel cycle options were compared in the analysis including the once-through cycle (OT), the DUPIC cycle, the MOX cycle and a closed fuel cycle with fast reactors (FR). The model uncertainty was addressed by using three different FCC modeling approaches with and without the time value of money consideration. The relative ratios of FCC in comparison to OT did not change much by using different modeling approaches. This observation was consistent with the results of the sensitivity study for the discount rate. Two different sets of data with uncertainty range of unit costs were used to address the parameter uncertainty of the FCC calculation. The sensitivity study showed that the dominating contributor to the total variance of FCC is the uranium price. In general, the FCC of OT was found to be the lowest followed by FR, MOX, and DUPIC. But depending on the uranium price, the FR cycle was found to have lower FCC over OT. The reprocessing cost was also found to have a major impact on FCC.

Li, J.; McNelis, D. [Institute for the Environment, University of North Carolina, Chapel Hill (United States); Yim, M.S. [Department of Nuclear and Quantum Engineering, Korea Advanced Institute of Science and Technology (Korea, Republic of)

2013-07-01T23:59:59.000Z

471

Medicinal Plants  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Medicinal Plants Medicinal Plants Nature Bulletin No. 187 April 11, 1981 Forest Preserve District of Cook County George W. Dunne, President Roland F. Eisenbeis, Supt. of Conservation MEDICINAL PLANTS In springtime, many years ago, grandma made her family drink gallons of tea made by boiling roots of the sassafras. That was supposed to thin and purify the blood. Children were sent out to gather dandelion, curly dock, wild mustard, pokeberry and other greens as soon as they appeared -- not only because they added welcome variety to the diet of bread, meat, potatoes and gravy, but because some of them were also laxatives. For a bad "cold on the lungs," she slapped a mustard plaster on the patient's back, and on his chest she put a square of red flannel soaked in goose grease. For whooping cough she used a syrup of red clover blossoms. She made cough medicine from the bloodroot plant, and a tea from the compass plant of the prairies was also used for fevers and coughs. She made a pleasant tea from the blossoms of the linden or basswood tree. For stomach aches she used tea from any of several aromatic herbs such as catnip, fennel, yarrow, peppermint, spearmint, sweetflag, wild ginger, bergamot and splice bush.

472

Bog Plants  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Bog Plants Bog Plants Nature Bulletin No. 385-A June 6, 1970 Forest Preserve District of Cook County George W. Dunne, President Roland F. Eisenbeis, Supt. of Conservation BOG PLANTS Fifty years ago there were probably more different kinds of plants within a 50 mile radius from the Loop than anywhere else in the Temperate Zone. Industrial, commercial and residential developments, plus drainage and fires have erased the habitats where many of the more uncommon kinds flourished, including almost all of the tamarack swamps and quaking bogs. These bogs were a heritage from the last glacier. Its front had advanced in a great curve, from 10 to 20 miles beyond what is now the shoreline of Lake Michigan, before the climate changed and it began to melt back. Apparently the retreat was so rapid that huge blocks of ice were left behind, surrounded by the outwash of boulders, gravel and ground-up rock called "drift". These undrained depressions; became lakes. Sphagnum moss invaded many of them and eventually the thick floating mats of it supported a variety of bog-loving plants including certain shrubs, tamarack, and a small species of birch. Such lakes became bogs.

473

Energy Conversion Advanced Heat Transport Loop and Power Cycle  

SciTech Connect (OSTI)

The Department of Energy and the Idaho National Laboratory are developing a Next Generation Nuclear Plant (NGNP) to serve as a demonstration of state-of-the-art nuclear technology. The purpose of the demonstration is two fold 1) efficient low cost energy generation and 2) hydrogen production. Although a next generation plant could be developed as a single-purpose facility, early designs are expected to be dual-purpose. While hydrogen production and advanced energy cycles are still in its early stages of development, research towards coupling a high temperature reactor, electrical generation and hydrogen production is under way. Many aspects of the NGNP must be researched and developed in order to make recommendations on the final design of the plant. Parameters such as working conditions, cycle components, working fluids, and power conversion unit configurations must be understood. Three configurations of the power conversion unit were demonstrated in this study. A three-shaft design with 3 turbines and 4 compressors, a combined cycle with a Brayton top cycle and a Rankine bottoming cycle, and a reheated cycle with 3 stages of reheat were investigated. An intermediate heat transport loop for transporting process heat to a High Temperature Steam Electrolysis (HTSE) hydrogen production plant was used. Helium, CO2, and an 80% nitrogen, 20% helium mixture (by weight) were studied to determine the best working fluid in terms cycle efficiency and development cost. In each of these configurations the relative component size were estimated for the different working fluids. The relative size of the turbomachinery was measured by comparing the power input/output of the component. For heat exchangers the volume was computed and compared. Parametric studies away from the baseline values of the three-shaft and combined cycles were performed to determine the effect of varying conditions in the cycle. This gives some insight into the sensitivity of these cycles to various operating conditions as well as trade offs between efficiency and capital cost. Prametric studies were carried out on reactor outlet temperature, mass flow, pressure, and turbine cooling. Recommendations on the optimal working fluid for each configuration were made. A steady state model comparison was made with a Closed Brayton Cycle (CBC) power conversion system developed at Sandia National Laboratory (SNL). A preliminary model of the CBC was developed in HYSYS for comparison. Temperature and pressure ratio curves for the Capstone turbine and compressor developed at SNL were implemented into the HYSYS model. A comparison between the HYSYS model and SNL loop demonstrated power output predicted by HYSYS was much larger than that in the experiment. This was due to a lack of a model for the electrical alternator which was used to measure the power from the SNL loop. Further comparisons of the HYSYS model and the CBC data are recommended. Engineering analyses were performed for several configurations of the intermediate heat transport loop that transfers heat from the nuclear reactor to the hydrogen production plant. The analyses evaluated parallel and concentric piping arrangements and two different working fluids, including helium and a liquid salt. The thermal-hydraulic analyses determined the size and insulation requirements for the hot and cold leg pipes in the different configurations. Economic analyses were performed to estimate the cost of the va

Oh, C. H.

2006-08-01T23:59:59.000Z

474

Microsoft Word - 41889_GE_IGCC System Study_Factsheet_Rev01_07-20-04.doc  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Fact Sheet: Fact Sheet: "System Study For Improved Gas Turbine Performance For Coal IGCC Application" DOE Contract No: DE-FC26-03NT41889 I Project Description: A. Objective: This study will identify improvements in gas turbine performance for coal Integrated Gasification Combined Cycle (IGCC) application. The study will identify vital gas turbine parameters and quantify their influence in meeting the DOE Turbine Program overall IGCC plant goals of 50% net HHV efficiency, $1000/kW capital cost, and low emissions. Focus will be on air-cooled gas turbines for near-term operation in coal fed oxygen blown IGCC power plants with commercially demonstrated gasification, gas cleaning, & air separation technologies. A roadmap towards achieving DOE's goals for

475

Categorical Exclusion Determinations: Tennessee | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

April 29, 2010 April 29, 2010 CX-002142: Categorical Exclusion Determination Cogeneration at M.C. Stiles Wastewater Treatment Plant CX(s) Applied: B5.1 Date: 04/29/2010 Location(s): Memphis, Tennessee Office(s): Energy Efficiency and Renewable Energy, Golden Field Office April 23, 2010 CX-001907: Categorical Exclusion Determination Knox County Tennessee American Recovery and Reinvestment Act - Energy Efficiency and Conservation Block Grant (S) CX(s) Applied: A9, A11, B5.1 Date: 04/23/2010 Location(s): Knox County, Tennessee Office(s): Energy Efficiency and Renewable Energy, Golden Field Office April 23, 2010 CX-001641: Categorical Exclusion Determination Scale-Up of Hydrogen Transport Membranes (HTM) for Integrated Gasification Combined Cycle (IGCC) and FutureGen Coal-to-Hydrogen Plants (Kingsport)

476

Secretary Chu Announces $14 Million for Six New Projects to Advance IGCC  

Broader source: Energy.gov (indexed) [DOE]

4 Million for Six New Projects to Advance 4 Million for Six New Projects to Advance IGCC Technology Secretary Chu Announces $14 Million for Six New Projects to Advance IGCC Technology September 9, 2011 - 6:16pm Addthis Washington, D.C. -U.S. Department of Energy Secretary Steven Chu announced today the selection of six projects aimed at developing technologies to lower the cost of producing electricity in integrated gasification combined cycle (IGCC) power plants using carbon capture, while maintaining the highest environmental standards. Supported with up to $14 million in total funding, the selected projects will improve the economics of IGCC plants and promote the use of the Nation's abundant coal resources to produce clean, secure, and affordable energy. The successful development of advanced technologies and innovative concepts

477

winter_96  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

ELECTRIC'S GREENFIELD ELECTRIC'S GREENFIELD IGCC READY FOR DEMONSTRATION Tampa Electric Company (TEC) has reached a major milestone in its goal to bring clean, low-cost energy to the consumer well into the 21st century. Begun with an independent community plant siting effort, TEC in October initiated operation of a 250-MWe (net) Integrated Gasification Combined- Cycle (IGCC) system. This is the first increment of a planned build-out to 1,150 MWe at the new Polk Power Plant in Polk County, Florida. The advanced IGCC system offers high efficiency, extremely low emis- sions, and saleable solids and liquids in lieu of wastes. In addition to using an environmentally advanced power generation technology, the project will convert some 1,500 acres of phosphate mining spoils to useable

478

NETL: Gasification- Water-Gas Shift (WGS) Tests to Reduce Steam Use  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Syngas Processing Systems Syngas Processing Systems Water-Gas Shift (WGS) Tests to Reduce Steam Use National Carbon Capture Center at the Power Systems Development Facility Southern Company Services, Inc. Project Number: NT0000749 Project Description The National Carbon Capture Center is testing commercial water-gas shift (WGS) catalysts from multiple vendors in support of developing WGS reactor systems which will reduce the cost of carbon dioxide (CO2) capture from the production of syngas using coal. These tests have revealed that steam-to-carbon monoxide (CO) ratios can be reduced, resulting in a substantial increase in the net power output and significantly reducing the cost of electricity from an integrated gasification combined cycle (IGCC) plant with CO2 capture. Several commercially available WGS catalysts have been tested, and the results are being provided to the manufacturers to aid them in specifying future WGS systems for IGCC plants incorporating CO2 capture.

479

NETL: News Release - New Oxygen-Production Technology Proving Successful  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

22, 2009 22, 2009 New Oxygen-Production Technology Proving Successful Ceramic Membrane Enables Efficient, Cost-Effective Co-Production of Power and Oxygen Washington, D.C. -The Office of Fossil Energy's National Energy Technology Laboratory (NETL) has partnered with Air Products and Chemicals Inc. of Allentown, Penn. to develop the Ion Transport Membrane (ITM) Oxygen, a revolutionary new oxygen-production technology that requires less energy and offers lower capital costs than conventional technologies. ITM Oxygen will enhance the performance of integrated gasification combined cycle (IGCC) power plants, as well as other gasification-based processes. The technology will also enhance the economics of oxy-fired combustion technologies, making it an attractive option for the capture of carbon dioxide from existing coal-fired power plants.

480

FE Clean Coal News | Department of Energy  

Broader source: Energy.gov (indexed) [DOE]

August 22, 2011 August 22, 2011 DOE Launches World-Class Virtual Energy Simulation Training and Research Center A new training center developed to teach personnel how to operate clean integrated gasification combined cycle power plants is now up and running with help from the U.S. Department of Energy. August 16, 2011 DOE Research Grant Leads to Gas Turbine Manufacturing Improvements Research sponsored by the U.S. Department of Energy's Office of Fossil Energy has led to a new licensing agreement that will improve the performance of state-of-the-art gas turbines, resulting in cleaner, more reliable and affordable energy. August 15, 2011 Projects Aimed at Advancing State-of-the-Art Carbon Capture from Coal Power Plants Selected for Further Development Four projects aimed at reducing the energy and cost penalties of advanced

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481

Albany, OR * Anchorage, AK * Morgantown, WV * Pittsburgh, PA * Sugar Land, TX  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Low-Swirl Injectors for Hydrogen Gas Low-Swirl Injectors for Hydrogen Gas Turbines in Near-Zero Emissions Coal Power Plants-Lawrence Berkeley National Laboratory Background The U.S. Department of Energy Hy(DOE) Lawrence Berkeley National Laboratory (LBNL) is leading a project in partnership with gas turbine manufacturers and universities to develop a robust ultra-low emission combustor for gas turbines that burn high hydrogen content (HHC) fuels derived from gasification of coal. A high efficiency and ultra-low emissions HHC fueled gas turbine is a key component of a near-zero emis- sions integrated gasification combined cycle (IGCC) clean coal power plant. This project is managed by the DOE National Energy Technology Laboratory (NETL). NETL is researching advanced turbine technology with the goal of producing reliable,

482

New Computer Codes Unlock the Secrets of Cleaner Burning Coal  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Codes Codes Unlock the Secrets of Cleaner Burning Coal New Computer Codes Unlock the Secrets of Cleaner Burning Coal March 29, 2012 | Tags: Advanced Scientific Computing Research (ASCR), Combustion, Franklin, Hopper Linda Vu, lvu@lbl.gov, +1 510 495 2402 The Polk Power Station near Mulberry, Florida, is an Integrated