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1

The desulfurization of flue gas at the Mae Moh Power Plant Units 12 and 13  

SciTech Connect

As pollution of air, water and ground increasingly raises worldwide concern, the responsible national and international authorities establish and issue stringent regulations in order to maintain an acceptable air quality in the environment. In Thailand, the Electricity Generating Authority of Thailand (EGAT) takes full responsibility in environmental protection matters as well as in generating the electricity needed to supply the country`s very rapid power demand growth. Due to the rapidly increasing electricity demand of the country, EGAT had decided to install two further lignite-fired units of 300 MW each (Units 12 and 13) at the Mae Moh power generation station and they are now under construction. The arrangement and the capacity of all the power plant units are as shown. In 1989, EGAT started the work on the flue gas desulfurization system of Mae Moh power plant units 12 and 13 as planned. A study has been conducted to select the most suitable and most economical process for flue gas desulfurization. The wet scrubbing limestone process was finally selected for the two new units. Local limestone will be utilized in the process, producing a by-product of gypsum. Unfortunately, natural gypsum is found in abundance in Thailand, so the produced gypsum will be treated as landfill by mixing it with ash from the boilers of the power plants and then carrying it to the ash dumping area. The water from the waste ash water lake is utilized in the process as much as possible to minimize the requirement of service water, which is a limited resource. The Mae Moh power generation station is situated in the northern region of Thailand, 600 km north of Bangkok and about 30 km east of the town of Lampang, close to the Mae Moh lignite mine. Three lignite-fired units (Units 1-3) of 75 MW each, four units (Units 4-7) of 150 MW each and four units (Units 8-11) of 300 MW each are in operation.

Haemapun, C.

1993-12-31T23:59:59.000Z

2

Analysis of a pilot-scale constructed wetland treatment system for flue gas desulfurization wastewater.  

E-Print Network (OSTI)

??Coal-fired generation accounts for 45% of the United States electricity and generates harmful emissions, such as sulfur dioxide. With the implementation of Flue Gas Desulfurization… (more)

Talley, Mary Katherine

2012-01-01T23:59:59.000Z

3

Re-lining of scrubbers in flue gas desulfurization plants  

SciTech Connect

Rubber lining is used as corrosion protection material in scrubbers, tanks, pipe systems etc of European flue gas desulfurization plants. Although these rubber linings show in cases more than 15 years life, re-rubber lining is still necessary. Due to the expected higher availability of the power station units the time scale of such replacement must be kept to a minimum. As an efficient method for removal of the old lining the high pressure water systems has proven successful. Based on one such case of re-lining the working steps and time scale are demonstrated.

Fenner, J. [Keramchemie GmbH, Siershahn (Germany)

1999-11-01T23:59:59.000Z

4

Relining of scrubbers in flue gas desulfurization plants  

SciTech Connect

Rubber lining is used as a corrosion protection material in European flue gas desulfurization plants, for scrubbers, tanks, pipe systems, etc. Although these rubber linings can last more than 15 years, relining still is necessary. The difficulty of shutting down power station units requires that the time scale of this replacement be kept to a minimum. High-pressure water systems have proven successful as an efficient method for removal of the old lining. The working steps and time scale are demonstrated for one such relining case.

Fenner, J. [Keramchemie GmbH (Germany)

1999-09-01T23:59:59.000Z

5

Advanced Flue Gas Desulfurization (AFGD) Demonstration Project, A DOE Assessment  

NLE Websites -- All DOE Office Websites (Extended Search)

8 8 Advanced Flue Gas Desulfurization (AFGD) Demonstration Project A DOE Assessment August 2001 U.S. Department of Energy National Energy Technology Laboratory P.O. Box 880, 3610 Collins Ferry Road Morgantown, WV 26507-0880 and P.O. Box 10940, 626 Cochrans Mill Road Pittsburgh, PA 15236-0940 website: www.netl.doe.gov 2 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

6

Flue gas desulfurization: Physicochemical and biotechnological approaches  

SciTech Connect

Various flue gas desulfurization processes - physicochemical, biological, and chemobiological - for the reduction of emission of SO{sub 2} with recovery of an economic by-product have been reviewed. The physicochemical processes have been categorized as 'once-through' and 'regenerable.' The prominent once-through technologies include wet and dry scrubbing. The wet scrubbing technologies include wet limestone, lime-inhibited oxidation, limestone forced oxidation, and magnesium-enhanced lime and sodium scrubbing. The dry scrubbing constitutes lime spray drying, furnace sorbent injection, economizer sorbent injection, duct sorbent injection, HYPAS sorbent injection, and circulating fluidized bed treatment process. The regenerable wet and dry processes include the Wellman Lord's process, citrate process, sodium carbonate eutectic process, magnesium oxide process, amine process, aqueous ammonia process, Berglau Forchung's process, and Shell's process. Besides these, the recently developed technologies such as the COBRA process, the OSCAR process, and the emerging biotechnological and chemobiological processes are also discussed. A detailed outline of the chemistry, the advantages and disadvantages, and the future research and development needs for each of these commercially viable processes is also discussed.

Pandey, R.A.; Biswas, R.; Chakrabarti, T.; Devotta, S. [National Environmental Engineering Research Institute, Nagpur (India)

2005-07-01T23:59:59.000Z

7

Separation of Mercury from Flue Gas Desulfurization Scrubber Produced Gypsum  

SciTech Connect

Frontier Geosciences (Frontier; FGS) proposed for DOE Grant No. DE-FG02-07ER84669 that mercury control could be achieved in a wet scrubber by the addition of an amendment to the wet-FGD scrubber. To demonstrate this, a bench-scale scrubber and synthetic flue-gas supply was designed to simulate the limestone fed, wet-desulfurization units utilized by coal-fired power plants. Frontier maintains that the mercury released from these utilities can be controlled and reduced by modifying the existing equipment at installations where wet flue-gas desulfurization (FGD) systems are employed. A key element of the proposal was FGS-PWN, a liquid-based mercury chelating agent, which can be employed as the amendment for removal of all mercury species which enter the wet-FGD scrubber. However, the equipment design presented in the proposal was inadequate to demonstrate these functions and no significant progress was made to substantiate these claims. As a result, funding for a Phase II continuation of this work will not be pursued. The key to implementing the technology as described in the proposal and report appears to be a high liquid-to-gas ratio (L/G) between the flue-gas and the scrubber liquor, a requirement not currently implemented in existing wet-FGD designs. It may be that this constraint can be reduced through parametric studies, but that was not apparent in this work. Unfortunately, the bench-scale system constructed for this project did not function as intended and the funds and time requested were exhausted before the separation studies could occur.

Hensman, Carl, E., P.h.D; Baker, Trevor

2008-06-16T23:59:59.000Z

8

Workshop on sulfur chemistry in flue gas desulfurization  

SciTech Connect

The Flue Gas Desulfurization Workshop was held at Morgantown, West Virginia, June 7-8, 1979. The presentations dealt with the chemistry of sulfur and calcium compounds in scrubbers. DOE and EPRI programs in this area are described. Ten papers have been entered individually into EDB and ERA. (LTN)

Wallace, W.E. Jr.

1980-05-01T23:59:59.000Z

9

Rubber linings as surface protection in flue gas desulfurization plants  

SciTech Connect

The manufacturers of the German rubber lining industry have executed the rubber lining of over 1 million m{sup 2} of steel surfaces in over 150 scrubbers of flue gas desulfurization (FGD) plants, thereby effectively protecting them against corrosion. The application of rubber linings as surface protection in FGD plants has proven effective.

Fenner, J.

1997-04-01T23:59:59.000Z

10

ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS  

SciTech Connect

The U.S. Department of Energy and EPRI co-funded this project to improve the control of mercury emissions from coal-fired power plants equipped with wet flue gas desulfurization (FGD) systems. The project has investigated catalytic oxidation of vapor-phase elemental mercury to a form that is more effectively captured in wet FGD systems. If successfully developed, the process could be applicable to over 90,000 MW of utility generating capacity with existing FGD systems, and to future FGD installations. Field tests were conducted to determine whether candidate catalyst materials remain active towards mercury oxidation after extended flue gas exposure. Catalyst life will have a large impact on the cost effectiveness of this potential process. A mobile catalyst test unit was used to test the activity of four different catalyst materials for a period of up to six months each at three utility sites. Catalyst testing was completed at the first site, which fires Texas lignite, in December 1998; at the second test site, which fires a Powder River Basin subbituminous coal, in November 1999; and at the third site, which fires a medium- to high-sulfur bituminous coal, in January 2001. Results of testing at each of the three sites were reported in previous technical notes. At Site 1, catalysts were tested only as powders dispersed in sand bed reactors. At Sites 2 and 3, catalysts were tested in two forms, including powders dispersed in sand and in commercially available forms such as extruded pellets and coated honeycomb structures. This final report summarizes and presents results from all three sites, for the various catalyst forms tested. Field testing was supported by laboratory tests to screen catalysts for activity at specific flue gas compositions, to investigate catalyst deactivation mechanisms and methods for regenerating spent catalysts. Laboratory results are also summarized and discussed in this report.

Unknown

2001-06-01T23:59:59.000Z

11

Process for production desulfurized of synthesis gas  

DOE Patents (OSTI)

A process for the partial oxidation of a sulfur- and silicate-containing carbonaceous fuel to produce a synthesis gas with reduced sulfur content which comprises partially oxidizing said fuel at a temperature in the range of 1900.degree.-2600.degree. F. in the presence of a temperature moderator, an oxygen-containing gas and a sulfur capture additive which comprises a calcium-containing compound portion, a sodium-containing compound portion, and a fluoride-containing compound portion to produce a synthesis gas comprising H.sub.2 and CO with a reduced sulfur content and a molten slag which comprises (1) a sulfur-containing sodium-calcium-fluoride silicate phase; and (2) a sodium-calcium sulfide phase.

Wolfenbarger, James K. (Torrance, CA); Najjar, Mitri S. (Wappingers Falls, NY)

1993-01-01T23:59:59.000Z

12

Desulfurization of coke oven gas from the coking of coking coal blended with a sorbent and waste plastic  

Science Journals Connector (OSTI)

A new way to implement the simultaneous reutilization of solid waste, the desulfurization of coke oven gas (COG), and even the desulfurization of coke by the co-coking of coking coal (CC) and waste plastic (WP).....

Zhao Rongfang; Ye Shufeng; Xie Yusheng…

2007-03-01T23:59:59.000Z

13

Manganese-based sorbents for coal gas desulfurization  

SciTech Connect

The intent of this study is to perform a preliminary screening on a particular Mn-based sorbent, CST-939 (from Chemetals), for hot gas desulfurization. The purpose of the preliminary screening is to determine which temperature and type of coal gas this sorbent demonstrates the greatest capacity and efficiency for sulfur removal. The following conclusions were made from the data collected on the CST-939 sorbent: The sorbent efficiency and capacity are much greater at 343{degrees}C (650{degrees}F) than at 871{degrees}C (1,600{degrees}F). The sorbent efficiency and capacity are much greater in the presence of the more highly-reducing Shell gas than with the less-reducing KRW gas. The sorbent showed tremendous capacity for sulfur pickup, with actual loadings as high as 21 weight percent. Oxidative regeneration at 871{degrees}C (1,600{degrees}F) appeared to decompose sulfate; however, unusually high SO{sub 2} release during the second sulfidations and/or reductive regenerations indicated incomplete regeneration. The average crush strength of the reacted sorbent did not indicate any loss of strength as compared to the fresh sorbent. Superior sorbent performance was obtained in the presence of simulated Shell gas at 538{degrees}C (1,000{degrees}F).

Gasper-Galvin, L.D.; Fisher, E.P. [USDOE Morgantown Energy Technology Center, WV (United States); Goyette, W.J. [Chemetals, Inc., Baltimore, MD (United States)

1996-12-31T23:59:59.000Z

14

Flue gas desulfurization : cost and functional analysis of large-scale and proven plants  

E-Print Network (OSTI)

Flue Gas Desulfurization is a method of controlling the emission of sulfurs, which causes the acid rain. The following study is based on 26 utilities which burn coal, have a generating capacity of at least 50 Megawatts ...

Tilly, Jean

1983-01-01T23:59:59.000Z

15

KINETICS OF HOT-GAS DESULFURIZATION SORBENTS FOR TRANSPORT REACTORS  

SciTech Connect

Hot-gas desulfurization for the integrated gasification combined cycle (IGCC) process has been investigated by many researchers to remove effectively hydrogen sulfide with various metal oxide sorbents at elevated temperatures. Various metal oxide sorbents are formulated with metal oxides such as Fe, Co, Zn, and Ti. Initial reaction kinetics of formulated sorbents with hydrogen sulfide is studied in the presence of various amounts of moisture and hydrogen at various reaction temperatures. The objectives of this research are to study initial reaction kinetics for a sorbent-hydrogen sulfide heterogeneous reaction system, to investigate effects of concentrations of hydrogen sulfide, hydrogen, and moisture on dynamic absorption of H{sub 2}S into sorbents, and to evaluate effects of temperature and sorbent amounts on dynamic absorption of H{sub 2}S into sorbents. Experimental data on initial reaction kinetics of hydrogen sulfide with metal oxide sorbents were obtained with a 0.83-cm{sup 3} differential reactor. In this report, the reactivity of AHI-5 was examined. This sorbent was obtained from the Research Triangle Institute (RTI). The sorbent in the form of 70 {micro}m particles are reacted with 9000-18000 ppm hydrogen sulfide at 350-500 C. The range of space time of reaction gas mixtures is 0.071-0.088 s. The range of reaction duration is 4-10800 s.

K.C. Kwon

2001-01-01T23:59:59.000Z

16

Desulfurization of Digester Gas on Industrial-Sludge-Derived Adsorbents  

Science Journals Connector (OSTI)

The performance of adsorbents in the breakthrough tests is summarized in Tables 1 and 2, where besides the capacity expressed in milligrams per unit mass of an adsorbent or in milligrams per unit bed volume, the amount of water adsorbed during prehumidification, bed density, and pH before and after exposure to DG are listed. ... Probably the most important negative effect can be linked to the engagement of magnesium and calcium oxides in the carbonate entities, which, besides lowering surface pH and thus the number of HS- ions formed, limits the extent of reactions 2 and 7. Nevertheless, the performance of our adsorbents in desulfurization of DG is better than that of catalytically activated carbons, such as Midas or DarcoH2S, for which 73 and 39 mg/g of H2S adsorbed, respectively, was reported. ... result in adsorbents whose capacity, although smaller than that for the single-component waste oil sludge-based adsorbent, is high compared to that of conventional activated carbons. ...

Mykola Seredych; Teresa J. Bandosz

2007-01-12T23:59:59.000Z

17

PRODUCTION OF CONSTRUCTION AGGREGATES FROM FLUE GAS DESULFURIZATION SLUDGE  

SciTech Connect

Through a cooperative agreement with DOE, the Research and Development Department of CONSOL Inc. (CONSOL R and D) is teaming with SynAggs, Inc. and Duquesne Light to design, construct, and operate a 500 lb/h continuous pilot plant to produce road construction aggregate from a mixture of wet flue gas desulfurization (FGD) sludge, fly ash, and other components. The proposed project is divided into six tasks: (1) Project Management; (2) Mix Design Evaluation; (3) Process Design; (4) Construction; (5) Start-Up and Operation; and (6) Reporting. In this quarter, Tasks 1 and 2 were completed. A project management plan (Task 1) was issued to DOE on October 22, 1998 . The mix design evaluation (Task 2) with Duquesne Light Elrama Station FGD sludge and Allegheny Power Hatfields Ferry Station fly ash was completed. Eight semi-continuous bench-scale tests were conducted to examine the effects of mix formulation on aggregate properties. A suitable mix formulation was identified to produce aggregates that meet specifications of the American Association of State High Transport Officials (AASHTO) as Class A aggregate for use in highway construction. The mix formulation was used in designing the flow sheet of the pilot plant. The process design (Task 3) is approximately 80% completed. Equipment was evaluated to comply with design requirements. The design for the curing vessel was completed by an outside engineering firm. All major equipment items for the pilot plant, except the curing vessel, were ordered. Pilot plant construction (Task 4) was begun in October. The Hazardous Substance Plan was issued to DOE. The Allegheny County (PA) Heat Department determined that an air emission permit is not required for operation of the pilot plant.

NONE

1998-12-01T23:59:59.000Z

18

A Reusable Calcium-Based Sorbent for Desulfurizing Hot Coal Gas  

SciTech Connect

The overall objective of this project has been to develop a superior, regenerable, calcium-based sorbent for desulfurizing hot coal gas. The sorbent should be strong, durable, inexpensive to manufacture, and capable of being reused many times. To achieve these objectives the project has focused on the development of the very promising core-in-shell sorbent.

Wheelock, T.D.; Hasler, D.J.L.

2002-09-19T23:59:59.000Z

19

Integrated operation of a pressurized fixed bed gasifier and hot gas desulfurization system  

SciTech Connect

The primary objective of this contract continues to be the demonstration of high fuel gas desulfurization of high temperature fuel gas desulfurization and particulate removal using a moving bed process with regenerable metal oxide sorbent. The fuel gas source for test operation is a fixed bed, air blown gasifier located at GE Corporate Research and Development in Schenectady, New York. The demonstration project also includes the design, construction, installation and test operation of a gas turbine simulator which includes a modified GE MS6000 type gas turbine combustor and a film cooled, first stage LM 6000 nozzle assembly. The hot gas cleanup (HGCU) system and the gas turbine simulator have been designed to operate with the full 8000 lb/hr fuel gas flow from the gasification of 1800 lb/hr of coal at 280 psig and 1000 to 1150 F. An advanced formulation of zinc ferrite as well as zinc titanate have been used as the regenerable metal oxide sorbents in testing to date. Demonstration of halogen removal as well as characterization of alkali and heavy metal concentrations in the fuel gas remain objectives, as well. Results are discussed.

Cook, C.S.; Gal, E.; Furman, A.H.; Ayala, R.

1992-01-01T23:59:59.000Z

20

Integrated operation of a pressurized fixed bed gasifier and hot gas desulfurization system  

SciTech Connect

The primary objective of this contract continues to be the demonstration of high fuel gas desulfurization of high temperature fuel gas desulfurization and particulate removal using a moving bed process with regenerable metal oxide sorbent. The fuel gas source for test operation is a fixed bed, air blown gasifier located at GE Corporate Research and Development in Schenectady, New York. The demonstration project also includes the design, construction, installation and test operation of a gas turbine simulator which includes a modified GE MS6000 type gas turbine combustor and a film cooled, first stage LM 6000 nozzle assembly. The hot gas cleanup (HGCU) system and the gas turbine simulator have been designed to operate with the full 8000 lb/hr fuel gas flow from the gasification of 1800 lb/hr of coal at 280 psig and 1000 to 1150 F. An advanced formulation of zinc ferrite as well as zinc titanate have been used as the regenerable metal oxide sorbents in testing to date. Demonstration of halogen removal as well as characterization of alkali and heavy metal concentrations in the fuel gas remain objectives, as well. Results are discussed.

Cook, C.S.; Gal, E.; Furman, A.H.; Ayala, R.

1992-12-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Simultaneous removal of H2S and COS using Zn-based solid sorbents in the bench-scale continuous hot gas desulfurization system integrated with a coal gasifier  

Science Journals Connector (OSTI)

A bench-scale continuous hot gas desulfurization system using Zn-based solid sorbents was developed to remove H2S and COS simultaneously in a 110 Nm3.../h of real coal-gasified syngas. The bench-scale unit, which...

Young Cheol Park; Sung-Ho Jo; Ho-Jung Ryu…

2012-12-01T23:59:59.000Z

22

Flue gas desulfurization/denitrification using metal-chelate additives  

DOE Patents (OSTI)

A method of simultaneously removing SO/sub 2/ and NO from oxygen-containing flue gases resulting from the combustion of carbonaceous material by contacting the flue gas with an aqueous scrubber solution containing an aqueous sulfur dioxide sorbent and an active metal chelating agent which promotes a reaction between dissolved SO/sub 2/ and dissolved NO to form hydroxylamine N-sulfonates. The hydroxylamine sulfonates are then separated from the scrubber solution which is recycled. 3 figs.

Harkness, J.B.L.; Doctor, R.D.; Wingender, R.J.

1985-08-05T23:59:59.000Z

23

Hot coal gas desulfurization with manganese-based sorbents. Final report, September 1992--December 1994  

SciTech Connect

The focus of much current work being performed by the Morgantown Energy Technology Center (METC) of the Department of Energy on hot coal-derived fuel gas desulfurization is in the use of zinc-based sorbents. METC has shown interest in formulating and testing manganese-based pellets as alternative effective sulfur sorbents in the 700 to 1200{degree}C temperature range. To substantiate the potential superiority of Mn-based pellets, a systematic approach toward the evaluation of the desulfurizing power of single-metal sorbents is developed based on thermodynamic considerations. This novel procedure considered several metal-based sorbents and singled out manganese oxide as a prime candidate sorbent capable of being utilized under a wide temperature range, irrespective of the reducing power (determined by CO{sub 2}/CO ratio) of the fuel gas. Then, the thermodynamic feasibility of using Mn-based pellets for the removal of H{sub 2}S from hot-coal derived fuel gases, and the subsequent oxidative regeneration of loaded (sulfided) pellets was established. It was concluded that MnO is the stable form of manganese for virtually all commercially available coal-derived fuel gases. In addition, the objective of reducing the H{sub 2}S concentration below 150 ppMv to satisfy the integrated gasification combined cycle system requirement was shown to be thermodynamically feasible. A novel process is developed for the manufacture of Mn-based spherical pellets which have the desired physical and chemical characteristics required.

Hepworth, M.T.; Slimane, R.B.

1994-11-01T23:59:59.000Z

24

Potential Agricultural Uses of Flue Gas Desulfurization Gypsum in the Northern Great Plains  

SciTech Connect

Flue gas desulfurization gypsum (FGDG) is a byproduct from the combustion of coal for electrical energy production. Currently, FGDG is being produced by 15 electrical generating stations in Alabama, Florida, Indiana, Iowa, Kentucky, Ohio, North Carolina, South Carolina, Tennessee, Texas, and Wisconsin. Much of this byproduct is used in the manufacturing of wallboard. The National Network for Use of FGDG in Agriculture was initiated to explore alternative uses of this byproduct. In the northern Great Plains (North Dakota, South Dakota, and Montana), FGDG has the potential to be used as a Ca or S fertilizer, as an acid soil ameliorant, and for reclaiming or mitigating sodium-affected soils. Greater than 1.4 million Mg of FGDG could initially be used in these states for these purposes. Flue gas desulfurization gypsum can be an agriculturally important resource for helping to increase the usefulness of problem soils and to increase crop and rangeland production. Conducting beneficial use audits would increase the public awareness of this product and help identify to coal combustion electrical generating stations the agriculturally beneficial outlets for this byproduct.

DeSutter, T.M.; Cihacek, L.J. [North Dakota State University, Fargo, ND (United States). Department of Soil Science

2009-07-15T23:59:59.000Z

25

Bench-scale demonstration of hot-gas desulfurization technology. Quarterly report, October 1 - December 31, 1994  

SciTech Connect

The U.S. Department of Energy (DOE), Morgantown Energy Technology Center (METC), is sponsoring research in advanced methods for controlling contaminants in hot coal gasifier gas (coal gas) streams of integrated gasification combined-cycle (IGCC) power systems. The programs focus on hot-gas particulate removal and desulfurization technologies that match or nearly match the temperatures and pressures of the gasifier, cleanup system, and power generator. The work seeks to eliminate the need for expensive heat recovery equipment, reduce efficiency losses due to quenching, and minimize wastewater treatment costs. Hot-gas desulfurization research has focused on regenerable mixed-metal oxide sorbents which can reduce the sulfur in coal gas to less than 20 ppmv and can be regenerated in a cyclic manner with air for multicycle operation. Zinc titanate (Zn{sub 2}TiO{sub 4} or ZnTiO{sub 3}), formed by a solid-state reaction of zinc (ZnO) and titanium dioxide (TiO{sub 2}), is currently one of the leading sorbents. This report summarizes the highlights and accomplishments of the October slipstream test run of the Zinc Titanate Fluid Bed Desulfurization/Direct Sulfur Recovery Process (ZTFBD/DSRP) Mobile Laboratory at the Department of Energy`s Morgantown Energy Technology Center. Although the run had to be shortened due to mechanical problems with METC`s gasifier, there was sufficient on-stream time to demonstrate highly successful operation of both the zinc titanate fluid bed desulfurization and the DSRP with actual coal gas.

NONE

1994-12-31T23:59:59.000Z

26

Impact of additives for enhanced sulfur dioxide removal on re-emissions of mercury in wet flue gas desulfurization  

Science Journals Connector (OSTI)

Abstract The wet flue gas desulfurization process (FGD) in fossil fired power plants offers the advantage of simultaneously removing SO2 and other water soluble pollutants, such as certain oxidized mercury compounds (Hg2+). In order to maximize SO2 removal efficiency of installed FGD units, organic additives can be utilized. In the context of multi-pollutant control by wet FGD, the effect of formic and adipic acid on redox reactions of dissolved mercury compounds is investigated with a continuously operated lab-scale test-rig. For sulfite ( SO 3 2 - ) concentrations above a certain critical value, their potential as reducing agent leads to rapidly increasing formation and re-emission of elemental mercury (Hg0). Increasing chloride concentration and decreasing pH and slurry temperature have been identified as key factors for depressing Hg0 re-emissions. Both organic additives have a negative impact on Hg-retention and cause increased Hg0 re-emissions in the wet FGD process, with formic acid being the significantly stronger reducing agent. Different pathways of Hg2+ reduction were identified by qualitative interpretation of the pH-dependence and by comparison of activation enthalpies and activation entropies. While the first mechanism proposed identifies SO 3 2 - as reducing agent and is therefore relevant for any FGD process, the second mechanism involves the formate anion, thus being exclusively relevant for \\{FGDs\\} utilizing formic acid as additive.

Barna Heidel; Melanie Hilber; Günter Scheffknecht

2014-01-01T23:59:59.000Z

27

Separation of Fine Particles from Gases in Wet Flue Gas Desulfurization System Using a Cascade of Double Towers  

Science Journals Connector (OSTI)

Separation of Fine Particles from Gases in Wet Flue Gas Desulfurization System Using a Cascade of Double Towers ... The authors thank the High-Tech Research and Development Program of China (No. 2008AA05Z306), the Natural Science Foundation of Jiangsu Province (No. BK2008283), and the Scientific Research Foundation of Graduate School of Southeast University for their financial support. ... with high performance by cascading packed columns. ...

Jingjing Bao; Linjun Yang; Shijuan Song; Guilong Xiong

2012-02-15T23:59:59.000Z

28

Permitting and solid waste management issues for the Bailly Station wet limestone Advanced Flue Gas Desulfurization (AFGD) system  

SciTech Connect

Pure Air (a general partnership between Air Products and Chemicals, Inc., and Mitsubishi Heavy Industries America, Inc.). is constructing a wet limestone co-current advanced flue gas desulfurization (AFGD) system that has technological and commercial advantages over conventional FGD systems in the United States. The AFGD system is being installed at the Northern Indiana Public Service Company's Bailly Generating Station near Gary, Indiana. The AFGD system is scheduled to be operational by the Summer, 1992. The AFGD system will remove at least 90 percent of the sulfur dioxide (SO{sub 2}) in the flue gas from Boilers 7 and 8 at the Station while burning 3.2 percent sulfur coal. Also as part of testing the AFGD system, 95 percent removal of SO{sub 2} will be demonstrated on coals containing up to 4.5 percent sulfur. At the same time that SO{sub 2} is removed from the flue gas, a gypsum by-product will be produced which will be used for wallboard manufacturing. Since the AFGD system is a pollution control device, one would expect its installation to be received favorably by the public and regulatory agencies. Although the project was well received by regulatory agencies, on public group (Save the Dunes Council) was initially concerned since the project is located adjacent to the Indiana Dunes National Lakeshore. The purpose of this paper is to describe the project team's experiences in obtaining permits/approvals from regulatory agencies and in dealing with the public. 1 ref., 1 fig., 2 tabs.

Bolinsky, F.T. (Pure Air, Allentown, PA (United States)); Ross, J. (Northern Indiana Public Service Co., Hammond, IN (United States)); Dennis, D.S. (United Engineers and Constructors, Inc., Denver, CO (United States). Stearns-Roger Div.); Huston, J.S. (Environmental Alternatives, Inc., Warren NJ (USA))

1991-01-01T23:59:59.000Z

29

Summary and assessment of METC zinc ferrite hot coal gas desulfurization test program, final report: Volume 2, Appendices  

SciTech Connect

The Morgantown Energy Technology Center (METC) has conducted a test program to develop a zinc ferrite-based high temperature desulfurization process which could be applied to fuel gas entering downstream components such as molten carbonate fuel cells or gas turbines. As a result of prior METC work with iron oxide and zinc oxide sorbents, zinc ferrite evolved as a candidate with the potential for high capacity, low equilibrium levels of H/sub 2/S, and structural stability after multiple regenerations. The program consisted of laboratory-scale testing with a two-inch diameter reactor and simulated fixed-bed gasifier gas; bench-scale testing with a six-inch diameter reactor and actual gas from the METC 42-inch fixed bed gasifier; as well as laboratory-scale testing of zinc ferrite with simulated fluidized bed gasifier gas. Data from sidestream testing are presented. 18 refs.

Underkoffler, V.S.

1986-12-01T23:59:59.000Z

30

Desulfurization of heavy oil  

Science Journals Connector (OSTI)

Strategies for heavy oil desulfurization were evaluated by reviewing desulfurization literature and critically assessing the viability of the various methods for heavy oil. The desulfurization methods includin...

Rashad Javadli; Arno de Klerk

2012-03-01T23:59:59.000Z

31

Partitioning of mercury, arsenic, selenium, boron, and chloride in a full-scale coal combustion process equipped with selective catalytic reduction, electrostatic precipitation, and flue gas desulfurization systems  

SciTech Connect

A full-scale field study was carried out at a 795 MWe coal-fired power plant equipped with selective catalytic reduction (SCR), an electrostatic precipitator (ESP), and wet flue gas desulfurization (FGD) systems to investigate the distribution of selected trace elements (i.e., mercury, arsenic, selenium, boron, and chloride) from coal, FGD reagent slurry, makeup water to flue gas, solid byproduct, and wastewater streams. Flue gases were collected from the SCR outlet, ESP inlet, FGD inlet, and stack. Concurrent with flue gas sampling, coal, bottom ash, economizer ash, and samples from the FGD process were also collected for elemental analysis. By combining plant operation parameters, the overall material balances of selected elements were established. The removal efficiencies of As, Se, Hg, and B by the ESP unit were 88, 56, 17, and 8%, respectively. Only about 2.5% of Cl was condensed and removed from flue gas by fly ash. The FGD process removed over 90% of Cl, 77% of B, 76% of Hg, 30% of Se, and 5% of As. About 90% and 99% of the FGD-removed Hg and Se were associated with gypsum. For B and Cl, over 99% were discharged from the coal combustion process with the wastewater. Mineral trona (trisodium hydrogendicarbonate dehydrate, Na{sub 3}H(CO{sub 3}){sub 2}.2H{sub 2}O) was injected before the ESP unit to control the emission of sulfur trioxide (SO{sub 3}). By comparing the trace elements compositions in the fly ash samples collected from the locations before and after the trona injection, the injection of trona did not show an observable effect on the partitioning behaviors of selenium and arsenic, but it significantly increased the adsorption of mercury onto fly ash. The stack emissions of mercury, boron, selenium, and chloride were for the most part in the gas phase. 47 refs., 3 figs., 11 tabs.

Chin-Min Cheng; Pauline Hack; Paul Chu; Yung-Nan Chang; Ting-Yu Lin; Chih-Sheng Ko; Po-Han Chiang; Cheng-Chun He; Yuan-Min Lai; Wei-Ping Pan [Western Kentucky University, Bowling Green, KY (United States). Institute for Combustion Science and Environmental Technology

2009-09-15T23:59:59.000Z

32

Flue gas desulfurization sludge: establishment of vegetation on ponded and soil-applied waste. Final report January 1977-September 1981  

SciTech Connect

The report gives results of research to identify and evaluate forms of vegetation and methods of their establishment for reclaiming retired flue gas desulfurization sludge ponds. Also studied were the soil liming value of limestone scrubber sludge (LSS) and plant uptake and percolation losses of some chemical nutrients in the sludge. Several vegetation schemes were evaluated between 1977 and 1982 for covering and stabilizing LSS at Colbert Steam Plant, Cherokee, AL, and Shawnee Steam Plant, Paducah, KY. Eleven tree and 10 grass or legume species were tested for adaptability and survival when planted directly in LSS or in LSS amended with soil, municipal sewage sludge, or standard potting mix. Other studies indicated that LSS apparently has sufficient unreacted limestone to be a satisfactory soil liming agent.

Giordano, P.M.; Mays, D.A.; Soileau, J.M.

1984-01-01T23:59:59.000Z

33

Management of dry flue gas desulfurization by-products in underground mines. Quarterly report, April 1--June 30, 1996  

SciTech Connect

On September 30, 1993, the US Department of Energy - Morgantown Energy Technology Center (DOE-METC) and Southern Illinois University at Carbondale (SIUC) entered into a cooperative research agreement entitled {open_quotes}Management of Dry Flue Gas Desulfurization By-Products in Underground Mines{close_quotes} (DE-FC21-93MC30252). Under the agreement Southern Illinois University at Carbondale will develop and demonstrate two technologies for the placement of coal combustion residues in abandoned underground coal mines, and will assess the environmental impact of these technologies for the management of coal combustion by-products. The two technologies for the underground placement that will be developed and demonstrated are: (1) pneumatic placement, using virtually dry materials, and (2) hydraulic placement, using a {open_quotes}paste{close_quotes} mixture of materials with about 70% solids. Phase II of the overall program began April 1, 1996. The principal objective of Phase II is to develop and fabricate the equipment for placing the coal combustion by-products underground, and to conduct a demonstration of the technologies on the surface. Therefore, this quarter has been largely devoted to developing specifications for equipment components, visiting fabrication plants throughout Southern Illinois to determine their capability for building the equipment components in compliance with the specifications, and delivering the components in a timely manner.

NONE

1997-05-01T23:59:59.000Z

34

Recycling of Flue Gas Desulfurization residues in gneiss based hot mix asphalt: Materials characterization and performances evaluation  

Science Journals Connector (OSTI)

Abstract On the one hand, huge amount of Flue Gas Desulfurization (FGD) residues, produced during scrubbing flue gas, is discarded as solid waste. Such solid waste would cause serious environmental problems. One the other hand, high quality aggregates, such as limestone and basalt, are running out due to the rapid development of highway construction. Ungraded aggregates such as gneiss are therefore considered in China to replace the high quality aggregates. The application of FGD residues as a filler in gneiss based asphalt mixture has benefits both in environmental and economic sides. The main objective of this research was to visualize the raw materials characterization and evaluate the effect of FGD residues on the performance of gneiss based asphalt mixture. X-ray diffraction (XRD), X-ray fluorescence (XRF), Scanning Electron Microscope (SEM), Differential Scanning Calorimetric & Thermal gravimetric (DSC–TG) were used to investigate the features of raw materials. The performance of gneiss based asphalt mixture including high-temperature deformation resistance, low-temperature crack resistance and moisture-induced damage resistance were evaluated. Dynamic creep test, three-point bending test, Retained Marshall Stability (RMS), Tensile Strength Ratio (TSR), Indirect Tensile (IDT) strength and Resilient Modulus (MR) test were conducted and analyzed. Dissipated Creep Strain Energy to fracture (DCSEf) ratio, fracture energy and model analysis were also used to evaluate moisture resistance, crack resistance and deformation resistance of asphalt mixture respectively. Research results indicate that FGD residues can partly improve the moisture resistance and crack resistance of gneiss asphalt mixture, while it might worse the high-temperature deformation resistance.

Zongwu Chen; Shaopeng Wu; Fuzhou Li; Juyong Chen; Zhehuan Qin; Ling Pang

2014-01-01T23:59:59.000Z

35

Advances of flue gas desulfurization technology for coal-fired boilers and strategies for sulfur dioxide pollution prevention in China  

SciTech Connect

Coal is one of the most important kinds of energy resources at the present time and in the immediate future in China. Sulfur dioxide resulting from combustion of coal is one of the principle pollutants in the air. Control of SO{sub 2} discharge is still a major challenge for environmental protection in developing China. In this paper, research, development and application of technology of flue gas desulfurization (FGD) for coal-fired boilers in China will be reviewed with emphasis on cost-effective technology, and the development trends of FGD technology, as well as the strategy for SO{sub 2} discharge control in China, will be analyzed. A practical technology for middle-small-sized boilers developed by the primary author and the field investigation results will also be presented. At present, there are four major kinds of FGD technologies that are practical to be applied in China for their cost-effectiveness and efficiency to middle-small-sized boilers. An important development trend of the FGD technology for middle-small-sized boilers for the next decade is improvement of the existing cost-effective wet-type FGD technology, and in the future it will be the development of dry-type FGD technology. For middle-sized generating boilers, the development direction of the FGD technology is the spraying and drying process. For large-sized generating boilers, the wet-type limestone-plaster process will still be applied in the immediate future, and dry-type FGD technologies, such as ammonia with electron beam irradiation, will be developed in the future. State strategies for the control of SO{sub 2} discharge will involve the development and popularization of efficient coal-fired devices, extension of gas coal and liquefied coal, spreading coal washing, and centralized heating systems.

Yang, C.; Zeng, G.; Li, G.; Qiu, J.

1999-07-01T23:59:59.000Z

36

E-Print Network 3.0 - advanced hot-gas desulfurization Sample...  

NLE Websites -- All DOE Office Websites (Extended Search)

; Materials Science 28 Reproducedwith pennissionfrom ElsevierPergamon Biomass and Bioenerg..' Vol: 10, :os 2-3, pp..149-l66, 1996 Summary: at a commercialscale.. But hot-gas...

37

Adsorption and desorption of sulfur dioxide on novel adsorbents for flue gas desulfurization. Final report, September 1, 1994--February 29, 1996  

SciTech Connect

A sol-gel granulation method was developed to prepare spherical {gamma}-alumina granular supports and supported CuO granular sorbents for flue gas desulfurization. The prepared {gamma}-alumina supported CuO sorbents exhibit desirable pore structure and excellent mechanical properties. The sorbents contain higher loading (30-40 wt. %) of CuO dispersed in the monolayer or sub-monolayer form, giving rise to a larger SO{sub 2} sorption capacity ({gt}20 wt.%) and a faster sorption rate as compared to similar sorbents reported in the literature. With these excellent sulfation and mechanical properties, the sol-gel derived {gamma}-alumina supported CuO granular sorbents offer great potential for use in the dry, regenerative flue gas desulfurization process. Research efforts were also made to prepare DAY zeolite supported sorbents with various CuO contents by the microwave and conventional thermal dispersion methods at different conditions. Monolayer or sub-monolayer coating of Cu(NO{sub 3})sub 2 or CuO was achieved on several DAY supported sorbents by the microwave heating method but not by the conventional thermal dispersion method. The DAY zeolite supported CuO sorbents prepared by the microwave heating method can adsorb up to 15 wt.% of SO{sub 2}. The results obtained have demonstrated the feasibility of effective preparation of zeolite supported CuO sorbents by the microwave heating method.

Lin, Y.S.; Deng, S.G.

1996-08-05T23:59:59.000Z

38

The United States has significant natural gas  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

United States has significant natural gas United States has significant natural gas and oil reserves. But many of these resources are increasingly harder to locate and bring into production. To help meet this challenge, the U.S. Department of Energy's Office of Fossil Energy over the years has amassed wide ranging expertise in areas related to deepwater resource location, production, safety and environmental protection. The goal of these activities has been to not only help overcome

39

Unit Cost Natural Gas | OpenEI  

Open Energy Info (EERE)

2 2 Varnish cache server Browse Upload data GDR 429 Throttled (bot load) Error 429 Throttled (bot load) Throttled (bot load) Guru Meditation: XID: 2142281532 Varnish cache server Unit Cost Natural Gas Dataset Summary Description Provides annual energy usage for years 1989 through 2010 for UT at Austin; specifically, electricity usage (kWh), natural gas usage (Mcf), associated costs. Also provides water consumption for 2005 through 2010. Source University of Texas (UT) at Austin, Utilities & Energy Management Date Released Unknown Date Updated Unknown Keywords Electricity Consumption Natural Gas Texas Unit Cost Electricity Unit Cost Natural Gas University Water Data application/vnd.ms-excel icon Energy and Water Use Data for UT-Austin (xls, 32.8 KiB) Quality Metrics

40

Price Liquefied Freeport, TX Natural Gas Exports Price to United...  

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

United Kingdom (Dollars per Thousand Cubic Feet) Price Liquefied Freeport, TX Natural Gas Exports Price to United Kingdom (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1...

Note: This page contains sample records for the topic "gas desulfurization units" 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

FASTCHEM/trademark/ (Fly Ash and Flue Gas Desulfurization Sludge Transport and Geochemistry) package: Volume 2, User's guide to the EFLOW groundwater flow code  

SciTech Connect

This report documents a two-dimensional finite element code, EFLOW, developed to simulate water flow in fully or variably saturated porous media. This code is one component in the FASTCHEM/trademark/ (Fly Ash and Flue Gas Desulfurization Sludge Transport and Geochemistry) package. The formulation of the governing equations and the numerical procedures used in the code are presented. The flow equation is approximated using the Galerkin finite element method. For variably saturated flow problems, nonlinearities caused by unsaturated soil properties, atmospheric boundary conditions (e.g., infiltration, evaporation and seepage faces), and water uptake by plant roots are treated using Picard or Newton-Raphson methods. For fully saturated unconfined flow problems, the governing equations are formulated in an areal plane, and nonlinear water-table boundary conditions are treated using the Picard method. Several test problems are presented to verify the code and demonstrate its utility. These problems range from simple one-dimensional to complex two-dimensional and axisymmetric problems. 24 refs., 39 figs., 27 tabs.

Not Available

1988-09-01T23:59:59.000Z

42

Desulfurization behavior of iron-based sorbent with MgO and TiO{sub 2} additive in hot coal gas  

SciTech Connect

The sulfidation behaviors of iron-based sorbent with MgO and MgO-TiO{sub 2} are studied under different isothermal conditions from 623 to 873 K in a fixed bed reactor. The results of sorbents sulfidation experiments indicate that the sorbents with MgO and TiO{sub 2} additives are more attractive than those without additives for desulfurization of hot coal gas. The sulfur capacity (16.17, 18.45, and 19.68 g S/100 g sorbent) of M1F, M3F, and M5F sorbent containing 1, 3, and 5% MgO, respectively, is obviously bigger than that (15.02 g S/100 g sorbent) of M0F without additive. The feasible sulfidation temperature range for M3F sorbent is 773-873 K. The M3F sorbent is optimally regenerated at the temperature of 873 K, under the gas containing 2% oxygen, 15% steam and N{sub 2}, in the space velocity of 2500 h{sup -1}. The sorbent regenerated is also well performed in the second sulfidation (the effective sulfur capacities of 17.98 g S/100 g sorbents and the efficiency of removal sulfur of 99%). The capacity to remove sulfur decreases with steam content increasing in feeding gas from 0 to 10%, but it can restrain the formation of carbon and iron carbide. The addition of TiO{sub 2} in sorbent can shift the optimal sulfidation temperature lower. The iron-based sorbent with 3% MgO and 10% TiO{sub 2} (MFT) is active to the deep removal of H{sub 2}S and COS, especially in the temperature range of 673-723 K. The sulfur removal capacity of MFT sorbent is 21.60 g S/100 g sorbent. 16 refs., 12 figs., 8 tabs.

Weiren Bao; Zong-you Zhang; Xiu-rong Ren; Fan Li; Li-ping Chang [Taiyuan University of Technology, Taiyuan (China). Key Laboratory of Coal Science and Technology

2009-07-15T23:59:59.000Z

43

Efficiency United (Gas) - Commercial Efficiency Program | Department of  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Efficiency United (Gas) - Commercial Efficiency Program Efficiency United (Gas) - Commercial Efficiency Program Efficiency United (Gas) - Commercial Efficiency Program < Back Eligibility Commercial Industrial Savings Category Heating & Cooling Commercial Heating & Cooling Heating Home Weatherization Commercial Weatherization Appliances & Electronics Other Construction Manufacturing Water Heating Maximum Rebate See Page Four of Utility Application: $100-$50,000/customer/year depending on utility and remaining funding Custom:40% of project cost Program Info State Michigan Program Type Utility Rebate Program Rebate Amount Trap Repair or Replacement: $50/unit Boilers: $1-$1.50/MBH Furnace Replacement: $1.50/MBH or $150/unit Boiler Modulation Burner Control Retrofit: $1000/unit Boiler Water Reset Control: $300/unit

44

Life Cycle Greenhouse Gas Analysis of Natural Gas Extraction & Delivery in the United Statesy  

E-Print Network (OSTI)

delivery to large end-users? 6. How does natural gas power generation compare to coal-fired powerLife Cycle Greenhouse Gas Analysis of Natural Gas Extraction & Delivery in the United Statesy of natural gas in the United States? 3. Who uses natural gas in the U.S.? 4 Wh d t l f ?4. Where does natural

Boyer, Elizabeth W.

45

LIFAC sorbent injection desulfurization demonstration project  

SciTech Connect

In December 1990, the US Department of Energy selected 13 projects for funding under the Federal Clean Coal Technology Program (Round 3). One of the projects selected was the project sponsored by LIFAC North America, (LIFAC NA), titled LIFAC Sorbent Injection Desulfurization Demonstration Project.'' The host site for this $17 million, three-phase project is Richmond Power and Light's Whitewater Valley Unit No. 2 in Richmond, Indiana. The LIFAC technology uses upper-furnace limestone injection with patented humidification of the flue gas to remove 75--80% of the sulfur dioxide (SO{sub 2}) in the flue gas. In November 1990, after a ten (10) month negotiation period, LIFAC NA and the US DOE entered into a Cooperative Agreement for the design, construction, and demonstration of the LIFAC system. This report is the first Technical Progress Report covering the period from project execution through the end of December 1990. Due to the power plant's planned outage schedule, and the time needed for engineering, design and procurement of critical equipment, DOE and LIFAC NA agreed to execute the Design Phase of the project in August 1990, with DOE funding contingent upon final signing of the Cooperative Agreement.

Not Available

1991-01-01T23:59:59.000Z

46

COAL DESULFURIZATION PRIOR TO COMBUSTION  

E-Print Network (OSTI)

Corporation, 5-25~79. on Coal Liquefaction at ChevronHamersma, et a L, "Meyers Process for Coal Desulfurization,"in Wheelock, Coal Desulfurization, ACS Symp. Ser 64 (1977(.

Wrathall, J.

2013-01-01T23:59:59.000Z

47

Experimental and numerical study of gas dynamics of exhaust pipe of gas turbine unit  

Science Journals Connector (OSTI)

A few geometrical configurations of exhaust pipe of marine gas turbine unit were investigated experimentally in NPP “Mashproeykt...

Valery Solodov; Juriy Starodubtsev; Boris Isakov…

2004-02-01T23:59:59.000Z

48

Practical Operation of Prep-Scale Gas Chromatographic Units  

Science Journals Connector (OSTI)

......given in Table I. The cost of a recycling unit is...nitrogen is used as carrier gas. For narrower columns it depends on the length of production cycles. Once a recycling unit is used, the carrier gas cost becomes negligible, and......

B. Roz; R. Bonmati; G. Hagenbach; P. Valentin; G. Guiochon

1976-08-01T23:59:59.000Z

49

Small UHV-compatible gas inlet unit  

Science Journals Connector (OSTI)

A simple versatile device is described for introducing a dose of a selected pure gas into an UHV system.

S Koc

1987-01-01T23:59:59.000Z

50

Management of dry flue gas desulfurization by-products in underground mines. Topical report, October 1, 1993--March 31, 1998  

SciTech Connect

The DESEVAL-TRANS program is developed for the purpose of helping the engineer to design and economically evaluate coal combustion byproduct transportation systems that will operate between the power plant and the disposal site. The objective of the research project was to explore the technical, environmental and economic feasibility of disposing coal combustion byproducts in underground mines in Illinois. The DESEVAL-TRANS (short for Design and Evaluation of Transportation Systems) was developed in the Materials Handling and Systems Economics branch of the overall project. Four types of coal combustion byproducts were targeted for transportation and handling: Conventional fly ash; Scrubber sludge; Fluidized Bed Combustion (FBC) fly ash; and Spent-bed ash. Several transportation and handling systems that could handle these byproducts were examined. These technologies were classified under three general categories: Truck; Rail; and Container. The purpose of design models is to determine the proper number of transport units, silo capacity, loading and unloading rates, underground placement capacity, number of shifts, etc., for a given case, defined by a distance-tonnage combination. The cost computation models were developed for the determination of the operating and capital costs. An economic evaluation model, which is common to all categories, was also developed to establish the cost-per-ton of byproduct transported.

NONE

1998-09-01T23:59:59.000Z

51

Management of dry flue gas desulfurization by-products in underground mines. Technical progress report, 1 January--31 March 1994  

SciTech Connect

Southern Illinois University at Carbondale will develop and demonstrate several technologies for the handling and transport of dry coal combustion residues and for the underground placement in abandoned coal mines and assess associated environmental impacts. Although parts of the Residue Characterization portion of the program were delayed because residue samples were not obtained, other parts of the program are proceeding on schedule. The delays in obtaining residue samples were primarily caused by adverse weather conditions, the shut-down of one unit at the City Water, Light, and Power Company Plant for routing maintenance and problems due to conflicting schedules of utility and program personnel. However, by the end of the quarter most residue samples had been obtained, and the residue characterization studies were under way. Progress is described for five studies: environmental assessment and geotechnical stability and subsidence impacts; residue characterization; physico-chemical characterization of residues; identification and assessment of handling/transportation systems for FGD residues; and residue handling and transport.

Chugh, Y.P.; Esling, S.; Ghafoori, N.; Honaker, R.; Paul, B.; Sevim, H.; Thomasson, E.

1994-04-01T23:59:59.000Z

52

Efficiency United (Gas) - Residential Efficiency Program | Department of  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Efficiency United (Gas) - Residential Efficiency Program Efficiency United (Gas) - Residential Efficiency Program Efficiency United (Gas) - Residential Efficiency Program < Back Eligibility Low-Income Residential Multi-Family Residential Residential Savings Category Heating & Cooling Commercial Heating & Cooling Heating Home Weatherization Commercial Weatherization Sealing Your Home Appliances & Electronics Construction Design & Remodeling Other Ventilation Manufacturing Water Heating Windows, Doors, & Skylights Maximum Rebate Weatherization Measures: 50% of the cost Windows: $150 Water Heaters/Clothes Washers: 1 Pipe Wrap: Limit of 10 linear ft. Faucet Aerators: 2 High Efficiency Shower Head: 2 Program Info State Michigan Program Type Utility Rebate Program Rebate Amount Boiler: $200 Furnace: $100 - $200

53

Increase of unit efficiency by improved waste heat recovery  

SciTech Connect

For coal-fired power plants with flue gas desulfurization by wet scrubbing and desulfurized exhaust gas discharge via cooling tower, a further improvement of new power plant efficiency is possible by exhaust gas heat recovery. The waste heat of exhaust gas is extracted in a flue gas cooler before the wet scrubber and recovered for combustion air and/or feedwater heating by either direct or indirect coupling of heat transfer. Different process configurations for heat recovery system are described and evaluated with regard to net unit improvement. For unite firing bituminous coal an increase of net unit efficiency of 0.25 to 0.7 percentage points and for lignite 0.7 to 1.6 percentage points can be realized depending on the process configurations of the heat recovery systems.

Bauer, G.; Lankes, F.

1998-07-01T23:59:59.000Z

54

Modern Shale Gas Development in the United States: A Primer  

Energy.gov (U.S. Department of Energy (DOE))

This Primer on Modern Shale Gas Development in the United States was commissioned through the Ground Water Protection Council (GWPC). It is an effort to provide sound technical information on and...

55

Natural Gas Processing Plants in the United States: 2010 Update  

Gasoline and Diesel Fuel Update (EIA)

This special report presents an analysis of natural gas processing plants This special report presents an analysis of natural gas processing plants in the United States as of 2009 and highlights characteristics of this segment of the industry. The purpose of the paper is to examine the role of natural gas processing plants in the natural gas supply chain and to provide an overview and summary of processing plant characteristics in the United States, such as locations, capacities, and operations. Key Findings There were 493 operational natural gas processing plants in the United States with a combined operating capacity of 77 billion cubic feet (Bcf) per day. Overall, operating capacity increased about 12 percent between 2004 and 2009, not including the processing capacity in Alaska1. At the same time, the number of all processing plants in the lower 48 States decreased

56

A NOVEL APPROACH TO CATALYTIC DESULFURIZATION OF COAL  

SciTech Connect

Column chromatographic separation of the S=PBu{sub 3}/PBu{sub 3} product mixture followed by weighing the S=PBu{sub 3}, and by vacuum distillation of S=PBu{sub 3}/PBu{sub 3}mixture followed by gas chromatographic analysis are described. Effects of coal mesh size, pre-treatment with methanol Coal (S) + excess PR{sub 3} {yields} Coal + S=PR{sub 3}/PBu{sub 3} and sonication on sulfur removal by PBu{sub 3} revealed that particle size was not observed to affect desulfurization efficiency in a consistent manner. Coal pretreatment with methanol to induce swelling or the addition of a filter aid such as Celite reduced desulfurization efficiency of the PBu{sub 3} and sonication was no more effective than heating. A rationale is put forth for the lack of efficacy of methanol pretreatment of the coal in desulfurization runs with PBu{sub 3}. Coal desulfurization with PBu{sub 3} was not improved in the presence of miniscule beads of molten lithium or sodium as a desulfurizing reagent for SPBu{sub 3} in a strategy aimed at regenerating PBu{sub 3} inside coal pores. Although desulfurization of coals did occur in sodium solutions in liquid ammonia, substantial loss of coal mass was also observed. Of particular concern is the mass balance in the above reaction, a problem which is described in some detail. In an effort to solve this difficulty, a specially designed apparatus is described which we believe can solve this problem reasonably effectively. Elemental sodium was found to remove sulfur quantitatively from a variety of polycyclic organosulfur compounds including dibenzothiophene and benzothiophene under relatively mild conditions (150 C) in a hydrocarbon solvent without requiring the addition of a hydrogen donor. Lithium facilitates the same reaction at a higher temperature (254 C). Mechanistic pathways are proposed for these transformations. Curiously, dibenzothiophene and its corresponding sulfone was virtually quantitatively desulfurized in sodium solutions in liquid ammonia at -33 C, although the yield of biphenyl was only about 20 to 30%. On the other hand, benzothiophene gave a high yield of 2-ethylthiophenol under these conditions. Although our superbase P(MeNCH{sub 2}CH{sub 2}){sub 3}N, which is now commercially available, is a more effective desulfurizing agent for a variety of organophosphorus compounds than PPh{sub 3} or its acyclic analogue P(NMe){sub 3}, it does not desulfurize benzothiophene or dibenzothiophene.

John G. Verkade

2001-11-01T23:59:59.000Z

57

The Biocatalytic Desulfurization Project  

SciTech Connect

The material in this report summarizes the Diversa technical effort in development of a biocatalyst for the biodesulfurization of Petro Star diesel as well as an economic report of standalone and combined desulfurization options, prepared by Pelorus and Anvil, to support and inform the development of a commercially viable process. We will discuss goals of the projected as originally stated and their modification as guided by parallel efforts to evaluate commercialization economics and process parameters. We describe efforts to identify novel genes and hosts for the generation of an optimal biocatalyst, analysis of diesel fuels (untreated, chemically oxidized and hydrotreated) for organosulfur compound composition and directed evolution of enzymes central to the biodesulfurization pathway to optimize properties important for their use in a biocatalyst. Finally we will summarize the challenges and issues that are central to successful development of a viable biodesulfurization process.

David Nunn; James Boltz; Philip M. DiGrazia; Larry Nace

2006-03-03T23:59:59.000Z

58

Produce synthesis gas by steam reforming natural gas  

SciTech Connect

For production of synthesis gas from natural gas the steam reforming process is still the most economical. It generates synthesis gas for ammonia and methanol production as well as hydrogen, oxo gas and town gas. After desulfurization, the natural gas is mixed with steam and fed to the reforming furnace where decomposition of hydrocarbons takes place in the presence of a nickel-containing catalyst. Synthesis gas that must be free of CO and CO/sub 2/ is further treated in a CO shift conversion, a CO/sub 2/ scrubbing unit and a methanation unit. The discussion covers the following topics - reforming furnace; the outlet manifold system; secondary reformer; reformed gas cooling. Many design details of equipment used are given.

Marsch, H.D.; Herbort, H.J.

1982-06-01T23:59:59.000Z

59

Producer gas from citrus wood fuels irrigation power unit  

SciTech Connect

A 90-hp diesel engine operating a citrus irrigation system was converted to run on a dual-fuel mixture utilizing producer gas from citrus wood chips as the main fuel source. A chip feeder mechanism, gasifier, filter system and control unit were designed to meet typical irrigation power requirements. Blighted, unproductive and dead trees removed near the irrigation site were used for chipping. Data on chip moisture content, fuel analysis, drying rate and fuel/tree weight are presented but labour and equipment costs were not determined. 14 references.

Churchill, D.B.; Hedden, S.L.; Whitney, J.D.; Shaw, L.N.

1985-01-01T23:59:59.000Z

60

Federal Register Notice for Life Cycle Greenhouse Gas Perspective on Exporting Liquefied Natural Gas from the United States  

Energy.gov (U.S. Department of Energy (DOE))

The Office of Fossil Energy of the Department of Energy gives notice of the availability of the report Life Cycle Greenhouse Gas Perspective on Exporting Liquefied Natural Gas from the United...

Note: This page contains sample records for the topic "gas desulfurization units" 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

Gas-turbine units of OAO Aviadvigatel’ designed for operation on synthesis gas obtained from gasification of coal  

Science Journals Connector (OSTI)

Problems that have to be solved for adapting a 16-MW gas-turbine unit used as part of a gas turbine-based power station for firing low-grade...

D. D. Sulimov

2010-02-01T23:59:59.000Z

62

THE BIOCATALYTIC DESULFURIZATION PROJECT  

SciTech Connect

The analysis of Petro Star diesel sulfur species is complete and a report is attached. Further analytical efforts will concentrate on characterization of diesel fuel, hydrodesulfurized to varying degrees, in order to determine sulfur species that may be problematic to hydrogen treatment and represent potential target substrates for biodesulfurization in a combined HDS-BDS process. Quotes have been received and are being considered for the partial treatment of Petro Star Inc. marine diesel fuel. Direction of research is changing slightly; economic analysis of the hyphenated--BDSHDS, BDS-CED--has shown the highest probability of success to be with a BDS-HDS process where the biodesulfurization precedes hydrodesulfurization. Thus, the microorganisms will be tailored to focus on those compounds that tend to be recalcitrant to hydrodesulfurization and decrease the severity of the hydrodesulfurization step. A separate, detailed justification for this change is being prepared. Research activities have continued in the characterization of the desulfurization enzymes from multiple sources. Genes for all DszA, -B, -C and -D enzymes (and homologs) have been cloned and expressed. Activity determinations, on a variety of substituted benzothiophene and dibenzothiophene substrates, have been carried out and continue. In addition, chemical synthesis efforts have been carried out to generate additional substrates for analytical standards and activity determinations. The generation of a GSSM mutant library of the ''Rhodococcus IGTS8 dszA'' gene has been completed and development of protocols for a high throughput screen to expand substrate specificity are nearing completion. In an effort to obtain improved hosts as biocatalyst, one hundred-thirty ''Rhodococcus'' and related strains are being evaluated for growth characteristics and other criteria deemed important for an optimal biocatalyst strain. We have also begun an effort to generate derivatives of the entire IGTS8 BDS plasmid that will allow for its easy transfer and manipulation into a variety of hosts. To support this activity and to gain an understanding of additional genes that may potentially affect BDS activity, the nucleotide sequence of the entire complement of plasmids in IGTS8 is being determined. Lastly, we continue to develop genetic screens and selections for the discovery and improvement of the biodesulfurization genes and strains.

Scott Collins; David Nunn

2003-10-01T23:59:59.000Z

63

Desulfurization sorbent regeneration  

DOE Patents (OSTI)

A spent solid sorbent resulting from the removal of hydrogen sulfide from a fuel gas flow is regenerated with a steam-air mixture. The mixture of steam and air may also include additional nitrogen or carbon dioxide. The gas mixture contacts the spent sorbent containing metal sulfide at a temperature above 500/sup 0/C to regenerate the sulfide to metal oxide or carbonate. Various metal species including the period four transition metals and the lanthanides are suitable sorbents that may be regenerated by this method. In addition, the introduction of carbon dioxide gas permits carbonates such as those of strontium, barium and calcium to be regenerated. The steam permits regeneration of spent sorbent without formation of metal sulfate. Moreover, the regeneration will proceed with low oxygen concentrations and will occur without the increase in temperature to minimize the risk of sintering and densification of the sorbent. This method may be used for high-temperature fuel cells.

Jalan, V.M.; Frost, D.G.

1982-07-07T23:59:59.000Z

64

Price of Lake Charles, LA Natural Gas LNG Imports from United...  

Annual Energy Outlook 2012 (EIA)

Arab Emirates (Dollars per Thousand Cubic Feet) Price of Lake Charles, LA Natural Gas LNG Imports from United Arab Emirates (Dollars per Thousand Cubic Feet) Decade Year-0...

65

Changing Prospects for Natural Gas in the United States  

Science Journals Connector (OSTI)

...doubling ofoil life to 4000 hours...application of gas-fired combined-cycle...gas-fueled combustion turbine combined with...generation from the gas turbine part ofa facility...38, 39) and life cycle cost advantages...Steam-injected gas turbines represent a...

W. M. BURNET; T S. D. BAN

1989-04-21T23:59:59.000Z

66

High-volume, high-value usage of flue gas desulfurization (FGD) by- products in underground mines: Phase 1, Laboratory investigations. Quarterly report, April--June 1995  

SciTech Connect

The kinetics study which is investigating hydration reactions of the ADM by-product (Subtask 2.2) was continued this quarter. This study further aided in gaining information on mineral precipitation and dissolution reactions during hydration of the ADM materials. The information is of importance for a comprehensive understanding of the factors that control strength and long-term stability during aging of FGD materials. The decision was made by Addington, Inc., DOE, and the University of Kentucky that the originally selected mine site for the emplacement demonstration must be changed, mainly for safety reasons. Mine selection will be a priority for the next quarter (Jul--Sep, 1995). Another activity during this reporting period was related to Subtask 4.3, the selection and testing of the transport system for the FGD material. A laboratory-scale pneumatic emplacement test unit (ETU) for dry FGD materials was built at the CAER to generate data so that a final selection of the field demonstration technology can be made. A dry pneumatic system was chosen for laboratory testing because the equipment and expertise available at the CAER matched this sort of technology best. While the design of the laboratory system was based on shotcrete technology, the physical properties of the emplaced FGD material is expected to be similar for other transport techniques, either pneumatic or hydraulic. In other words, the selection of a dry pneumatic transport system for laboratory testing does not necessarily imply that a scaled-up version will be used for the field demonstration. The ETU is a convenient means of producing samples for subsequent chemical and physical testing by a representative emplacement technology. Ultimately, the field demonstration technology will be chosen based on the laboratory data and the suitability of locally available equipment.

NONE

1995-09-01T23:59:59.000Z

67

Changing Prospects for Natural Gas in the United States  

Science Journals Connector (OSTI)

...34). Diesel engine technology is...natural gas in reciprocating engines: (i) production...prob-lems when new models were first introduced...the capital cost of a combined-cycle...all based on reciprocating engine and gas turbine...

W. M. BURNET; T S. D. BAN

1989-04-21T23:59:59.000Z

68

Economic analysis of shale gas wells in the United States  

E-Print Network (OSTI)

Natural gas produced from shale formations has increased dramatically in the past decade and has altered the oil and gas industry greatly. The use of horizontal drilling and hydraulic fracturing has enabled the production ...

Hammond, Christopher D. (Christopher Daniel)

2013-01-01T23:59:59.000Z

69

Changing Prospects for Natural Gas in the United States  

Science Journals Connector (OSTI)

...re-quired for compressed natural gas (26), and these vehicles...the lower energy price of natural gas would be sufficient to attract...added equipment, such as high-pressure tanks, needed to store natural gas on board automobiles with...

W. M. BURNET; T S. D. BAN

1989-04-21T23:59:59.000Z

70

90-MW single-shaft power generating steam-gas unit based on the GTÉ-65 gas turbine and K-30-60 steam turbine  

Science Journals Connector (OSTI)

This is an examination of a variant of the monoblock PGU-90 steam-gas unit developed at the “Leningradskii Metallicheskii Zavod” (LMZ) branch of “Silovye mashiny” based on a GTÉ-65 gas turbine unit and a K-30-...

A. S. Lebedev; O. V. Antonyuk; V. A. Mart’yanov…

2011-01-01T23:59:59.000Z

71

Flue gas desulfurization gypsum and fly ash  

SciTech Connect

The Cumberland Fossil Plant (CUF) is located in Stewart County, Tennessee, and began commercial operation in 1972. This is the Tennessee Valley Authority`s newest fossil (coal-burning) steam electric generating plant. Under current operating conditions, the plant burns approximately seven million tons of coal annually. By-products from the combustion of coal are fly ash, approximately 428,000 tons annually, and bottom ash, approximately 115,000 tons annually. Based on historical load and projected ash production rates, a study was initially undertaken to identify feasible alternatives for marketing, utilization and disposal of ash by-products. The preferred alternative to ensure that facilities are planned for all by-products which will potentially be generated at CUF is to plan facilities to handle wet FGD gypsum and dry fly ash. A number of different sites were evaluated for their suitability for development as FGD gypsum and ash storage facilities. LAW Engineering was contracted to conduct onsite explorations of sites to develop information on the general mature of subsurface soil, rock and groundwater conditions in the site areas. Surveys were also conducted on each site to assess the presence of endangered and threatened species, wetlands and floodplains, archaeological and cultural resources, prime farmland and other site characteristics which must be considered from an environmental perspective.

Not Available

1992-05-01T23:59:59.000Z

72

Draft Addendum to Environmental Review Documents Concerning Exports of Natural Gas from the United States  

Energy.gov (U.S. Department of Energy (DOE))

On August 15, 2014, the Department of Energy's Office of Fossil Energy published the final Addendum To Environmental Review Documents Concerning Exports Of Natural Gas From The United States ...

73

Patent analysis to identify shale gas development in China and the United States  

Science Journals Connector (OSTI)

Abstract Shale gas has become an increasingly important form of hydrocarbon energy, and related technologies reflect the geographical characteristics of the countries where the gas is extracted and stored. The United States (U.S.) produces most of the world’s shale gas, while China has the world’s largest shale gas reserves. In this research, we focused on identifying the trends in shale-gas related technologies registered to the United States Patent and Trademark Office (USPTO) and to the State Intellectual Property Office of the People’s Republic of China (SIPO) respectively. To cluster shale-gas related technologies, we text-mined the abstracts of patent specifications. It was found that in the U.S., the key advanced technologies were related to hydraulic fracturing, horizontal drilling, and slick water areas, whereas China had a focus on proppants. The results of our study are expected to assist energy experts in designing energy policies related to technology importation.

Woo Jin Lee; So Young Sohn

2014-01-01T23:59:59.000Z

74

Uncertainty in Life Cycle Greenhouse Gas Emissions from United States Coal  

E-Print Network (OSTI)

analyses involving coal. Greenhouse gas emissions from fuel use and methane releases at coal mines, fuel.5 million metric tons of methane emissions. Close to 95% of domestic coal was consumed by the electricityUncertainty in Life Cycle Greenhouse Gas Emissions from United States Coal Aranya Venkatesh

Jaramillo, Paulina

75

Natural gas from shale formation – The evolution, evidences and challenges of shale gas revolution in United States  

Science Journals Connector (OSTI)

Abstract Extraction of natural gas from shale rock in the United States (US) is one of the landmark events in the 21st century. The combination of horizontal drilling and hydraulic fracturing can extract huge quantities of natural gas from impermeable shale formations, which were previously thought to be either impossible or uneconomic to produce. This review offers a comprehensive insight into US shale gas opportunities, appraising the evolution, evidence and the challenges of shale gas production in the US. The history of US shale gas in this article is divided into three periods and based on the change of oil price (i.e., the period before the 1970s oil crisis, the period from 1970s to 2000, and the period since 2000), the US has moved from being one of the world's biggest importers of gas to being self-sufficient in less than a decade, with the shale gas production increasing 12-fold (from 2000 to 2010). The US domestic natural gas price hit a 10-year low in 2012. The US domestic natural gas price in the first half of 2012 was about $2 per million British Thermal Unit (BTU), compared with Brent crude, the world benchmark price for oil, now about $ 80–100/barrel, or $14–17 per million BTU. Partly due to an increase in gas-fired power generation in response to low gas prices, US carbon emissions from fossil-fuel combustion fell by 430 million ton CO2 – more than any other country – between 2006 and 2011. Shale gas also stimulated economic growth, creating 600,000 new jobs in the US by 2010. However, the US shale gas revolution would be curbed, if the environmental risks posed by hydraulic fracturing are not managed effectively. The hydraulic fracturing is water intensive, and can cause pollution in the marine environment, with implications for long-term environmental sustainability in several ways. Also, large amounts of methane, a powerful greenhouse gas, can be emitted during the shale gas exploration and production. Hydraulic fracturing also may induce earthquakes. These environmental risks need to be managed by good practices which is not being applied by all the producers in all the locations. Enforcing stronger regulations are necessary to minimize risk to the environment and on human health. Robust regulatory oversight can however increase the cost of extraction, but stringent regulations can foster an historic opportunity to provide cheaper and cleaner gas to meet the consumer demand, as well as to usher in the future growth of the industry.

Qiang Wang; Xi Chen; Awadhesh N. Jha; Howard Rogers

2014-01-01T23:59:59.000Z

76

Changing Prospects for Natural Gas in the United States  

Science Journals Connector (OSTI)

...value (LHV), which excludes the heat of condensation of the water vapor in the exhaust. For natural gas combustion...Commonly used absorption fluid pairs are ammonia-water and lithium bromide-water. 51. D. R. Kosar, B. M. Cohen, W...

W. M. BURNET; T S. D. BAN

1989-04-21T23:59:59.000Z

77

Life Cycle Greenhouse Gas Perspective on Exporting Liquefied Natural Gas from the United States  

Energy.gov (U.S. Department of Energy (DOE))

This analysis calculates the life cycle greenhouse gas (GHG) emissions for regional coal and imported natural gas power in Europe and Asia. The primary research questions are as follows:...

78

Portugal Egypt Figure 2. Natural gas supply and disposition in the United States, 2012  

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

Portugal Egypt Figure 2. Natural gas supply and disposition in the United States, 2012 (trillion cubic feet) Natural Gas Plant Liquids Production Gross Withdrawals From Gas and Oil Wells Nonhydrocarbon Gases Removed Vented/Flared Reservoir Repressuring Production Dry Gas Imports Canada Trinidad/Tobago Natural Gas Storage Facilities Exports Japan Canada Mexico Additions Withdrawals Gas Industry Use Residential Commercial Industrial Vehicle Fuel Electric Power 29.5 0.8 0.2 3.3 2.963 0.112 0.620 0.971 0.014 24.1 1.3 2.9 2.8 2.5 2.9 7.2 0.03 9.1 0.003 Sources: Energy Information Administration (EIA), Form EIA-176, "Annual Report of Natural and Supplemental Gas Supply and Disposition"; Form EIA-895, "Annual Quantity and

79

Economics of Residential Gas Furnaces and Water Heaters in United States  

NLE Websites -- All DOE Office Websites (Extended Search)

Economics of Residential Gas Furnaces and Water Heaters in United States Economics of Residential Gas Furnaces and Water Heaters in United States New Construction Market Speaker(s): Alex Lekov Gabrielle Wong-Parodi James McMahon Victor Franco Date: May 8, 2009 - 12:00pm Location: 90-3122 In the new single-family home construction market, the choice of what gas furnace and gas water heater combination to install is primarily driven by first cost considerations. In this study, the authors use a life-cycle cost analysis approach that accounts for uncertainty and variability of inputs to assess the economic benefits of installing different gas furnace and water heater combinations. Among other factors, it assesses the economic feasibility of eliminating the traditional metal vents and replacing them with vents made of plastic materials used in condensing and power vent

80

LIFAC Sorbent Injection Desulfurization Demonstration Project: A DOE Assessment  

NLE Websites -- All DOE Office Websites (Extended Search)

41 41 LIFAC Sorbent Injection Desulfurization Demonstration Project: A DOE Assessment January 2001 U.S. Department of Energy National Energy Technology Laboratory P.O. Box 880, 3610 Collins Ferry Road Morgantown, WV 26507-0880 and P.O. Box 10940, 626 Cochrans Mill Road Pittsburgh, PA 15236-0940 website: www.netl.doe.gov Disclaimer 2 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

Note: This page contains sample records for the topic "gas desulfurization units" 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

United States Producing and Nonproducting Crude Oil and Natural Gas Reserves From 1985 Through 2004  

Gasoline and Diesel Fuel Update (EIA)

United States Producing and Nonproducing Crude Oil and Natural Gas Reserves From 1985 Through 2004 By Philip M. Budzik Abstract The Form EIA-23 survey of crude oil and natural gas producer reserves permits reserves to be differentiated into producing reserves, i.e., those reserves which are available to the crude oil and natural gas markets, and nonproducing reserves, i.e., those reserves which are unavailable to the crude oil and natural gas markets. The proportion of nonproducing reserves relative to total reserves grew for both crude oil and natural gas from 1985 through 2004, and this growth is apparent in almost every major domestic production region. However, the growth patterns in nonproducing crude oil and natural gas reserves are

82

U.S. Liquefied Natural Gas Exports to United Kingdom  

Gasoline and Diesel Fuel Update (EIA)

Babb, MT Havre, MT Port of Morgan, MT Pittsburg, NH Grand Island, NY Massena, NY Niagara Falls, NY Waddington, NY Sumas, WA Sweetgrass, MT Total to Chile Sabine Pass, LA Total to China Kenai, AK Sabine Pass, LA Total to India Freeport, TX Sabine Pass, LA Total to Japan Cameron, LA Kenai, AK Sabine Pass, LA Total to Mexico Douglas, AZ Nogales, AZ Calexico, CA Ogilby Mesa, CA Otay Mesa, CA Alamo, TX Clint, TX Del Rio, TX Eagle Pass, TX El Paso, TX Hidalgo, TX McAllen, TX Penitas, TX Rio Bravo, TX Roma, TX Total to Portugal Sabine Pass, LA Total to Russia Total to South Korea Freeport, TX Sabine Pass, LA Total to Spain Cameron, LA Sabine Pass, LA Total to United Kingdom Sabine Pass, LA Period: Monthly Annual

83

United States, Canada and Mexico Release the "North American Natural Gas  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

and Mexico Release the "North American and Mexico Release the "North American Natural Gas Vision" United States, Canada and Mexico Release the "North American Natural Gas Vision" February 25, 2005 - 10:29am Addthis WASHINGTON, DC -- The North American Energy Working Group (NAEWG), a group of senior energy officials from Canada, Mexico and the United States, today released the "North American Natural Gas Vision," a trilateral report by the three governments that includes information on the natural gas market in the North American region, including forecasts through the year 2012. U.S. Energy Secretary Samuel Bodman joined Minister of Natural Resources Canada R. John Efford and Mexico's Energy Secretary Fernando Elizondo in announcing the report's release. "This document is a key cooperative effort among the three countries to

84

A 25 kWe low concentration methane catalytic combustion gas turbine prototype unit  

Science Journals Connector (OSTI)

Abstract Low concentration methane, emitted from various industries e.g. coal mines and landfills into atmosphere, is not only an important greenhouse gas, but also a wasted energy resource if not utilized. In the past decade, we have been developing a novel VAMCAT (ventilation air methane catalytic combustion gas turbine) technology. This turbine technology can be used to mitigate methane emissions for greenhouse gas reduction, and also to utilize the low concentration methane as an energy source. This paper presents our latest research results on the development and demonstration of a 25 kWe lean burn catalytic combustion gas turbine prototype unit. Recent experimental results show that the unit can be operated with 0.8 vol% of methane in air, producing about 19–21 kWe of electricity output.

Shi Su; Xinxiang Yu

2014-01-01T23:59:59.000Z

85

Limiting net greenhouse gas emissions in the United States  

SciTech Connect

In 1988, Congress requested that DOE produce a study on carbon dioxide inventory and policy to provide an inventory of emissions sources and to analyze policies to achieve a 20% reduction in carbon dioxide emissions in 5 to 10 years and a 50% reduction in 15 to 20 years. Energy and environmental technology data were analyzed using computational analysis models. This information was then evaluated, drawing on current scientific understanding of global climate change, the possible consequences of anthropogenic climate change (change caused by human activity) and the relationship between energy production and use and the emission of radiatively important gases. Topics discussed include: state of the science in estimating atmosphere/climate change relationships, the potential consequences of atmosphere/climate change, us greenhouse emissions past and present, an approach to analyzing the technical potential and cost of reducing US energy-related greenhouse gas emissions, current policy base and National Energy Strategy actions, fiscal instruments, regulatory instruments, combined strategies and instruments, macroeconomic impacts, carbon taxation and international trade, a comparison to other studies.

Bradley, R A; Watts, E C; Williams, E R [eds.] [eds.

1991-09-01T23:59:59.000Z

86

Figure A1. Natural gas processing plant capacity in the United States, 2013 2012  

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

5 5 Figure A1. Natural gas processing plant capacity in the United States, 2013 2012 Table A2. Natural gas processing plant capacity, by state, 2013 (million cubic feet per day) Alabama 1,403 Arkansas 24 California 926 Colorado 5,450 Florida 90 Illinois 2,100 Kansas 1,818 Kentucky 240 Louisiana 10,737 Michigan 479 Mississippi 1,123

87

U.S. Liquefied Natural Gas Exports to United Kingdom  

Gasoline and Diesel Fuel Update (EIA)

Warroad, MN Babb, MT Havre, MT Port of Morgan, MT Sherwood, ND Pittsburg, NH Buffalo, NY Grand Island, NY Massena, NY Niagara Falls, NY Waddington, NY Sumas, WA Sweetgrass, MT Total to Chile Sabine Pass, LA Total to China Kenai, AK Sabine Pass, LA Total to India Freeport, TX Sabine Pass, LA Total to Japan Cameron, LA Freeport, TX Kenai, AK Port Nikiski, AK Sabine Pass, LA Total to Mexico Douglas, AZ Nogales, AZ Calexico, CA Ogilby Mesa, CA Otay Mesa, CA San Diego, CA Alamo, TX Clint, TX Del Rio, TX Eagle Pass, TX El Paso, TX Hidalgo, TX McAllen, TX Penitas, TX Rio Bravo, TX Roma, TX Total to Portugal Sabine Pass, LA Total to Russia Kenai, AK Total to South Korea Freeport, TX Sabine Pass, LA Total to Spain Cameron, LA Sabine Pass, LA Total to United Kingdom Freeport, TX Sabine Pass, LA LNG Exports from Cameron, LA LNG Exports from Kenai, AK LNG Exports from Freeport, TX LNG Exports from Nogales, AZ LNG Exports from Otay Mesa, CA LNG Exports from Sabine Pass, LA LNG Exports from Sweetgrass, MT Period: Monthly Annual

88

Testing the technical state of gas-transferring unit compressor cases and their repair under the conditions of compressor stations  

Science Journals Connector (OSTI)

Problems related to the use of nondestructive testing methods during engineering diagnostics of the cast cases of compressors that are used in gas-transfer units that operate in gas-main pipelines are considered....

I. I. Kryukov; N. A. Kalinin; S. A. Leont’ev…

2011-02-01T23:59:59.000Z

89

Life Cycle Greenhouse Gas Perspective on Exporting Liquefied Natural Gas from the United States  

Energy.gov (U.S. Department of Energy (DOE))

On May 29, 2014, the Department of Energy’s (DOE) Office of Fossil Energy announced the availability for public review and comment the report Life Cycle Greenhouse Gas Perspective on Exporting...

90

Natural Gas Processing Plants in the United States: 2010 Update / Regional  

Gasoline and Diesel Fuel Update (EIA)

Gulf of Mexico States Gulf of Mexico States Gulf of Mexico States The Gulf of Mexico area, which includes the States of Texas, Louisiana, Mississippi, Alabama, and Florida, has in the past accounted for the majority of natural gas production. Processing plants are especially important in this part of the country because of the amount of NGLs in the natural gas produced and existence of numerous petro-chemical plants seeking that feedstock in this area. Consequently, the States along the Gulf of Mexico are home to the largest number of plants and the most processing capacity in the United States. Natural gas produced in this area of the country is typically rich in NGLs and requires processing before it is pipeline-quality dry natural gas. Offshore natural gas production can contain more than 4 gallons of

91

EIA Data: 2011 United States Oil and Gas Supply | OpenEI  

Open Energy Info (EERE)

Oil and Gas Supply Oil and Gas Supply Dataset Summary Description This dataset is the 2011 United States Oil and Gas Supply, part of the Annual Energy Outlook that highlights changes in the AEO Reference case projections for key energy topics. Source EIA Date Released December 16th, 2010 (3 years ago) Date Updated Unknown Keywords AEO EIA energy gas oil Supply Data application/vnd.ms-excel icon Oil and Gas Supply (xls, 32.3 KiB) Quality Metrics Level of Review Peer Reviewed Comment Temporal and Spatial Coverage Frequency Annually Time Period License License Open Data Commons Public Domain Dedication and Licence (PDDL) Comment http://www.eia.gov/abouteia/copyrights_reuse.cfm Rate this dataset Usefulness of the metadata Average vote Your vote Usefulness of the dataset Average vote Your vote

92

J.K. Spruce power plant, Unit 1, San Antonio, Texas  

SciTech Connect

CPS Energy's J.K. Spruce power plant, Unit 1 was recently recognised by the EUCG Fossil Productivity Committee as the best performer in the large coal plant category over the 2002-2006 evaluation period. The competition was tough, with more than 80 plants in the running, but Unit 1 emerged as the clear winner by earning top points for high plant reliability and very low nonfuel O & M costs. It meets its environmental goals when burning PRB coal in its tangentially fired furnace with recently upgraded low NOx burners, overfire air and a new combustion control system. A baghouse and wet flue gas desulfurization system clean up combustion products. 3 photos.

Peltier, R. [CPS Energy (United States)

2008-10-15T23:59:59.000Z

93

DESULFURIZATION OF COAL MODEL COMPOUNDS AND COAL LIQUIDS  

E-Print Network (OSTI)

Pollutants Associated With Coal Combustion. • E.P.A.Control Guidelines for Coal-Derived Pollutants .Forms of Sulfur in Coal • . . . . Coal Desulfurization

Wrathall, James Anthony

2011-01-01T23:59:59.000Z

94

Natural Gas Processing Plants in the United States: 2010 Update / Appendix  

Gasoline and Diesel Fuel Update (EIA)

Appendix Appendix The preceding report is the most comprehensive report published by the EIA on natural gas processing plants in the United States. The data in the report for the year 2008 were collected on Form EIA-757, Natural Gas Processing Survey Schedule A, which was fielded to EIA respondents in the latter part of 2008 for the first time. This survey was used to collect information on the capacity, status, and operations of natural gas processing plants and to monitor constraints of natural gas processing plants during periods of supply disruption in areas affected by an emergency, such as a hurricane. EIA received authorization to collect information on processing plants from the Office of Management and Budget in early 2008. The form consists of two parts, Schedule A and Schedule B. Schedule A is

95

Generation risk assessment in volatile conditions with wind, hydro, and natural gas units  

Science Journals Connector (OSTI)

This paper studies a generating company (GENCO)’s midterm (a few months to a year) scheduling payoffs and risks in volatile operating conditions. The proposed algorithm considers the integration of intermittent wind units into a GENCO’s generation assets and coordinates the GENCO’s hourly wind generation schedule with that of natural gas (NG) units (with volatile gas prices) and hydro units (with water inflow forecast) for maximizing the GENCO’s payoff. The proposed midterm GENCO model applies market price forecasts to the risk-constrained stochastic price-based unit commitment (PBUC) for calculating the GENCO’s risk in energy and ancillary services markets. The proposed PBUC minimizes the cost of (a) NG contracts, storage, startup and shutdown, (b) startup and shutdown of cascaded hydro units, and (c) penalty for defaulting on the scheduled power delivery. Simulation results show that the diversification of generating assets including bilateral contracts (BCs) could enhance the GENCO’s midterm planning by increasing the expected payoff and decreasing the financial risk.

Cem Sahin; Mohammad Shahidehpour; Ismet Erkmen

2012-01-01T23:59:59.000Z

96

Oil and Gas Wells: Rules Relating to Spacing, Pooling, and Unitization  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Wells: Rules Relating to Spacing, Pooling, and Wells: Rules Relating to Spacing, Pooling, and Unitization (Minnesota) Oil and Gas Wells: Rules Relating to Spacing, Pooling, and Unitization (Minnesota) < Back Eligibility Utility Fed. Government Commercial Agricultural Investor-Owned Utility State/Provincial Govt Industrial Construction Municipal/Public Utility Local Government Residential Installer/Contractor Rural Electric Cooperative Tribal Government Low-Income Residential Schools Retail Supplier Institutional Multi-Family Residential Systems Integrator Fuel Distributor Nonprofit General Public/Consumer Transportation Program Info State Minnesota Program Type Siting and Permitting The Department of Natural Resources is given the authority to create and promulgate regulations related to spacing, pooling, and utilization of oil

97

Desulfurization of lignite using steam and air  

E-Print Network (OSTI)

OF CONTENTS PAGE INTRODUCTION LITERATURE REVIEW Sulfur Removal Using a Fixed Bed Reactor Sulfur Removal Using a Batch Fluidized Bed Reactor . . 9 Continuous Fluidized Bed Reactor Systems for Desulfurization of Coal Clean Coke Process IGT Process... . This study was aimed primarily at producing better metallurgical coke. The ef+ects of various gases on +he sulfur remova1 wo re measured 0 for coal samples at varying t mperatures up to 1273 K The sample was h ated. at a constant ra+ e until the t. st...

Carter, Glenn Allen

2012-06-07T23:59:59.000Z

98

Federal Register Notice for Addendum to Environmental Review Documents Concerning Exports of Natural Gas from the United States  

Energy.gov (U.S. Department of Energy (DOE))

The Office of Fossil Energy (FE) of the Department of Energy (DOE) announces the availability of the Addendum To Environmental Review Documents Concerning Exports Of Natural Gas From The United...

99

A Study of the Causes of the Service Fracture of Turbine Rotor Blade of Compressor Station Gas-Turbine Unit  

Science Journals Connector (OSTI)

On the basis of structural and fractographic the analysis of the fractured surface of working turbine blade of GTK-10-2 gas-turbine unit of compressor station it is established...

A. Ya. Krasovs’kyi; O. E. Gopkalo; I. O. Makovets’ka; O. O. Yanko

2013-07-01T23:59:59.000Z

100

Ultrasound-promoted chemical desulfurization of Illinois coals  

SciTech Connect

The overall objectives of the program were to investigate the use of ultrasound to promote coal desulfurization reactions and to evaluate chemical coal desulfurization schemes under mild conditions through a fundamental understanding of their reaction mechanisms and kinetics. The ultimate goal was to develop an economically feasible mild chemical process to reduce the total sulfur content of Illinois Basin Coals, while retaining their original physical characteristics, such as calorific value and volatile matter content. During the program, potential chemical reactions with coal were surveyed under various ultrasonic irradiation conditions for desulfurization, to formulate preliminary reaction pathways, and to select a few of the more promising chemical processes for more extensive study.

Chao, S.S.

1991-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Corrective action decision document, Second Gas Station, Tonopah test range, Nevada (Corrective Action Unit No. 403)  

SciTech Connect

This Corrective Action Decision Document (CADD) for Second Gas Station (Corrective Action Unit [CAU] No. 403) has been developed for the U.S. Department of Energy`s (DOE) Nevada Environmental Restoration Project to meet the requirements of the Federal Facility Agreement and Consent Order (FFACO) of 1996 as stated in Appendix VI, {open_quotes}Corrective Action Strategy{close_quotes} (FFACO, 1996). The Second Gas Station Corrective Action Site (CAS) No. 03-02-004-0360 is the only CAS in CAU No. 403. The Second Gas Station CAS is located within Area 3 of the Tonopah Test Range (TTR), west of the Main Road at the location of former Underground Storage Tanks (USTs) and their associated fuel dispensary stations. The TTR is approximately 225 kilometers (km) (140 miles [mi]) northwest of Las Vegas, Nevada, by air and approximately 56 km (35 mi) southeast of Tonopah, Nevada, by road. The TTR is bordered on the south, east, and west by the Nellis Air Force Range and on the north by sparsely populated public land administered by the Bureau of Land Management and the U.S. Forest Service. The Second Gas Station CAS was formerly known as the Underground Diesel Tank Site, Sandia Environmental Restoration Site Number 118. The gas station was in use from approximately 1965 to 1980. The USTs were originally thought to be located 11 meters (m) (36 feet [ft]) east of the Old Light Duty Shop, Building 0360, and consisted of one gasoline UST (southern tank) and one diesel UST (northern tank) (DOE/NV, 1996a). The two associated fuel dispensary stations were located northeast (diesel) and southeast (gasoline) of Building 0360 (CAU 423). Presently the site is used as a parking lot, Building 0360 is used for mechanical repairs of vehicles.

NONE

1997-11-01T23:59:59.000Z

102

An approach for assessing engineering risk from shale gas wells in the United States  

Science Journals Connector (OSTI)

Abstract In response to a series of “energy crises” in the 1970s, the United States government began investigating the potential of unconventional, domestic sources of energy to offset imported oil. Hydraulic fracturing applied to vertical tight sand and coal bed methane wells achieved some degree of success during a period of high energy prices in the early 1980s, but shale gas remained largely untapped until the late 1990s with the application of directional drilling, a mature technology adapted from deepwater offshore platforms that allowed horizontal wells to penetrate kilometers of organic-rich shale, and staged hydraulic fracturing, which created high permeability flowpaths from the horizontal wells into a much greater volume of the target formations than previous completion methods. These new engineering techniques opened up vast unconventional natural gas and oil reserves, but also raised concerns about potential environmental impacts. These include short-term and long-term impacts to air and water quality from rig operations, potential migration of gas, fluids and chemicals through the ground, and effects on small watersheds and landscapes from roads, pads and other surface structures. Engineering risk assessment commonly uses integrated assessment models (IAMs), which define sources of risk from features, events and processes. The risk from each system element is assessed using high-fidelity models. Output from these is simplified into reduced-order models, so that a large, integrated site performance assessment can be run using the IAM. The technique has been applied to engineered systems in geologic settings for sequestering carbon dioxide, and it is also applicable to shale gas, albeit with some modifications of the various system elements. Preliminary findings indicate that shale gas well drilling and hydraulic fracturing techniques are generally safe when properly applied. Incident reports recorded by state environmental agencies suggest that human error resulting from the disregard of prescribed practices is the greatest cause of environmental incidents. This can only be addressed through education, regulations and enforcement.

Daniel J. Soeder; Shikha Sharma; Natalie Pekney; Leslie Hopkinson; Robert Dilmore; Barbara Kutchko; Brian Stewart; Kimberly Carter; Alexandra Hakala; Rosemary Capo

2014-01-01T23:59:59.000Z

103

Are fluctuations in natural gas consumption per capita transitory? Evidence from time series and panel unit root tests  

Science Journals Connector (OSTI)

Abstract The stationary properties of natural gas consumption are essential for predicting the impacts of exogenous shocks on energy demand, which can help modeling the energy-growth nexus. Then, this paper proposes to investigate the panel unit root proprieties of natural gas energy consumption of 48 countries over the period of 1971–2010. We apply the Harvey et al. [69] linearity test in order to determine the type of the unit root tests (the Kruse (2010) nonlinear unit root or LM (Lagrange Multiplier) linear unit root tests). Our results show that the stationarity of natural gas consumption cannot be rejected for more than 60% of countries. In order to provide corroborating evidence, we employed not only the first and second generation panel unit root tests, but also the recent LM panel unit root test developed by Im et al. [28]. This test allows for structural breaks both in intercept and slope. The empirical findings support evidence in favor of stationarity of natural gas consumption for all panels. These results announce that any shock to natural gas consumption has a transitory impact for almost all countries implying that energy consumption will turn back to its time trend.

Muhammad Shahbaz; Naceur Khraief; Mantu Kumar Mahalik; Khair Uz Zaman

2014-01-01T23:59:59.000Z

104

United States natural gas markets, contracts and risks: What lessons for the European Union and Asia-Pacific natural gas markets?  

Science Journals Connector (OSTI)

Abstract The article examines the natural gas markets of the United States, the European Union and the Asia-Pacific region and their regulation and contractual structures. The article?s main focus is on the United States natural gas markets. The European Union and Asia-Pacific markets are compared to this more developed market. By comparing the physical and ideological characteristics of, and differences between, the three main international gas markets, the article exposes the limits of regulatory and contractual transplants in this area of law and policy. Each of these markets is unique, which limits the opportunities for modelling certain market institutions on the basis of the more developed markets in the United States. This applies for both the EU and the Asia-Pacific region.

Kim Talus

2014-01-01T23:59:59.000Z

105

Table 1. Summary statistics for natural gas in the United States, 2007-2011  

Gasoline and Diesel Fuel Update (EIA)

Table 1. Summary statistics for natural gas in the United States, 2007-2011 See footnotes at end of table. Number of Wells Producing at End of Year 452,945 476,652 493,100 487,627 514,637 Production (million cubic feet) Gross Withdrawals From Gas Wells R 14,991,891 R 15,134,644 R 14,414,287 R 13,247,498 12,291,070 From Oil Wells R 5,681,871 R 5,609,425 R 5,674,120 R 5,834,703 5,907,919 From Coalbed Wells R 1,999,748 R 2,022,228 R 2,010,171 1,916,762 1,779,055 From Shale Gas Wells 1,990,145 R 2,869,960 R 3,958,315 5,817,122 8,500,983 Total 24,663,656 25,636,257 26,056,893 R 26,816,085 28,479,026 Repressuring 3,662,685 3,638,622 3,522,090 3,431,587 3,365,313 Vented and Flared 143,457 166,909 165,360

106

Desulfurization of Texas lignite using steam and air  

E-Print Network (OSTI)

in Coal Sulfur Removal From Coal By Pyrolysis EXPERIMENTAL METHOD Experimental Apparatus Experimental Procedure Analyses of the Products RESULTS AND DISCUSSION Temperature Effect Upon Desulfurization Pressure Effect Upon Desulfurization... . Treatment Composition Effect Pyrolysis Conditions vs. Addition of' Air V1 V111 ix 10 15 20 24 31 31 35 39 43 45 49 52 53 V11 TABLE OF CONTENTS (Continued) PAGE Pyrolysis Conditions vs. Addition of Steam and Air . . 53 Sulfur Removal...

Stone, Robert Reginald

1981-01-01T23:59:59.000Z

107

Coupled flow and geomechanical analysis for gas production in the Prudhoe Bay Unit L-106 well Unit C gas hydrate deposit in Alaska  

E-Print Network (OSTI)

Hydrate deposits that are desirable gas production targets almost invari- ably involve coarse, unlithified, unconsolidated media (such as sands

Kim, J.

2014-01-01T23:59:59.000Z

108

Natural Gas Processing Plants in the United States: 2010 Update / National  

Gasoline and Diesel Fuel Update (EIA)

National Overview National Overview Processing Plant Utilization Data collected for 2009 show that the States with the highest total processing capacity are among the States with the highest average utilization rates. This is to be expected as most of the plants are located in production areas that have been prolific for many years. In fact, the five States situated along the Gulf of Mexico accounted for nearly 49 percent of total processing volume in 2009. The total utilization rate in the United States averaged 66 percent of total capacity in 2009 (Table 2). Plants in Alaska ran at 86 percent of total capacity during the year, the highest capacity utilization rate in the country. Texas had significant utilization capacity at 71 percent, for an average of 14 Bcf per day of natural gas in 2009. However, a number of

109

Reductions of NO{sub x} emissions on oil and gas firing at Bowline Unit 1  

SciTech Connect

In response to the NYSDEC, Part 227 regulations for the emissions of nitrogen oxides (NO{sub x}), Orange and Rockland Utilities, Inc. (ORU) and Burns & Roe Company (BRC) evaluated the options available to reduce the NO{sub x} emissions at two oil and gas fired units at Bowline Point Generating Station. Replacement of all of the existing burners with new low NO{sub x} burners and possibly overfire air ports presents the most costly method of achieving this goal. Therefore, other methods of NO{sub x} reduction were considered including utilizing some form of off-stoichiometric, burners out of service (BOOS), firing. It was determined that the stringent emission limits could be met utilizing off-stoichiometric firing techniques. New oil gun atomizer tips allowing off-stoichiometric firing with mechanical atomization and swirlers of a new design are replacing the existing atomizers. The new hardware eliminates the problems of opacity while operating with off-stoichiometric firing.

Paschedag, A.E.; Martinsen, R.A.; O`Sullivan, R.C.; Schmidt, D.W. [and others

1996-01-01T23:59:59.000Z

110

Deep Desulfurization of Diesel Oil and Crude Oils by a Newly Isolated Rhodococcus erythropolis Strain  

Science Journals Connector (OSTI)

...released from fossil fuel combustion...acid rain and air pollution (6, 22...5 ml metal solution (16). A...desulfurization of fossil fuels. FIG. 1...enrichments. Water Air Soil Pollut...desulfurization of fossil fuels. Nat. Biotechnol...

Bo Yu; Ping Xu; Quan Shi; Cuiqing Ma

2006-01-01T23:59:59.000Z

111

The effects of potential changes in United States beef production on global grazing systems and greenhouse gas emissions  

E-Print Network (OSTI)

and greenhouse gas emissions Jerome Dumortier1 , Dermot J Hayes2 , Miguel Carriquiry2 , Fengxia Dong3 , Xiaodong in the U.S. causes a net increase in GHG emissions on a global scale. We couple a global agricultural production in the United States. The effects on emissions from agricultural production (i.e., methane

Zhou, Yaoqi

112

Eco Logic International gas-phase chemical reduction process: The thermal desorption unit. Applications analysis report. Final report  

SciTech Connect

The report details the Superfund Innovative Technology Evaluation of the Eco Logic International`s gas-phase chemical reduction process, with an emphasis on their thermal desorption unit. The Eco Logic process employs a high temperature reactor filled with hydrogen as a means to destroy chlorinated organic wastes. The process is designed around a reduction reaction, which reduces the organic wastes into a high-BTU gas product. The thermal desorption unit is designed to work in conjunction with the Eco Logic Reactor system. It is intended to process soils and sludges, desorbing the organic contaminants into a hydrogen gas stream for subsequent treatment and destruction within the Reactor System. The demonstration program was conducted at the Middleground Island Landfill in Bay City, Michigan during October to December, 1992. The report provides details of the test program, summaries of analytical tests conducted on a variety of process streams, process economics, and case study information.

Sudell, G.

1994-09-01T23:59:59.000Z

113

Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2002-2006  

Gasoline and Diesel Fuel Update (EIA)

5 5 Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2002-2006 See footnotes at end of table. Number of Gas and Gas Condensate Wells Producing at End of Year .................................. 387,772 393,327 406,147 R 425,887 448,641 Production (million cubic meters) Gross Withdrawals From Gas Wells .............................................. 503,894 506,356 506,454 R 494,748 508,075 From Oil Wells ................................................ 174,047 176,617 172,292 R 169,476 157,583 Total ................................................................. 677,942 682,973 678,746 R 664,223 665,657 Repressuring .................................................... 97,839 100,462 104,819 R 104,759 92,453 Vented and Flared

114

PRODUCTION OF CONSTRUCTION AGGREGATES FROM FLUE GAS DESULFURIZATION SLUDGE  

SciTech Connect

The three main conclusions of this report are: (1) The pilot plant successfully demonstrated the continuous, fully-integrated, long-term process operation, including the mixing, pelletizing, and curing steps for aggregate production. The curing vessel, which was designed for the pilot plant test, was operated in a mass flow mode and performed well during pilot plant operation. (2) The pilot plant test demonstrated process flexibility. The same equipment was used to produce lightweight, medium-weight, and road aggregates. The only change was the mix formulation. Aggregates were produced from a variety of mix designs and from FGD sludge with solids concentrations between 45.0% and 56.7% and moisture contents between 55.0% and 43.3%. (3) The pilot plant provided operating data and experience to design and cost a commercial plant, which was not part of the cooperative agreement.

M.M. Wu; D.C. McCoy; R.O. Scandrol; M.L. Fenger; J.A. Withum; R.M. Statnick

2000-05-01T23:59:59.000Z

115

Interdependency of electricity and natural gas markets in the United States : a dynamic computational model  

E-Print Network (OSTI)

Due to high storage costs and limited storage availability, natural gas is generally used as a just-in- time resource that needs to be delivered as it is consumed. With the shale gas revolution, coal retirements and ...

Jenkins, Sandra Elizabeth

2014-01-01T23:59:59.000Z

116

Cooled turbine blades in the GTÉ-65 gas turbine power unit  

Science Journals Connector (OSTI)

Experience with the development, study, and manufacturing of cooled blades for the GTÉ-65 high temperature gas turbine is described.

V. V. Rtishchev; V. V. Krivonosova; Yu. M. Sundukov…

2009-11-01T23:59:59.000Z

117

Analysis of Dibenzothiophene Desulfurization in a Recombinant Pseudomonas putida Strain  

Science Journals Connector (OSTI)

...two-step resting-cell process combining sequentially P...bottlenecks that limit the commercialization of BDS have been identified...our understanding of the BDS process at a molecular level, the...influence the desulfurization process rate (2). The activity...

Javier Calzada; María T. Zamarro; Almudena Alcón; Victoria E. Santos; Eduardo Díaz; José L. García; Felix Garcia-Ochoa

2008-12-01T23:59:59.000Z

118

Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2005-2009  

Gasoline and Diesel Fuel Update (EIA)

9 9 Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2005-2009 See footnotes at end of table. Number of Wells Producing at End of Year .... 425,887 440,516 452,945 R 476,652 493,100 Production (million cubic meters) Gross Withdrawals From Gas Wells .............................................. 494,748 509,577 483,238 R 442,265 420,197 From Oil Wells ................................................ 169,476 156,860 164,759 R 162,742 164,611 From Coalbed Wells ....................................... NA NA 50,400 R 56,249 55,990 From Shale Gas Wells .................................... NA NA NA 64,682 95,811 Total ................................................................. 664,223 666,438 698,397 R 725,938 736,609

119

Addendum To Environmental Review Documents Concerning Exports Of Natural Gas From The United States  

Energy.gov (U.S. Department of Energy (DOE))

The purpose of the Addendum is to provide additional information to the public regarding the potential environmental impacts of unconventional natural gas exploration and production activities. DOE...

120

Measurements of methane emissions at natural gas production sites in the United States  

Science Journals Connector (OSTI)

...to a lower pressure destination...atmospheric pressure tank, rather...This lower pressure end point allows more gas to flow...such as a combustor. The nine unloading...population of high emitting wells...America’s Natural Gas Alliance...

David T. Allen; Vincent M. Torres; James Thomas; David W. Sullivan; Matthew Harrison; Al Hendler; Scott C. Herndon; Charles E. Kolb; Matthew P. Fraser; A. Daniel Hill; Brian K. Lamb; Jennifer Miskimins; Robert F. Sawyer; John H. Seinfeld

2013-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

ADSORPTIVE DESULFURIZATION OF LIQUID TRANSPORTATION FUELS VIA NICKEL-BASED ADSORBENTS FOR FUEL CELL APPLICATONS.  

E-Print Network (OSTI)

??The objectives of this work are to compare the adsorptive desulfurization capacity of several different types of nickel-based adsorbents and to identify ways for further… (more)

Clemons, Jennifer

2009-01-01T23:59:59.000Z

122

Oxidative desulfurization of dibenzothiophene with tert-butyl hydro peroxide in a photochemical micro-reactor.  

E-Print Network (OSTI)

??Sulfur content in fuels is an increasingly critical environmental issue. Hydrodesulfurization removes sulfur from hydrocarbons; however, further desulfurization is necessary in fuels. New methods are… (more)

Hebert, Eilleen M.

2007-01-01T23:59:59.000Z

123

Natural Gas Processing Plants in the United States: 2010 Update / National  

Gasoline and Diesel Fuel Update (EIA)

National Overview National Overview Btu Content The natural gas received and transported by the major intrastate and interstate mainline transmission systems must be within a specific energy (Btu) content range. Generally, the acceptable Btu content is 1,035 Btu per cubic foot, with an acceptable deviation of +/-50 Btu. However, when natural gas is extracted, its Btu content can be very different from acceptable pipeline specifications. The Btu content of natural gas extracted varies depending on the presence of water, NGLs, as well as CO2, nitrogen, helium, and others. Significant amounts of NGLs in natural gas is generally associated with higher Btu values. Consistent with this, Btu values reported by plants in Texas and other Gulf of Mexico States are comparatively high (Table 3). On

124

Automatic control systems for gas-turbine units in mini power stations: Testing automation at the stages of design and tuning  

Science Journals Connector (OSTI)

This paper presents the testing automation procedure for automatic control systems of gas-turbine units used as drives in small-size power stations. We substantiate the applicability of mathematical modeling...

B. V. Kavalerov

2013-11-01T23:59:59.000Z

125

Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2004-2008  

Gasoline and Diesel Fuel Update (EIA)

9 9 Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2004-2008 See footnotes at end of table. Number of Wells Producing at End of Year .... 406,147 425,887 440,516 R 452,945 478,562 Production (million cubic meters) Gross Withdrawals From Gas Wells .............................................. 506,454 494,748 509,577 R 483,238 510,019 From Oil Wells ................................................ 172,292 169,476 156,860 R 164,759 165,506 From Coalbed Wells ....................................... NA NA NA 50,400 53,757 Total ................................................................. 678,746 664,223 666,438 R 698,397 729,282 Repressuring .................................................... 104,819 104,759

126

Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2003-2007  

Gasoline and Diesel Fuel Update (EIA)

9 9 Table B1. Summary Statistics for Natural Gas in the United States, Metric Equivalents, 2003-2007 See footnotes at end of table. Number of Wells Producing at End of Year .... 393,327 406,147 425,887 R 440,516 452,768 Production (million cubic meters) Gross Withdrawals From Gas Wells .............................................. 506,356 506,454 494,748 R 509,577 530,629 From Oil Wells ................................................ 176,617 172,292 169,476 R 156,860 165,699 Total ................................................................. 682,973 678,746 664,223 R 666,438 696,328 Repressuring .................................................... 100,462 104,819 104,759 92,453 107,274 Vented and Flared ............................................

127

A Bench Study of Intensive Care Unit Ventilators: New versus Old and Turbine-Based versus Compressed Gas-Based Ventilators  

E-Print Network (OSTI)

. Material: Four turbine- based ventilators and nine conventional servo-valve compressed-gas ventilators were1 A Bench Study of Intensive Care Unit Ventilators: New versus Old and Turbine-Based versus Compressed Gas-Based Ventilators Arnaud W. Thille,1 MD; Aissam Lyazidi,1 Biomed Eng MS; Jean-Christophe M

Paris-Sud XI, Université de

128

Price Discovery in the Natural Gas Markets of the United States and Canada  

E-Print Network (OSTI)

of stored natural gas. Weather variations have an obvious effect on natural gas prices. According to U.S. Department of Energy (U.S. Department of Energy (U.S.DOE), 2003), natural gas demand during winter months is more than 1.5 times daily winter... Deviation Minimum (Date) Maximum (Date) Henry Huba 4.54 2.71 1.03 (12/04/1998) 19.38 (02/25/2003) Chicago 4.55 2.64 1.23 (12/04/1998) 23.00 (02/02/1996) New York 5.36 3.61 1.34 (12/04/1998) 55.00 (01/14/2004) Malin 4.22 2.97 0.93 (02...

Olsen, Kyle

2011-02-22T23:59:59.000Z

129

PROPERTY TABLES AND CHARTS (SI UNITS) Table A1 Molar mass, gas constant, and  

E-Print Network (OSTI)

.0943 Carbon monoxide CO 28.011 0.2968 133 3.50 0.0930 Carbon tetrachloride CCl4 153.82 0.05405 556.4 4.56 0 Table A­20 Ideal-gas properties of carbon dioxide, CO2 Table A­21 Ideal-gas properties of carbon.1355 n-Butane C4H10 58.124 0.1430 425.2 3.80 0.2547 Carbon dioxide CO2 44.01 0.1889 304.2 7.39 0

Kostic, Milivoje M.

130

Recoverable Natural Gas Resource of the United States: Summary of Recent Estimates  

Science Journals Connector (OSTI)

...Summary of Recent Estimates John B. Curtis 1 Scott L. Montgomery...montgomery@prodigy.net John B. Curtis is associate professor...Technology Institute (Holtberg and Cochener, 2001), the National Petroleum...the Potential Gas Committee: John D. Haun, David F. Morehouse...

John B. Curtis; Scott L. Montgomery

131

Natural Gas Processing Plants in the United States: 2010 Update / Regional  

Gasoline and Diesel Fuel Update (EIA)

Regional Analysis Regional Analysis Rocky Mountain States and California Rocky Mountain States and California The Rocky Mountain States, which include all of the States west of the Great Plains and Texas and those east of California, have seen significant natural gas production increases over the last decade. With the development of new production basins, including the San Juan Basin, Powder River Basin, and Green River Basin, natural gas processing capacity in this region has expanded significantly. In 2009, California and Rocky Mountain States accounted for a total of 16.9 Bcf per day or about 22 percent of total U.S. capacity. Since 2004, only California and New Mexico noted a decrease in overall processing capacity, falling by 17 and 12 percent, respectively. Processing capacity in all of the remaining States (Colorado, Montana, New

132

Natural Gas Processing Plants in the United States: 2010 Update / National  

Gasoline and Diesel Fuel Update (EIA)

National Overview National Overview Processing Capacity Processing plants are typically clustered close to major producing areas, with a high number of plants close to the Federal Gulf of Mexico offshore and the Rocky Mountain production areas (Figure 1). In terms of both the number of plants and processing capacity, about half of these plants are concentrated in the States along the Gulf of Mexico. Gulf States have been some of the most prolific natural gas producing areas. U.S. natural gas processing capacity showed a net increase of about 12 percent between 2004 and 2009 (not including the State of Alaska), with the largest increase occurring in Texas, where processing capacity rose by more than 4 Bcf per day. In fact, increases in Texas' processing capacity accounted for 57 percent of the total lower 48 States' capacity increase

133

Greenhouse Gas Emissions for Refrigerant Choices in Room Air Conditioner Units  

Science Journals Connector (OSTI)

In this work, potential replacement refrigerants for window-mounted room air conditioners (RACs) in the U.S. have been evaluated using a greenhouse gas (GHG) emissions analysis. ... De Kleine, R. D.; Keoleian, G. A.; Kelly, J. C.Optimal replacement of residential air conditioning equipment to minimize energy, greenhouse gas emissions, and consumer cost in the US Energy Policy 2011, 39, 3144– 3153 ... Most of the inventory data have been collected from Thailand, except for the upstream of fuel oil and fuel transmission, which have been computed from Greenhouse gases, Regulated Emissions, and Energy use in Transportation version 1.7 and Global Emission Model for Integrated Systems version 4.3. ...

Michael D. Galka; James M. Lownsbury; Paul Blowers

2012-11-08T23:59:59.000Z

134

Natural Gas Processing Plants in the United States: 2010 Update / Table 1  

Gasoline and Diesel Fuel Update (EIA)

1. Natural Gas Processing Plant Capacity by State 1. Natural Gas Processing Plant Capacity by State Natural Gas Processing Capacity (Million Cubic Feet per Day) Number of Natural Gas Plants Average Plant Capacity (Million Cubic Feet per Day) Change Between 2004 and 2009 State 2009 Percent of U.S. Total 2009 Percent of U.S. Total 2004 2009 Capacity (Percent) Number of Plants Texas 19,740 25.5 163 33.1 95 121 24.7 -3 Louisiana 18,535 23.9 60 12.2 271 309 12.3 -1 Wyoming 7,273 9.4 37 7.5 154 197 5.1 -8 Colorado 3,791 4.9 44 8.9 49 86 81.1 1 Oklahoma 3,740 4.8 58 11.8 58 64 8.8 -1 New Mexico 3,022 3.9 24 4.9 137 126 -11.8 -1 Mississippi 2,273 2.9 4 0.8 262 568 44.6 -2 Illinois 2,102 2.7 2 0.4 1101 1,051 -4.6 0 Kansas 1,250 1.6 6 1.2 353 208 -64.6 -4 Alabama 1,248 1.6 12 2.4 87 104 -4.7 -3 Utah 1,185 1.5 12 2.4 61 99 22.2 -4 Michigan 977 1.3 10 2.0 30 98 102.2 -6 California 876 1.1 20 4.1 43 44 -15.5 -4 Arkansas 710 0.9 4 0.8 10 178

135

Economics of residential gas furnaces and water heaters in United States new construction market  

SciTech Connect

New single-family home construction represents a significant and important market for the introduction of energy-efficient gas-fired space heating and water-heating equipment. In the new construction market, the choice of furnace and water-heater type is primarily driven by first cost considerations and the availability of power vent and condensing water heaters. Few analysis have been performed to assess the economic impacts of the different combinations of space and water-heating equipment. Thus, equipment is often installed without taking into consideration the potential economic and energy savings of installing space and water-heating equipment combinations. In this study, we use a life-cycle cost analysis that accounts for uncertainty and variability of the analysis inputs to assess the economic benefits of gas furnace and water-heater design combinations. This study accounts not only for the equipment cost but also for the cost of installing, maintaining, repairing, and operating the equipment over its lifetime. Overall, this study, which is focused on US single-family new construction households that install gas furnaces and storage water heaters, finds that installing a condensing or power-vent water heater together with condensing furnace is the most cost-effective option for the majority of these houses. Furthermore, the findings suggest that the new construction residential market could be a target market for the large-scale introduction of a combination of condensing or power-vent water heaters with condensing furnaces.

Lekov, Alex B.; Franco, Victor H.; Wong-Parodi, Gabrielle; McMahon, James E.; Chan, Peter

2009-05-06T23:59:59.000Z

136

Table B1. Summary statistics for natural gas in the United States, metric equivalents, 2008-2012  

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

6 6 Table B1. Summary statistics for natural gas in the United States, metric equivalents, 2008-2012 See footnotes at end of table. Number of Wells Producing at End of Year 476,652 493,100 487,627 514,637 482,822 Production (million cubic meters) Gross Withdrawals From Gas Wells 428,565 408,167 375,127 348,044 360,663 From Oil Wells 158,841 160,673 165,220 167,294 140,725 From Coalbed Wells 57,263 56,922 54,277 50,377 43,591 From Shale Gas Wells 81,268 112,087 164,723 240,721 291,566 Total 725,938 737,849 759,347 806,436 836,545 Repressuring 103,034 99,734 97,172 95,295 92,304 Vented and Flared 4,726 4,682 4,699 5,931 6,027 Nonhydrocarbon Gases Removed 20,351 20,431 23,693 24,577 21,573

137

FLNG compared to LNG carriers - Requirements and recommendations for LNG production facilities and re-gas units.  

E-Print Network (OSTI)

??An increasing price and demand for natural gas has made it possible to explore remote gas fields. Traditional offshore production platforms for natural gas have… (more)

Aronsson, Erik

2012-01-01T23:59:59.000Z

138

High-temperature desulfurization of gasifier effluents with rare earth and rare earth/transition metal oxides  

SciTech Connect

We have improved the application of mixed rare-earth oxides (REOs) as hot gas desulfurization adsorbents by impregnating them on stable high surface area supports and by the inclusion of certain transition metal oxides. We report comparative desulfurization experiments at high temperature (900 K) using a synthetic biomass gasifier effluent containing 0.1 vol % H{sub 2}S, along with H{sub 2}, CO{sub 2}, and water. More complex REO sorbents outperform the simpler CeO{sub 2}/La{sub 2}O{sub 3} mixtures, in some cases significantly. Supporting REOs on Al{sub 2}O{sub 3} (?20 wt % REO) or ZrO{sub 2} actually increased the sulfur capacities found after several cycles on a total weight basis. Another major increase in sulfur capacity took place when MnO{sub x} or FeO{sub x} is incorporated. Apparently most of the Mn or Fe is dispersed on or near the surface of the mixed REOs because the capacities with REOs greatly exceeded those of Al{sub 2}O{sub 3}-supported MnO{sub x} or FeO{sub x} alone at these conditions. In contrast, incorporating Cu has little effect on sulfur adsorption capacities. Both the REO and transition metal/REO adsorbents could be regenerated completely using air for at least five repetitive cycles.

Dooley, Kerry M.; Kalakota, Vikram; Adusumilli, Sumana

2011-01-01T23:59:59.000Z

139

Natural Gas Processing Plants in the United States: 2010 Update / Regional  

Gasoline and Diesel Fuel Update (EIA)

Midwestern and Eastern States Midwestern and Eastern States Midwestern and Eastern States Midwestern and Eastern States combined accounted for about 13 percent of total U.S. processing capacity in 2009, accounting for the smallest portion of any region in the lower 48 States. The combined processing capacity in these States more than doubled, although a few of the States saw decreased capacity compared with 2004. Processing capacity in Illinois, Kansas, North Dakota, and Pennsylvania fell since 2004, with the highest decrease occurring in Kansas, which saw a 65 percent drop in processing capacity. At the same time, the number of plants in Kansas decreased by four. The decrease was likely the result of falling natural gas proved reserves, which decreased in this State between 1995 and 2005. While the proved reserves have

140

Natural Gas Processing Plants in the United States: 2010 Update / Regional  

Gasoline and Diesel Fuel Update (EIA)

Regional Analysis Regional Analysis Alaska Alaska The State of Alaska had the third-largest processing capacity, trailing only Texas and Louisiana. While much of the natural gas processed in Alaska does not enter any transmission system and is instead re-injected into reservoirs, its processing capability is nonetheless significant. At 9.5 Bcf per day of processing capacity, the State of Alaska accounted for about 12 percent of total U.S. capacity. As of 2009, there were a total of 4 plants in the State, with the largest one reporting a capacity of 8.5 Bcf per day. Average plant size of 2.4 Bcf per day far exceeded any other State, with Illinois noting the next largest average plant size of 1.1 Bcf per day. In addition to the significant processing total capacity, plants in

Note: This page contains sample records for the topic "gas desulfurization units" 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

Operator Trainer System for the Petrobras P-26 Semi-Submersible Oil and Gas Production Unit  

Science Journals Connector (OSTI)

Abstract Operator trainer systems aim to improve operator performance, by simulating scenarios such as emergency conditions, thus reducing accidents and increasing processes economical results. In this paper, we present PETROBRAS' Oil & Gas Production Process and Utilities Simulator Environment called AMBTREI (Training Environment) that mimics the actual Control Room of an E&P semi-submersible Platform at a very high fidelity level. This training environment was created utilizing Soteica's Operator Training System solution (S-OTS). The dynamic process model will be described as well as the Process Control Interface that was implemented. The software used will be explained in detail and the conclusions that have been reached in almost 2 years of use will be presented.

A.C. Pereira; A. Riera; G. Padilla; E. Musulin; N.J. Nakamura

2009-01-01T23:59:59.000Z

142

Development of a micro-cogeneration laboratory and testing of a natural gas CHP unit based on PEM fuel cells  

Science Journals Connector (OSTI)

Abstract This work discusses the design and the development of a Laboratory of Micro-Cogeneration (LMC) at Politecnico di Milano. The LMC laboratory is a unique structure devoted to small-scale power generation, with the main goals of testing and improving the performance of systems that produce or utilize electric and thermal (hot and/or cold) power in a very general sense, spanning from combined heat and power (CHP) units to heaters, from absorption chillers to heat pumps, but also able to perform tests on fuel processors and electrolyzers. The laboratory features a supply of natural gas as well as H2 and O2 from a high pressure electrolyzer and of CO, CO2 and N2 from bottles, permitting to carry out experiments with simulated synthesis fuels. The maximum allowable electrical power produced, exported to the grid or to an electronic loadbank, or consumed by the system under test is 100 kW; maximum allowable thermal power is roughly 200 kW with variable temperature water circuits (from chilled water up to a 150 °C at 8 bar superheated water loop). This work outlines also the instruments used for on-line recording of thermodynamic properties, emissions and power, aiming at monitoring and reconstructing mass and energy balances. One of the first experimental campaign has been carried out on a CHP system based on polymer electrolyte membrane fuel cells (PEM), a promising candidate for distributed CHP thanks to low pollutant emissions and good efficiency, rapid startup and flexibility, although affected by a rather complex fuel processing section to provide the appropriate fuel to the PEM. This work presents the experimental analysis of a 20 kW prototype PEM CHP system complete of natural gas processor. The prototype is operated at LMC to characterize the processing section and the thermodynamic performances of the overall system. Despite its non-optimized layout, the unit has shown encouraging total efficiency (76%) and primary energy saving index (6%).

S. Campanari; G. Valenti; E. Macchi; G. Lozza; N. Ravidà

2014-01-01T23:59:59.000Z

143

Natural Gas Processing Plants in the United States: 2010 Update / Table 2  

Gasoline and Diesel Fuel Update (EIA)

2. Average Annual Flows and Utilization Rates for Processing Plants in the United States 2. Average Annual Flows and Utilization Rates for Processing Plants in the United States Average Annual Flows (Million Cubic Feet per Day) Minimum Plant Utilization Rate Maximum Plant Utilization Rate Average Utilization Rate (Percent) 2008 Percent of U.S. Total Texas 14,020 27.3 3 100 71 Louisiana 10,462 20.4 3 100 56 Alaska 8,105 15.8 77 100 86 Wyoming 4,462 8.7 21 100 61 Colorado 2,934 5.7 15 100 77 Oklahoma 2,789 5.4 12 100 75 New Mexico 2,221 4.3 17 95 73 Illinois 1,601 3.1 35 76 76 Kansas 852 1.7 51 84 68 Alabama 746 1.5 32 80 60 Utah 728 1.4 22 100 61 Mississippi 688 1.3 29 67 30 California 557 1.1 2 100 64 West Virginia 382 0.7 70 91 82 Kentucky 217 0.4 40 92 75 Michigan 182 0.4 5 100 19 North Dakota 158 0.3 33 94 80 Montana 89 0.2 27 88 54 Pennsylvania 36 0.1 43 89 70 Arkansas 27 0.1 3 90 4 Florida 20 0.0 22 22 22 Tennessee 16 0.0 64 64 64 TOTAL U.S. 51,289 100.0 2 100 66 Note: Average utilization rates are based on 2008 flows and 2009 capacity,

144

A multi-level simulation platform of natural gas internal reforming solid oxide fuel cell–gas turbine hybrid generation system – Part II. Balancing units model library and system simulation  

Science Journals Connector (OSTI)

Following our integrated hierarchical modeling framework of natural gas internal reforming solid oxide fuel cell (IRSOFC), this paper firstly introduces the model libraries of main balancing units, including some state-of-the-art achievements and our specific work. Based on gPROMS programming code, flexible configuration and modular design are fully realized by specifying graphically all unit models in each level. Via comparison with the steady-state experimental data of Siemens–Westinghouse demonstration system, the in-house multi-level SOFC–gas turbine (GT) simulation platform is validated to be more accurate than the advanced power system analysis tool (APSAT). Moreover, some units of the demonstration system are designed reversely for analysis of a typically part-load transient process. The framework of distributed and dynamic modeling in most of units is significant for the development of control strategies in the future.

Cheng Bao; Ningsheng Cai; Eric Croiset

2011-01-01T23:59:59.000Z

145

Microbial Desulfurization of Gasoline in a Mycobacterium goodii X7B Immobilized-Cell System  

Science Journals Connector (OSTI)

...oxides released from fossil fuel combustion contribute to acid rain and air pollution (11, 24). With the...the desulfurization of fossil fuels. MATERIALS AND METHODS...with a sodium chloride solution (0.85%), and resuspended...

Fuli Li; Ping Xu; Jinhui Feng; Ling Meng; Yuan Zheng; Lailong Luo; Cuiqing Ma

2005-01-01T23:59:59.000Z

146

THE USE OF FERRIC SULFATE - ACID MEDIA FOR THE DESULFURIZATION OF MODEL COMPOUNDS OF COAL  

E-Print Network (OSTI)

of Cleaning Processes to U.S. Coals • . 23 B. Purpose . C.Low Temp. Processes for Coal Desulfurization", M.S. Thesis,R.A. , "Chem. Desulf. of Coal", AIChE Sym:p. Series, Meyers,

Clary, Lloyd R.

2014-01-01T23:59:59.000Z

147

User converts gas boiler to fluidized bed to save $1. 5M  

SciTech Connect

Retrofitting a fluidized bed combustion (FBC) system may allow Clayton Foods Inc. to reduce its annual fuel bill by $1.5 million when the system comes on line in 1986. The system will burn low-grade, high-sulfur coal instead of natural gas, and should pay back the $4.1 million investment in under five years. The dual bed design separates the chemical processes of combustion and desulfurization into two chambers, which allows smaller-sized combustors that achieve high efficiencies in less time than conventional, single-bed fluidized bed boilers. Possible limitations prevent other manufacturers from making the dual-bed system. The Wormser unit is the only retrofit application of this technology in an industrial setting.

Springer, N.

1985-07-29T23:59:59.000Z

148

Enhanced durability of high-temperature desulfurization sorbents for moving-bed applications. Option 2 Program: Development and testing of zinc titanate sorbents  

SciTech Connect

One of the most advantageous configurations of the integrated gasification combined cycle (IGCC) power system is coupling it with a hot gas cleanup for the more efficient production of electric power in an environmentally acceptable manner. In conventional gasification cleanup systems, closely heat exchangers are necessary to cool down the fuel gases for cleaning, sometimes as low as 200--300{degree}F, and to reheat the gases prior to injection into the turbine. The result is significant losses in efficiency for the overall power cycle. High-temperature coal gas cleanup in the IGCC system can be operated near 1000{degree}F or higher, i.e., at conditions compatible with the gasifier and turbine components, resulting is a more efficient overall system. GE is developing a moving-bed, high-temperature desulfurization system for IGCC power systems in which mixed-metal oxides are currently being used as desulfurization sorbents. The objective of this contract is to identify and test fabrication methods and sorbent chemical compositions that enhance the long-term chemical reactivity and mechanical durability of zinc ferrite and other novel sorbents for moving-bed, high-temperature desulfurization of coal-derived gases. Zinc ferrite was studied under the base program of this contract. In the next phase of this program novel sorbents, particularly zinc titanate-based sorbents, are being studied under the remaining optional programs. This topical report summarizes only the work performed under the Option 2 program. In the course of carrying out the program, more than 25 zinc titanate formulations have been prepared and characterized to identify formulations exhibiting enhanced properties over the baseline zinc titanate formulation selected by the US Department of Energy.

Ayala, R.E.

1993-04-01T23:59:59.000Z

149

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

SciTech Connect

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

150

Updated greenhouse gas and criteria air pollutant emission factors and their probability distribution functions for electricity generating units  

SciTech Connect

Greenhouse gas (CO{sub 2}, CH{sub 4} and N{sub 2}O, hereinafter GHG) and criteria air pollutant (CO, NO{sub x}, VOC, PM{sub 10}, PM{sub 2.5} and SO{sub x}, hereinafter CAP) emission factors for various types of power plants burning various fuels with different technologies are important upstream parameters for estimating life-cycle emissions associated with alternative vehicle/fuel systems in the transportation sector, especially electric vehicles. The emission factors are typically expressed in grams of GHG or CAP per kWh of electricity generated by a specific power generation technology. This document describes our approach for updating and expanding GHG and CAP emission factors in the GREET (Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation) model developed at Argonne National Laboratory (see Wang 1999 and the GREET website at http://greet.es.anl.gov/main) for various power generation technologies. These GHG and CAP emissions are used to estimate the impact of electricity use by stationary and transportation applications on their fuel-cycle emissions. The electricity generation mixes and the fuel shares attributable to various combustion technologies at the national, regional and state levels are also updated in this document. The energy conversion efficiencies of electric generating units (EGUs) by fuel type and combustion technology are calculated on the basis of the lower heating values of each fuel, to be consistent with the basis used in GREET for transportation fuels. On the basis of the updated GHG and CAP emission factors and energy efficiencies of EGUs, the probability distribution functions (PDFs), which are functions that describe the relative likelihood for the emission factors and energy efficiencies as random variables to take on a given value by the integral of their own probability distributions, are updated using best-fit statistical curves to characterize the uncertainties associated with GHG and CAP emissions in life-cycle modeling with GREET.

Cai, H.; Wang, M.; Elgowainy, A.; Han, J. (Energy Systems)

2012-07-06T23:59:59.000Z

151

Enhancing the use of coals by gas reburning-sorbent injection: Volume 4 -- Gas reburning-sorbent injection at Lakeside Unit 7, City Water, Light and Power, Springfield, Illinois. Final report  

SciTech Connect

A demonstration of Gas Reburning-Sorbent Injection (GR-SI) has been completed at a cyclone-fired utility boiler. The Energy and Environmental Research Corporation (EER) has designed, retrofitted and tested a GR-SI system at City Water Light and Power`s 33 MWe Lakeside Station Unit 7. The program goals of 60% NO{sub x} emissions reduction and 50% SO{sub 2} emissions reduction were exceeded over the long-term testing period; the NO{sub x} reduction averaged 63% and the SO{sub 2} reduction averaged 58%. These were achieved with an average gas heat input of 22% and a calcium (sorbent) to sulfur (coal) molar ratio of 1.8. GR-SI resulted in a reduction in thermal efficiency of approximately 1% at full load due to firing natural gas which forms more moisture in flue gas than coal and also results in a slight increase in air heater exit gas temperature. Minor impacts on other areas of unit performance were measured and are detailed in this report. The project at Lakeside was carried out in three phases, in which EER designed the GR-SI system (Phase 1), completed construction and start-up activities (Phase 2), and evaluated its performance with both short parametric tests and a long-term demonstration (Phase 3). This report contains design and technical performance data; the economics data for all sites are presented in Volume 5.

NONE

1996-03-01T23:59:59.000Z

152

Reducing greenhouse gas emissions from deforestation : the United Nations Framework Convention on Climate Change and policy-making in Panama.  

E-Print Network (OSTI)

??The Framework Convention on Climate Change has yet to deal with tropical deforestation although it represents an important source of greenhouse gas emissions. In December… (more)

Guay, Bruno.

2007-01-01T23:59:59.000Z

153

,"Price of U.S. Liquefied Natural Gas Imports From The United Arab Emirates (Dollars per Thousand Cubic Feet)"  

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

The United Arab Emirates (Dollars per Thousand Cubic Feet)" The United Arab Emirates (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From The United Arab Emirates (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103ua3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103ua3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

154

Addendum to the Closure Report for Corrective Action Unit 403: Second Gas Station, Tonopah Test Range, Nevada, Revision 0  

SciTech Connect

This document constitutes an addendum to the Closure Report for Corrective Action Unit 403: Second Gas Station, Tonopah Test Range, Nevada, September 1998 as described in the document Supplemental Investigation Report for FFACO Use Restrictions, Nevada Test Site, Nevada (SIR) dated November 2008. The SIR document was approved by NDEP on December 5, 2008. The approval of the SIR document constituted approval of each of the recommended UR removals. In conformance with the SIR document, this addendum consists of: • This page that refers the reader to the SIR document for additional information • The cover, title, and signature pages of the SIR document • The NDEP approval letter • The corresponding section of the SIR document This addendum provides the documentation justifying the cancellation of the UR for CAS 03-02-004-0360, Underground Storage Tanks. This UR was established as part of a Federal Facility Agreement and Consent Order (FFACO) corrective action and is based on the presence of contaminants at concentrations greater than the action levels established at the time of the initial investigation (FFACO, 1996). Since this UR was established, practices and procedures relating to the implementation of risk-based corrective actions (RBCA) have changed. Therefore, this UR was reevaluated against the current RBCA criteria as defined in the Industrial Sites Project Establishment of Final Action Levels (NNSA/NSO, 2006). This re-evaluation consisted of comparing the original data (used to define the need for the UR) to risk-based final action levels (FALs) developed using the current Industrial Sites RBCA process. The re-evaluation resulted in a recommendation to remove the UR because contamination is not present at the site above the risk-based FALs. Requirements for inspecting and maintaining this UR will be canceled, and the postings and signage at this site will be removed. Fencing and posting may be present at this site that are unrelated to the FFACO UR such as for radiological control purposes as required by the NV/YMP Radiological Control Manual (NNSA/NSO, 2004). This modification will not affect or modify any non-FFACO requirements for fencing, posting, or monitoring at this site.

Grant Evenson

2009-05-01T23:59:59.000Z

155

Apparatus and method for the desulfurization of petroleum by bacteria  

DOE Patents (OSTI)

A method is described for treating petroleum with anaerobic microorganisms acting as biocatalysts that can remove sulfur atoms from hydrocarbon molecules, under anaerobic conditions, and then convert the sulfur atoms to hydrogen sulfide. The microorganisms utilized are from the family known as the ``Sulfate Reducing Bacteria``. These bacteria generate metabolic energy from the oxidation of organic compounds, but use oxidized forms of sulfur as an electron acceptor. Because the biocatalyst is present in the form of bacteria in an aqueous suspension, whereas the reacting substrate consists of hydrocarbon molecules in an organic phase, the actual desulfurization reaction takes place at the aqueous-organic interphase. To ensure adequate interfacial contacting and mass transfer, a biphasic electrostatic bioreactor system is utilized. The bioreactor is utilized to disperse and recoalesce a biocatalyst contained in the aqueous liquid phase into the organic liquid phase containing the sulfur. High-intensity electrical fields rupture the aqueous drops into a plurality of microdroplets and induce continuous coalescence and redispersion as the microdroplets travel through the organic phase, thus increasing surface area. As the aqueous microdroplets progress through the organic phase, the biocatalyst then reacts with the sulfur to produce hydrogen sulfide which is then removed from the bioreactor. The organic liquid, now free of the sulfur, is ready for immediate use or further processing. 5 figs.

Lizama, H.M.; Scott, T.C.; Scott, C.D.

1995-10-17T23:59:59.000Z

156

Evaluation of sulfur-reducing microorganisms for organic desulfurization. [Pyrococcus furiosus  

SciTech Connect

Because of substantial portion of the sulfur in Illinois coal is organic, microbial desulfurization of sulfidic and thiophenic functionalities could hold great potential for completing pyritic sulfur removal. We are testing the hypothesis that organic sulfur can be reductively removed as H{sub 2}S through the activities of anaerobic microorganisms. Our objectives for this year include the following: (1) To obtain cultures that will reductively desulfurize thiophenic model compounds. In addition to crude oil enrichments begun last year, we sampled municipal sewage sludge. (2) To continue to work toward optimizing the activity of the DBDS-reducing cultures obtained during the previous year. (3) To expand coal desulfurization work to include other coals including Illinois Basin Coal 101 and a North Dakota lignite, which might be more susceptible to the dibenzyldisulfide reducing cultures due to its lower rank. (4) To address the problem of sulfide sorption, by investigating the sorption capacity of coals in addition to Illinois Basin Coal 108.

Miller, K.W.

1991-01-01T23:59:59.000Z

157

Reforming Brazil?s offshore oil and gas safety regulatory framework: Lessons from Norway, the United Kingdom and the United States  

Science Journals Connector (OSTI)

Abstract We propose reforming the Brazilian regulatory safety framework (BRSF) for offshore oil and gas production and drilling operations. Brazil has emerged as a leading offshore producer with extensive proven reserves yet to be exploited. However, the BRSF has not been updated since 2007, and there are now major concerns about the industry?s safety, particularly after the BP Deepwater Horizon accident, along with the technical challenges due to extreme conditions under which Brazil?s resources are located. Drawing on experiences from three leading offshore oil and gas producers (Norway, the UK, and the US), we recommend the adoption of three best practices: the UK?s ‘safety case’ approach (where operators are expected to provide convincing and valid arguments that a system is sufficiently safe for a given application in a specific environment), Norway?s ‘barrier management’ (evidence that there are at least two tested and independent barriers to avoid accidents) and greater investment in safety research and development, as suggested by the US?s National Commission on the BP Deepwater Horizon Oil Spill and Offshore Drilling. We discuss implications for policy reform and how best practices can be applied within the Brazilian context.

Pietro A.S. Mendes; Jeremy Hall; Stelvia Matos; Bruno Silvestre

2014-01-01T23:59:59.000Z

158

The effects of gas-to-oil rate in ultra low sulfur diesel hydrotreating  

Science Journals Connector (OSTI)

Hydrotreating has become a critical refining process as fuel sulfur specifications are tightened around the world. Recently, refiners in the United States have been learning how to optimize the performance of ultra low sulfur diesel (ulsd) hydrotreaters. The gas-to-oil feed rate ratio is known to be an important variable in this respect. It is well known that the gas-to-oil rate must be kept high enough to maintain the desired hydrogen partial pressure through the hydrotreating reactor, and to minimize the inhibiting effect of hydrogen sulfide. A lesser-known effect is the effect of gas-to-oil rate on the vapor–liquid equilibrium in the reactor. Changing the gas-to-oil rate alters the distribution of reactants between vapor and liquid in a way that changes the relative reaction rates of different sulfur compounds. This paper presents some pilot plant data and analysis showing this effect of phase equilibrium in deep diesel desulfurization. The effect can be modeled using the Frye–Mosby equation, which accounts for the effects of feed vaporization and phase equilibrium on the reaction rates of individual sulfur compounds in a trickle bed hydrotreater.

George Hoekstra

2007-01-01T23:59:59.000Z

159

Building commissioning: a golden opportunity for reducing energy costs and greenhouse gas emissions in the United States  

Science Journals Connector (OSTI)

Commissioning is arguably the single most cost-effective strategy for reducing energy, costs, and greenhouse gas emissions in buildings today. Although commissioning has earned increased recognition in recent ...

Evan Mills

2011-05-01T23:59:59.000Z

160

Real-World Greenhouse Gas Emissions from a MY2010 Diesel Truck Traveling Across the Continental United States  

Energy.gov (U.S. Department of Energy (DOE))

Data analysis from this study will provide insight into real-world performance of current emissions reduction devices, under various operating conditions, and with respect to greenhouse gas emissions.

Note: This page contains sample records for the topic "gas desulfurization units" 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

Shale Gas Glossary | Department of Energy  

Office of Environmental Management (EM)

Glossary Shale Gas Glossary Shale Gas Glossary More Documents & Publications Natural Gas from Shale: Questions and Answers Modern Shale Gas Development in the United States: A...

162

Ultrasound-promoted chemical desulfurization of Illinois coals. Final technical report, September 1, 1990--August 31, 1991  

SciTech Connect

The overall objectives of the program were to investigate the use of ultrasound to promote coal desulfurization reactions and to evaluate chemical coal desulfurization schemes under mild conditions through a fundamental understanding of their reaction mechanisms and kinetics. The ultimate goal was to develop an economically feasible mild chemical process to reduce the total sulfur content of Illinois Basin Coals, while retaining their original physical characteristics, such as calorific value and volatile matter content. During the program, potential chemical reactions with coal were surveyed under various ultrasonic irradiation conditions for desulfurization, to formulate preliminary reaction pathways, and to select a few of the more promising chemical processes for more extensive study.

Chao, S.S.

1991-12-31T23:59:59.000Z

163

Desulfurization of Liquid Fuel via Fractional Evaporation and Subsequent Hydrodesulfurization Upstream a Fuel Cell System  

Science Journals Connector (OSTI)

The polymer electrolyte membrane fuel cell (PEMFC) and the solid oxide fuel cell (SOFC) are favored for application in the foreseeable future. ... For fuel cells to be fuelled with liquid fuels as per Figure 1, an upstream desulfurization step is mandatory. ... fuel?recovered ...

Markus Brune; Rainer Reimert

2005-08-17T23:59:59.000Z

164

Novel Nanoscale Catalysts and Desulfurizers for Aviation Fuels Martin Duran* and Abdul-Majeed Azad  

E-Print Network (OSTI)

reforming catalysts for jet fuel", The Ohio Fuel Cell Symposium of the Ohio Fuel Cell Coalition, May 23Novel Nanoscale Catalysts and Desulfurizers for Aviation Fuels Martin Duran* and Abdul-Majeed Azad) to hydrogen through steam reforming poses a challenge since these fuels contain sulfur up to about 1000 ppm

Azad, Abdul-Majeed

165

Studying the advisability of using gas-turbine unit waste gases for heating feed water in a steam turbine installation with a type T-110/120-12.8 turbine  

Science Journals Connector (OSTI)

Results of calculation studying of a possibility of topping of a steam-turbine unit (STU) with a type T-110/120-12.8 turbine of the Urals Turbine Works (UTZ) by a gas-turbine unit (GTU) of 25-MW capacity the wast...

A. D. Trukhnii; G. D. Barinberg; Yu. A. Rusetskii

2006-02-01T23:59:59.000Z

166

Computational and experimental test of self starting regimes for the in-house needs of the PGU-450 steam-gas unit at the Kaliningrad TÉTs-2 Heating and Power Plant during supply disruptions  

Science Journals Connector (OSTI)

The major stages of a computational test of the self starting regimes for the in-house needs of unit No. 1 of the 450 MW steam-gas unit at the Kaliningrad TÉTs-2 Heating and Electric Power Plant during supply ...

S. N. Sakharov; V. A. Kuz’michev

2008-05-01T23:59:59.000Z

167

Flue-gas sulfur-recovery plant for a multifuel boiler  

SciTech Connect

In October 1991, a Finnish fluting mill brought on stream a flue-gas desulfurization plant with an SO{sub 2} reduction capacity of 99%. The desulfurization plant enabled the mill to discontinue the use of its sulfur burner for SO{sub 2} production. The required makeup sulfur is now obtained in the form of sulfuric acid used by the acetic acid plant, which operates in conjunction with the evaporating plant. The mill`s sulfur consumption has decreased by about 6,000 tons/year (13.2 million lb/year) because of sulfur recycling.

Miettunen, J. [Tampella Power Inc., Tampere (Finland); Aitlahti, S. [Savon Sellu Oy, Kuopio (Finland)

1993-12-01T23:59:59.000Z

168

Demonstration of natural gas reburn for NO{sub x} emissions reduction at Ohio Edison Company`s cyclone-fired Niles Plant Unit Number 1  

SciTech Connect

Electric utility power plants account for about one-third of the NO{sub x} and two-thirds of the SO{sub 2} emissions in the US cyclone-fired boilers, while representing about 9% of the US coal-fired generating capacity, emit about 14% of the NO{sub x} produced by coal-fired utility boilers. Given this background, the Environmental Protection Agency, the Gas Research Institute, the Electric Power Research Institute, the Pittsburgh Energy Technology Center, and the Ohio Coal Development Office sponsored a program led by ABB Combustion Engineering, Inc. (ABB-CE) to demonstrate reburning on a cyclone-fired boiler. Ohio Edison provided Unit No. 1 at their Niles Station for the reburn demonstration along with financial assistance. The Niles Unit No. 1 reburn system was started up in September 1990. This reburn program was the first full-scale reburn system demonstration in the US. This report describes work performed during the program. The work included a review of reburn technology, aerodynamic flow model testing of reburn system design concepts, design and construction of the reburn system, parametric performance testing, long-term load dispatch testing, and boiler tube wall thickness monitoring. The report also contains a description of the Niles No. 1 host unit, a discussion of conclusions and recommendations derived from the program, tabulation of data from parametric and long-term tests, and appendices which contain additional tabulated test results.

Borio, R.W.; Lewis, R.D.; Koucky, R.W. [ABB Power Plant Labs., Windsor, CT (United States)] [ABB Power Plant Labs., Windsor, CT (United States); Lookman, A.A. [Energy Systems Associates, Pittsburgh, PA (United States)] [Energy Systems Associates, Pittsburgh, PA (United States); Manos, M.G.; Corfman, D.W.; Waddingham, A.L. [Ohio Edison, Akron, OH (United States)] [Ohio Edison, Akron, OH (United States); Johnson, S.A. [Quinapoxet Engineering Solutions, Inc., Windham, NH (United States)] [Quinapoxet Engineering Solutions, Inc., Windham, NH (United States)

1996-04-01T23:59:59.000Z

169

Desulfurization of coal: enhanced selectivity using phase transfer catalysts. Quarterly report, March 1 - May 31, 1996  

SciTech Connect

Due to environmental problems related to the combustion of high sulfur Illinois coal, there continues to be interest in the development in viable pre-combustion desulfurization processes. Recent studies by the authors have obtained very good sulfur removals but the reagents that are used are too expensive. Use of cheaper reagents leads to a loss of desired coal properties. This study investigated the application phase transfer catalysts to the selective oxidation of sulfur in coal using air and oxygen as oxidants. The phase transfer catalyst is expected to function as a selectivity moderator by permitting the use of milder reaction conditions that otherwise necessary. This would enhance the sulfur selectivity and help retain the heating value of the coal. The use of certain coal combustion wastes for desulfurization, and the application of cerium (IV) catalyzed air oxidation for selective sulfur oxidation are also being studied. If successful, this project could lead to the rapid development of a commercially viable desulfurization process. This would significantly improve the marketability of Illinois coal.

Palmer, S.R.; Hippo, E.J. [Southern Illinois Univ., Carbondale, IL (United States)

1996-12-31T23:59:59.000Z

170

Integrating desulfurization with CO{sub 2}-capture in chemical-looping combustion  

SciTech Connect

Chemical looping combustion (CLC) is an emerging technology for clean combustion. We have previously demonstrated that the embedding of metal nanoparticles into a nanostructured ceramic matrix can result in unusually active and sinter-resistant nanocomposite oxygen carrier materials for CLC which maintain high reactivity and high-temperature stability even when sulfur contaminated fuels are used in CLC. Here, we propose a novel process scheme for in situ desulfurization of syngas with simultaneous CO{sub 2}-capture in chemical looping combustion by using these robust nanocomposite oxygen carriers simultaneously as sulfur-capture materials. We found that a nanocomposite Cu-BHA carrier can indeed strongly reduce the H{sub 2}S concentration in the fuel reactor effluent. However, during the process the support matrix is also sulfidized and takes part in the redox process of CLC. This results in SO{sub 2} production during the reduction of the oxygen carrier and thus limits the degree of desulfurization attainable with this kind of carrier. Nevertheless, the results suggest that simultaneous desulfurization and CO{sub 2} capture in CLC is feasible with Cu as oxygen carrier as long as appropriate carrier support materials are chosen, and could result in a novel, strongly intensified process for low-emission, high efficiency combustion of sulfur contaminated fuel streams.

Solunke, Rahul; Veser, Goetz

2011-02-01T23:59:59.000Z

171

Compliance with revised acid rain monitoring requirements for gas and oil fired units: Appendix D and E of Part 75  

SciTech Connect

EPA`s CEM rule (40 CFR Part 75) implements the monitoring provisions of Title IV of the Clean Air Act Amendments of 1990. In most cases Part 75 requires utilities to monitor sulfur dioxide (SO{sub 2}), nitrogen oxide (NO{sub x}) and carbon dioxide emissions (CO{sub 2}), and volumetric flow and opacity using Continuous Emissions Monitoring Systems (CEMS). Appendix D and E of 40 CFR Part 75 provide alternatives to using Continuous Emissions Monitoring Systems (CEMS) to comply with the monitoring requirements of Title IV of the Clean Air Act. EPA is considering a number of changes to Part 75, including significant changes to Appendix D and E. Part 75 was originally promulgated on January 11, 1993. Due to both experience gained in the implementation of Phase 1 and the early implementation of Phase 2 and petitions filed by several groups, EPA has prepared a number of changes to Part 75. This paper discusses what EPA anticipates these changes will be and how EPA anticipates that these changes will affect the regulated community. In addition, it discusses EPA`s expectations for certification applications for units using Appendix D and E.

Sheppard, M.; Culligan, K. [EPA, Washington, DC (United States). Acid Rain Div.

1995-12-31T23:59:59.000Z

172

Deepwater Oil & Gas Resources | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Deepwater Oil & Gas Resources Deepwater Oil & Gas Resources The United States has significant natural gas and oil reserves. But many of these resources are increasingly harder to...

173

Fuel gas conditioning process  

DOE Patents (OSTI)

A process for conditioning natural gas containing C.sub.3+ hydrocarbons and/or acid gas, so that it can be used as combustion fuel to run gas-powered equipment, including compressors, in the gas field or the gas processing plant. Compared with prior art processes, the invention creates lesser quantities of low-pressure gas per unit volume of fuel gas produced. Optionally, the process can also produce an NGL product.

Lokhandwala, Kaaeid A. (Union City, CA)

2000-01-01T23:59:59.000Z

174

Enhanced durability of desulfurization sorbents for fluidized-bed applications  

SciTech Connect

To extend the operating temperature range and further improve the durability of fluidizable sorbents, zinc titanate, another leading regenerable sorbent, was selected for development in the later part of this project. A number of zinc titanate formulations were prepared in the 50 to 300 {mu}m range using granulation and spray drying methods. Important sorbent preparation variables investigated included zinc to titanium ratio, binder type, binder amount, and various chemical additives such as cobalt and molybdenum. A number of sorbents selected on the basis of screening tests were subjected to bench-scale testing for 10 cycles at high temperature, high pressure (HTHP) conditions using the reactor system designed and constructed during the base program. This reactor system is capable of operation either as a 2.0 in. or 3.0 in. I.D. bubbling bed and is rated up to 20 atm operation at 871{degrees}C. Bench-scale testing variables included sorbent type, temperature (550 to 750{degrees}C), gas type (KRW or Texaco gasifier gas), steam content of coal gas, and fluidizing gas velocity (6 to 15 cm/s). The sorbents prepared by spray drying showed poor performance in terms of attrition resistance and chemical reactivity. On the other hand, the granulation method proved to be very successful. For example, a highly attrition-resistant zinc titanate formulation, ZT-4, prepared by granulation exhibited virtually no zinc loss and demonstrated a constant high reactivity and sulfur capacity over 10 cycles, i.e., approximately a 60 percent capacity utilization, with Texaco gas at 750{degrees}C, 15 cm/s fluidizing velocity and 15 atm pressure. The commercial potential of the granulation method for zinc titanate manufacture was demonstrated by preparing two 80 lb batches of sorbent with zinc to titanium mol ratios of 0.8 and 1.5.

Gupta, R.P.; Gangwal, S.K.

1992-11-01T23:59:59.000Z

175

Enhanced durability of desulfurization sorbents for fluidized-bed applications  

SciTech Connect

To extend the operating temperature range and further improve the durability of fluidizable sorbents, zinc titanate, another leading regenerable sorbent, was selected for development in the later part of this project. A number of zinc titanate formulations were prepared in the 50 to 300 [mu]m range using granulation and spray drying methods. Important sorbent preparation variables investigated included zinc to titanium ratio, binder type, binder amount, and various chemical additives such as cobalt and molybdenum. A number of sorbents selected on the basis of screening tests were subjected to bench-scale testing for 10 cycles at high temperature, high pressure (HTHP) conditions using the reactor system designed and constructed during the base program. This reactor system is capable of operation either as a 2.0 in. or 3.0 in. I.D. bubbling bed and is rated up to 20 atm operation at 871[degrees]C. Bench-scale testing variables included sorbent type, temperature (550 to 750[degrees]C), gas type (KRW or Texaco gasifier gas), steam content of coal gas, and fluidizing gas velocity (6 to 15 cm/s). The sorbents prepared by spray drying showed poor performance in terms of attrition resistance and chemical reactivity. On the other hand, the granulation method proved to be very successful. For example, a highly attrition-resistant zinc titanate formulation, ZT-4, prepared by granulation exhibited virtually no zinc loss and demonstrated a constant high reactivity and sulfur capacity over 10 cycles, i.e., approximately a 60 percent capacity utilization, with Texaco gas at 750[degrees]C, 15 cm/s fluidizing velocity and 15 atm pressure. The commercial potential of the granulation method for zinc titanate manufacture was demonstrated by preparing two 80 lb batches of sorbent with zinc to titanium mol ratios of 0.8 and 1.5.

Gupta, R.P.; Gangwal, S.K.

1992-11-01T23:59:59.000Z

176

The utilization of flue gas desulfurization waste by-products in construction brick.  

E-Print Network (OSTI)

??Millions of tons of waste by-products from Texas coal burning plants are produced each year. Two common byproducts are the fuel ashes and calcium sulfate… (more)

Berryman, Charles Wayne

2012-01-01T23:59:59.000Z

177

A Regenerable Calcium-Based Core-in-Shell Sorbent for Desulfurizing Hot Coal Gas  

Science Journals Connector (OSTI)

Other materials used in the sorbent formulations included reagent-grade calcium carbonate from the Fisher Co. and calcium sulfate hemihydrate obtained as commercial-grade plaster of Paris. ... Once coated, the pellets were allowed to tumble for 2.0 h to consolidate the coating. ...

T. T. Akiti, Jr.; K. P. Constant; L. K. Doraiswamy; T. D. Wheelock

2002-01-12T23:59:59.000Z

178

Management of dry flue gas desulfurization by-products in underground mines  

SciTech Connect

Disposal of coal combustion by-products (CCBs) in an environmentally sound manner is a major issue facing the coal and utility industries in the US today. Disposal into abandoned sections of underground coal mines may overcome many of the surface disposal problems along with added benefits such as mitigation of subsidence and acid mine drainage. However, many of the abandoned underground coal mines are located far from power plants, requiring long distance hauling of by-products which will significantly contribute to the cost of disposal. For underground disposal to be economically competitive, the transportation and handling cost must be minimized. This requires careful selection of the system and optimal design for efficient operation. The materials handling and system economics research addresses these issues. Transportation and handling technologies for CCBs were investigated from technical, environmental and economic points of view. Five technologies were found promising: (1) Pneumatic Trucks, (2) Pressure Differential Rail Cars, (3) Collapsible Intermodal Containers, (4) Cylindrical Intermodal Tanks, and (5) Coal Hopper Cars with Automatic Retractable Tarping. The first two technologies are currently being utilized in transporting by-products from power plants to disposal sites, whereas the next three are either in development or in conceptualization phases. In this research project, engineering design and cost models were developed for the first four technologies. The engineering design models are in the form of spreadsheets and serve the purpose of determining efficient operating schedules and sizing of system components.

Sevim, H.

1997-06-01T23:59:59.000Z

179

Desulfurization of a coal model compound by in situ hydrogen generation through water-gas shift  

E-Print Network (OSTI)

TECHNIQUE 94 PAGE APPENDIX 5 TEMPERATURE PROGRAM 101 APPENDIX 6 TEMPERATURE PROFILES 104 NOTATION 112 VITA 113 1x LIST OF FIGURES FIGURE PAGE 1 Reaction Scheme or Benzothiophene (from Guin et al. Ind. Eng. Chem. Process. Dev. , 19 (1980)) 2... and Conversion 62 5 Computer Results or Non-Linear Regression Analysis 98 6 Results of Kinetic Parameters Estimation 7 Statistical Analysis Results for Temperature Profile Tl 108 8 Statistical Analysis Results f or Temperature Prof ile T2 109 9...

Kumar, Meyyappan

1982-01-01T23:59:59.000Z

180

Evaluation of sulfur-reducing microorganisms for organic desulfurization. Final technical report, September 1, 1990--August 31, 1991  

SciTech Connect

Because of substantial portion of the sulfur in Illinois coal is organic, microbial desulfurization of sulfidic and thiophenic functionalities could hold great potential for completing pyritic sulfur removal. We are testing the hypothesis that organic sulfur can be reductively removed as H{sub 2}S through the activities of anaerobic microorganisms. Our objectives for this year include the following: (1) To obtain cultures that will reductively desulfurize thiophenic model compounds. In addition to crude oil enrichments begun last year, we sampled municipal sewage sludge. (2) To continue to work toward optimizing the activity of the DBDS-reducing cultures obtained during the previous year. (3) To expand coal desulfurization work to include other coals including Illinois Basin Coal 101 and a North Dakota lignite, which might be more susceptible to the dibenzyldisulfide reducing cultures due to its lower rank. (4) To address the problem of sulfide sorption, by investigating the sorption capacity of coals in addition to Illinois Basin Coal 108.

Miller, K.W.

1991-12-31T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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.


181

ComEd, Nicor Gas, Peoples Gas and North Shore Gas - Bonus Rebate Program  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

ComEd, Nicor Gas, Peoples Gas and North Shore Gas - Bonus Rebate ComEd, Nicor Gas, Peoples Gas and North Shore Gas - Bonus Rebate Program (Illinois) ComEd, Nicor Gas, Peoples Gas and North Shore Gas - Bonus Rebate Program (Illinois) < Back Eligibility Residential Savings Category Heating & Cooling Commercial Heating & Cooling Cooling Heating Maximum Rebate $1,000 Program Info Start Date 01/01/2013 Expiration Date 04/30/2013 State Illinois Program Type Utility Rebate Program Rebate Amount ComEd Rebates Central Air Conditioner Unit 14 SEER or above: $350 Central Air Conditioner Unit Energy Star rated: $500 Nicor Gas, Peoples Gas and North Shore Gas Furnace: $200 - $500 (varies based on gas company and unit installed) Provider ComEd Energy ComEd, Nicor Gas, Peoples Gas and North Shore Gas are offering a Complete System Replacement Rebate Program to residential customers. The program is

182

Development and evaluation of two reactor designs for desulfurization of Texas lignites  

E-Print Network (OSTI)

Studies One of the earliest extensive studies of sulfur removal from coal was performed by R. D. Snow in 1932. The primary goal of this study was to produce a better metallurgical coke. The effects of various gases on sulfur removal were measured... of coke, most of the hydrogen rich parts of the coal are devolatilized. It is the hydrogen, however, that provides a large part of the energy when the product is used as a fuel. Clearly, any desulfurization technique for fuel should take place under...

Merritt, Stanley Duane

2012-06-07T23:59:59.000Z

183

Shale gas production: potential versus actual greenhouse gas emissions  

E-Print Network (OSTI)

Estimates of greenhouse gas (GHG) emissions from shale gas production and use are controversial. Here we assess the level of GHG emissions from shale gas well hydraulic fracturing operations in the United States during ...

O’Sullivan, Francis Martin

184

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

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

185

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

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

186

Energy Management in Olefins Units  

E-Print Network (OSTI)

to the point where waste heat from pyrolysis generates more than enough steam to power the olefins unit recovery section. Furthermore, incorporating gas turbine driven electrical generators or process compressors adds to the utility export potential of the unit...

Wells, T. A.

1982-01-01T23:59:59.000Z

187

Molecular Gas, AGN Feedback and the Unusual Case of K. A. Alatalo (UC, Berkeley), T. A. Davis (Oxford University, United King-  

E-Print Network (OSTI)

Molecular Gas, AGN Feedback and the Unusual Case of NGC1266 K. A. Alatalo (UC, Berkeley), T. A effort. It remarkably hosts about 109 M of molecular gas and has a spectrum that exhibits extended wings and revealed that the bulk of the gas is concentrated within 100 pc of the nucleus. Combined with the presence

Bureau, Martin

188

United States of Agriculture  

E-Print Network (OSTI)

United States Department of Agriculture Forest Service Rocky Mountain Research Station Proceedings Research Station. 130 p. Declinesinhabitatofgreatersage, grazing practices, changes in wildfire regimes, increased spread of invasive species, gas and oil

189

Desulfurization of saturated C3S molecules on Mo(110): the effect of ring strain  

SciTech Connect

The reactions of trimethylene sulfide (c-C3H6S) and 1-propanethiol (C3H7SH) have been investigated on Mo(110) under ultrahigh vacuum using temperature-programmed reaction spectroscopy and Auger electron spectroscopy. Deuterium preadsorption experiments were conducted in conjunction with temperature-programmed reaction spectroscopy to deduce some mechanistic details of the reactions. Desulfurization reactions of both molecules to produce propane and propene were observed in the temperature range of 300-350 K, with propane production preceding propene production. In addition, trimethylene sulfide decomposed to form cyclopropane at 190 K. Both trimethylene sulfide and 1-propanethiol reacted on Mo(110) to produce gaseous dihydrogen in two peaks at approximately 350 and 540 K, as well as surface carbon and sulfur. Small amounts of reversibly adsorbed 1-propanethiol desorbed from Mo(110) between 175 and 200 K. Auger electron spectroscopy measurements suggest that approximately 50% of chemisorbed trimethylene sulfide decomposed to form hydrocarbons, while 70% of irreversibly chemisorbed 1-propanethiol decomposed to form hydrocarbons. The decomposition of trimethylene sulfide to cyclopropane is postulated to occur by one of three pathways. One of these pathways is entirely intramolecular, and the other two involve metallacycle transition states or intermediates. Trimethylene sulfide and 1-propanethiol are proposed to form propane and propene by way of a surface propyl thiolate intermediate, in a fashion similar to the reactions of tetrahydrothiophene and 1-butanethiol on Mo(110). The possible contributions of ring strain to the energetics and selectivity of the desulfurization reactions are discussed.

Roberts, J.T.; Friend, C.M.

1987-06-24T23:59:59.000Z

190

Thermostabilization of desulfurization enzymes from Rhodococcos sp. IGTS8. Final technical report  

SciTech Connect

The objective of this project was to develop thermophilic cultures capable of expressing the desulfurization (dsz) operon of Rhodococcus sp. IGTS8. The approaches taken in this project included the development of plasmid and integrative expression vectors that function well in Thermus thermophilus, the cloning of Rhodococcus dsz genes in Thermus expression vectors, and the isolation of bacterial cultures that express the dsz operon at thermophilic temperatures. This project has resulted in the development of plasmid and integrative expression vectors for use in T. thermophilus. The dsz genes have been expressed at moderately thermophilic temperatures (52 C) in Mycobacterium phlei and at temperatures as high as 72 C in T. thermophilus. The tools and methods developed in this project will be generally useful for the expression of heterologous genes in Thermus. Key developments in the project have been the isolation of a Mycobacterium phlei culture capable of expressing the desulfurization operon at 52 C, development of plasmid and integrative expression vectors for Thermus thermophilus, and the development of a host-vector system based on the malate dehydrogenase gene that allows plasmids to be stably maintained in T. thermophilus and provides a convenient reporter gene for the accurate quantification of gene expression. Publications have been prepared regarding each of these topics; these preprints are included.

John J. Kilbane II

2000-12-15T23:59:59.000Z

191

United States Department of  

E-Print Network (OSTI)

play an important role in a national program for reducing greenhouse gas emissions. The conversion potential through conversion of nonforest land to forest land and through the management of forest lands and sinks in the United States can be identified. International treaties on greenhouse gas reduction require

192

Control of scale in flue gas scrubbers  

SciTech Connect

This patent describes a flue gas desulfurization system in which sulfur dioxide-containing flue gas is passed in countercurrent flow with an aqueous calcium-bearing scrubbing liquor whereby the sulfur dioxide is removed from the flue gas by being absorbed by the scrubbing liquor and converted to calcium sulfite and/or calcium sulfate. The improvement of minimizing the formation of calcium scale on the surfaces of the system comprises maintaining in the scrubbing liquor about 0.1-25 ppm of a 1:1 diisobutylene-maleic anhydride copolymer having an average molecular weight of 11000. The copolymer is incorporated in the scrubbing liquor as a 10-15% aqueous dispersion.

Thomas, P.A.; Dewitt-Dick, D.B.

1987-06-02T23:59:59.000Z

193

Gas vesicles.  

Science Journals Connector (OSTI)

...these costs can be compared is in units of energy expenditure per time (joules per second...requires 7.24 x 10-18 kg of Gvp. The energy cost of making this protein, Eg, is...Eg = 2.84 x 101- o J. The rate of energy expenditure in gas vesicle synthesis then...

A E Walsby

1994-03-01T23:59:59.000Z

194

Federal Register Notice for Life Cycle Greenhouse Gas Perspective...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Natural Gas from the United States (Life Cycle Analysis Greenhouse Gas Report, or LCA GHG Report) and invites the submission of comments. LifecycleGreenhouseGas.pdf More...

195

Corrosion protection by means of rubber linings in a flue gas scrubber made of concrete  

SciTech Connect

Rubber linings have been applied as a corrosion protection measure for steel surfaces, particularly in the absorbers, in the flue gas desulfurization plants of a large number of power stations in Europe and have decidedly proven their effectiveness. The rubber linings applied consist of either precured and/or cold-curing rubber sheets. In the course of the past five to seven years, the eastern European states have also begun retro-fitting their existing power stations with flue gas desulfurization plants. As the first of its kind, a scrubber in the flue gas desulfurization plant of the Konin Power Station in Poland, which operates on the basis of the limestone-gypsum process, was constructed of concrete. In this case also, the corrosion protection measures implemented consisted in the application of a precured rubber lining on the basis of butyl rubber. A surface area measuring 1,500 m{sup 2} of the concrete absorber was protected by means of this corrosion protection system.

Fenner, J.; Matos, A.; Seiffert, W. [Keramchemie GmbH, Siershahn (Germany)

1998-12-31T23:59:59.000Z

196

Polyethylene glycol as a green solvent for effective extractive desulfurization of liquid fuel at ambient conditions  

Science Journals Connector (OSTI)

Abstract Today there are serious regulations to reduce sulfur content of fuels because the \\{SOx\\} produced during the combustion of fuels containing sulfur compounds make the air polluted and have dangerous environmental impacts. With the aim of replacement of the present volatile, flammable and toxic organic solvents or inefficient, corrosive and expensive ionic liquids (ILs), the polyethylene glycol (PEG) was introduced as a green, effective, non-toxic, non-corrosive and also recyclable molecular solvent for extractive desulfurization (EDS) of benzothiophenic compounds from liquid fuel in this work for the first time. PEG shows excellent EDS and it has the higher extraction efficiency for dibenzothiophene (DBT) (76% within 90 s) than those of ILs. Using this extractant, the BDT content was reduced from 512 to 10 ppmw (98%) only within three extraction stages, the minimum number of cycles within shortest time reported up to now, and the deep desulfurization was achieved. Effect of some important parameters including initial concentration of sulfur compound, PEG dosage, time and temperature of extraction on the EDS process was investigated. It was fond that extraction performance of PEG is independent to temperature and initial sulfur content, which is an excellent finding for industrialization. The feasibility of PEG for extraction of different thiophenic compounds was observed in the order of dibenzothiophene > benzothiophene > 4,6-dimethyldibenzothiopene. Finally, the PEG was reused in several cycles and then it was regenerated by adsorption method. The results of the present work hopefully provide useful information for future industrial application of PEG as an efficient green solvent for the EDS of liquid fuels.

Effat Kianpour; Saeid Azizian

2014-01-01T23:59:59.000Z

197

Production Optimization in Shale Gas Reservoirs.  

E-Print Network (OSTI)

?? Natural gas from organic rich shales has become an important part of the supply of natural gas in the United States. Modern drilling and… (more)

Knudsen, Brage Rugstad

2010-01-01T23:59:59.000Z

198

Graphite-moderated, gas-cooled, and water-moderated, water-cooled reactors as power units in nuclearelectric power stations  

Science Journals Connector (OSTI)

The present article reviews a number of papers submitted at the Second International Conference on the Peaceful Uses of Atomic Energy bearing on water-cooled, water-moderated, graphite-moderated, and gas-coole...

Yu. I. Koryakin

1960-11-01T23:59:59.000Z

199

Natural Gas Reforming  

Energy.gov (U.S. Department of Energy (DOE))

Natural gas reforming is an advanced and mature production process that builds upon the existing natural gas pipeline delivery infrastructure. Today, 95% of the hydrogen produced in the United States is made by natural gas reforming in large central plants. This technology is an important pathway for near-term hydrogen production.

200

United States  

Gasoline and Diesel Fuel Update (EIA)

United States United States Coal ................................................ 4,367 4,077 4,747 4,181 4,473 4,125 4,983 4,330 4,414 4,003 4,796 4,178 4,344 4,479 4,348 Natural Gas .................................... 2,802 2,843 3,694 2,863 2,713 2,880 3,636 2,707 2,792 2,972 3,815 2,849 3,052 2,986 3,109 Petroleum (a) .................................. 74 73 81 67 73 70 75 66 75 70 76 66 74 71 71 Other Gases ................................... 32 33 36 32 32 34 37 33 33 35 39 34 33 34 35 Nuclear ........................................... 2,176 2,044 2,257 2,170 2,106 2,037 2,167 2,010 2,144 2,074 2,206 2,055 2,162 2,080 2,120 Renewable Energy Sources: Conventional Hydropower ........... 736 886 716 633 765 887 708 646 767 919 729 659 742 751 768 Wind ............................................ 491 520 353 449 477 521 379 475

Note: This page contains sample records for the topic "gas desulfurization units" 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

Word Pro - Untitled1  

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

6 6 Installed Nameplate Capacity of Fossil-Fuel Steam-Electric Generators With Environmental Equipment By Fuel and Equipment Type, 2010 Total Units by Equipment Type, 1985-2010² Coal Units by Equipment Type, Petroleum and Natural Gas Units 1985-2010² by Equipment Type, 1985-2010² 318 U.S. Energy Information Administration / Annual Energy Review 2011 Coal Units Petroleum and Natural Gas Units Particulate Collectors Thousand Megawatts 329 165 185 26 75 1 Particulate Collectors Cooling Towers Flue Gas Particulate Collectors Cooling Towers Flue Gas 0 50 100 150 200 250 300 350 1985 1990 1995 2000 2005 2010 0 100 200 300 400 Thousand Megawatts Flue Gas Desulfurization¹ Particulate Collectors Cooling Towers Flue Gas Desulfurization¹ Particulate Collectors Desulfurization¹ Desulfurization¹ Cooling Towers

202

Natural Gas Annual, 2001  

Gasoline and Diesel Fuel Update (EIA)

1 1 EIA Home > Natural Gas > Natural Gas Data Publications Natural Gas Annual, 2001 The Natural Gas Annual, 2001 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2001. Summary data are presented for each State for 1997 to 2001. The data that appear in the tables of the Natural Gas Annual, 2001 are available as self-extracting executable files in ASCII TXT or CSV file format. This volume emphasizes information for 2001, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file. Also available are files containing the following data: Summary Statistics - Natural Gas in the United States, 1997-2001 (Table 1) ASCII TXT, and Natural Gas Supply and Disposition by State, 2001 (Table 2) ASCII TXT.

203

International Standards and Units of Radioactivity  

Science Journals Connector (OSTI)

... latter could be measured and their radium contents expressed in grams. For the measurement of radon, grams (or cubic centimetres) of this gas are impracticable as units, and it ... gas are impracticable as units, and it was therefore decided to use as unit of radon the quantity which is in radioactive equilibrium with 1 gm. of radium; it was ...

1947-12-06T23:59:59.000Z

204

EIS-0105: Conversion to Coal, Baltimore Gas & Electric Company, Brandon Shores Generating Station Units 1 and 2, Anne Arundel County, Maryland  

Energy.gov (U.S. Department of Energy (DOE))

The U.S. Department of Energy’s Economic Regulatory Administration Office of Fuels Program, Coal and Electricity Division prepared this statement to assess the potential environmental and socioeconomic impacts associated with prohibiting the use of petroleum products as a primary energy source for Units 1 and 2 of the Brandon Shores Generating Station, located in Anne Arundel County, Maryland.

205

Design assessment of a 150 kWt CFBC Test Unit  

SciTech Connect

For clean and efficient energy generation from coal, the most suitable technology known to date is 'Fluidized Bed Combustion' technology. Applications of circulating fluidized bed (CFB) combustion technology have been steadily increasing in both capacity and number over the past decade. Designs of these units have been based on the combustion tests carried out in pilot scale facilities to determine the combustion and desulfurization characteristics of coal and limestone reserves in CFB conditions. Similarly, utilization of Turkish lignites in CFB boilers necessitates adaptation of CFB combustion technology to these resources. However, the design of these test units are not based on firing coals with high ash, volatile matter and sulfur contents like Turkish lignites. For this purpose, a 150 kWt CFB combustor test unit is designed and constructed in Chemical Engineering Department of Middle East Technical University, based on the extensive experience acquired at the existing 0.3 MWt Bubbling Atmospheric Fluidized Bed Combustor (AFBC) Test Rig. Following the commissioning tests, a combustion test is carried out for investigation of combustion characteristics of Can lignite in CFB conditions and for assessment of the design of test unit. Comparison of the design outputs with experimental results reveals that most of the predictions and assumptions have acceptable agreement with the operating conditions. In conclusion, the performance of 150 kWt CFBC Test Unit is found to be satisfactory to be utilized for the long term research studies on combustion and desulfurization characteristics of indigenous lignite reserves in circulating fluidized bed combustors. (author)

Batu, A. [Mimag-Samko Energy Technologies Inc., Armada Is Merkezi Kat: 5, No: 4 Sogutozu, Ankara (Turkey); Selcuk, N.; Kulah, G. [Middle East Technical University, Chemical Engineering Department, 06531 Ankara (Turkey)

2010-04-15T23:59:59.000Z

206

Natural Gas Fuel Basics | Department of Energy  

Energy Savers (EERE)

Natural Gas Fuel Basics Natural Gas Fuel Basics July 30, 2013 - 4:40pm Addthis Only about one-tenth of 1% of all the natural gas in the United States is currently used for...

207

Compressed Gas Cylinder Safe Handling, Use and  

E-Print Network (OSTI)

Compressed Gas Cylinder Safe Handling, Use and Storage 2012 Workplace Safety and Environmental Protection #12;i College/Unit: Workplace Safety and Environmental Protection Procedure Title: Compressed Gas................................................ 4 7 General Gas Cylinder Information

Saskatchewan, University of

208

API unit  

Science Journals Connector (OSTI)

API unit [An arbitrary unit of the American Petroleum Institute for measuring natural radioactivity; used in certain well logging methods] ? API-Einheit f

2014-08-01T23:59:59.000Z

209

Reduction in Unit Steam Production  

E-Print Network (OSTI)

In 2001 the company's Arch-Brandenburg facility faced increased steam costs due to high natural gas prices and decreased production due to shutdown of a process. The facility was challenged to reduce unit steam consumption to minimize the effects...

Gombos, R.

2004-01-01T23:59:59.000Z

210

United States Department of  

E-Print Network (OSTI)

United States Department of Agriculture Forest Service Pacific Northwest Research Station General.S. Department of Agriculture, Forest Service, Pacific Northwest Research Station. 25 p. Estimates of forest of California's legislatively mandated green- house gas inventory. Reliable estimates of live-tree carbon stores

Fried, Jeremy S.

211

Ultra-high CO2 capture efficiency in CFB oxyfuel power plants by calcium looping process for CO2 recovery from purification units vent gas  

Science Journals Connector (OSTI)

Abstract This work presents a new option for the recovery of the CO2 losses from CO2 purification units in oxyfuel plants, by means of the Ca-looping process. The idea is to capture the CO2 in the vent stream from purification units by reaction with CaO sorbent in a carbonator reactor, where CaCO3 is formed. Sorbent is then regenerated in a calciner reactor by oxyfuel combustion of a fraction of the coal fed to the power plant. Since the Ca-looping process requires a continuous purge of exhaust sorbent and make-up of fresh limestone, the system is best coupled with a CFB boiler, where the exhausted Ca-rich sorbent can be used for in-furnace sulfur absorption. In this work, detailed mass and energy balances of the system proposed are reported, including a preliminary sizing of the reactors of the Ca-looping unit. A sensitivity analysis was also performed, by considering two types of coal as feed (mainly differing in sulfur content), two levels of non-condensable gases in the impure CO2 stream to be purified and different behaviors of the exhausted Ca-based sorbent injected in the CFB boiler, where it can experience different levels of recarbonation. Interesting results were obtained for this new system, which can capture about 90% of the CO2 vented from the purification unit in a reasonably compact reactors system, allowing an overall CO2 avoidance of the order of 99% with respect to conventional coal-fired steam plants without capture. As far as energy penalties are concerned, they were evaluated by the specific primary energy consumption for CO2 avoided index (SPECCA). Small differences with respect to reference oxyfuel plants without CO2 recovery were obtained, with either slightly better or slightly worse performances, depending on the sulfur content of the coal used. Penalties are associated to the export of CaO in the final exhausted sulfated sorbent from the CFB boiler, which increases when a higher sulfur coal is used. However, experimental analysis on the recarbonation level which can be attained by the CaL exhaust sorbent in the CFB boiler and further process optimization are needed to correctly account for these penalties and possibly minimize them.

Matteo C. Romano

2013-01-01T23:59:59.000Z

212

Preliminary Assessment of Hydrocarbon Gas Sources from the Mt. Elbert No. 1 Gas Hydrate Test Well  

E-Print Network (OSTI)

in two primary horizons; an upper zone, (“D ” Unit) containing 14 meters of gas hydrate-bearing sands

Thomas D. Lorenson; Timothy S. Collett; Robert B. Hunter

213

Management of dry flue gas desulfurization by-products in underground mines. Quarterly report, August 1--October 31, 1997  

SciTech Connect

The objective of this project was to develop and demonstrate two technologies for the placement of coal combustion by-products in abandoned underground coal mines, and to assess the environmental impact of these technologies for the management of CCB materials. The two technologies for the underground placement that were to be developed and demonstrated are: (1) pneumatic placement using virtually dry CCB products, and (2) hydraulic placement using a paste mixture of CCB products with about 70% solids. The period covered by this report is the second quarter of Phase 3 of the overall program. During this period over 8,000 tons of CCB mixtures was injected using the hydraulic paste technology. This amount of material virtually filled the underground opening around the injection well, and was deemed sufficient to demonstrate fully the hydraulic injection technology. By the end of this quarter about 2,000 tons of fly ash had been placed underground using the pneumatic placement technology. While the rate of injection of about 50 tons per hour met design criteria, problems were experienced in the delivery of fly ash to the pneumatic demonstration site. The source of the fly ash, the Archer Daniels Midland Company power plant at Decatur, Illinois is some distance from the demonstration site, and often sufficient tanker trucks are not available to haul enough fly ash to fully load the injection equipment. Further, on some occasions fly ash from the plant was not available. The injection well was plugged three times during the demonstration. This typically occurred due to cementation of the FBC ash in contact with water. After considerable deliberations and in consultation with the technical project officer, it was decided to stop further injection of CCB`s underground using the developed pneumatic technology.

Chugh, Y.P.

1997-12-31T23:59:59.000Z

214

Management of dry gas desulfurization by-products in underground mines. Quarterly report, October 1--December 31, 1996  

SciTech Connect

The objective is to develop and demonstrate two technologies for the placement of coal combustion by-products in abandoned underground coal mines, and to assess the environmental impact of these technologies for the management of coal combustion by-products. The two technologies for the underground placement that will be developed and demonstrated are: (1) pneumatic placement using virtually dry coal combustion by-products, and (2) hydraulic placement using a paste mixture of combustion by-products with about 70% solids. Phase 2 of the overall program began April 1, 1996. The principal objective of Phase 2 is to develop and fabricate the equipment for both the pneumatic and hydraulic placement technologies, and to conduct a limited, small-scale shakedown test of the pneumatic and hydraulic placement equipment. The shakedown test originally was to take place on the surface, in trenches dug for the tests. However, after a thorough study it was decided, with the concurrence of DOE-METC, to drill additional injection wells and conduct the shakedown tests underground. This will allow a more thorough test of the placement equipment.

NONE

1996-12-31T23:59:59.000Z

215

Intermountain Gas Company (IGC) - Gas Heating Rebate Program | Department  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Intermountain Gas Company (IGC) - Gas Heating Rebate Program Intermountain Gas Company (IGC) - Gas Heating Rebate Program Intermountain Gas Company (IGC) - Gas Heating Rebate Program < Back Eligibility Residential Savings Category Heating & Cooling Commercial Heating & Cooling Heating Program Info State Idaho Program Type Utility Rebate Program Rebate Amount Furnace: $200/unit Provider Customer Service The Intermountain Gas Company's (IGC) Gas Heating Rebate Program offers customers a $200 per unit rebate when they convert to a high efficiency natural gas furnace that replaces a heating system using another energy source. New furnaces must meet a minimum AFUE efficiency rating of 90%, and the home must have been built at least three years prior to the furnace conversion to qualify for the rebate. Visit IGC's program web site for more

216

UNIT NUMBER:  

NLE Websites -- All DOE Office Websites (Extended Search)

193 UNIT NUMBER: 197 UNIT NAME: CONCRETE RUBBLE PILE (30) REGULATORY STATUS: AOC LOCATION: Outside plant security fence, north of the plant on Big Bayou Creek on private property....

217

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

7 UNIT NUMBER UNIT NAME Rubble oile 41 REGULATORY STATUS: AOC LOCATION: Butler Lake Dam, West end of Butler Lake top 20 ft wide, 10 ft APPROXIMATE DIMENSIONS: 200 ft long, base 30...

218

Effect of High-Pressure Impregnation on Structure Variation and Desulfurization Property of a Zn-Based Sorbent Prepared Using Lignite as a Support  

Science Journals Connector (OSTI)

Effect of High-Pressure Impregnation on Structure Variation and Desulfurization Property of a Zn-Based Sorbent Prepared Using Lignite as a Support ... Lignite reserves are relatively abundant in China; however, its utilization is significantly limited because of its high water content and low calorific value. ...

Xiurong Ren; Qiang He; Yurong Dong; Meijun Wang; Liping Chang; Weiren Bao

2014-06-10T23:59:59.000Z

219

A Path to Reduce Methane Emissions from Gas Systems | Department...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Ernest Moniz Secretary of Energy The United States is now the world's largest producer of natural gas. This natural gas revolution is driving economic growth across the country,...

220

"Assessment of the Adequacy of Natural Gas Pipeline Capacity...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

"Assessment of the Adequacy of Natural Gas Pipeline Capacity in the Northeast United States" Report Now Available "Assessment of the Adequacy of Natural Gas Pipeline Capacity in...

Note: This page contains sample records for the topic "gas desulfurization units" 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

Assessment of the Adequacy of Natural Gas Pipeline Capacity in...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Assessment of the Adequacy of Natural Gas Pipeline Capacity in the Northeast United States - November 2013 Assessment of the Adequacy of Natural Gas Pipeline Capacity in the...

222

Questar Gas - Home Builder Gas Appliance Rebate Program | Department of  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Questar Gas - Home Builder Gas Appliance Rebate Program Questar Gas - Home Builder Gas Appliance Rebate Program Questar Gas - Home Builder Gas Appliance Rebate Program < Back Eligibility Construction Multi-Family Residential Residential Savings Category Heating & Cooling Commercial Heating & Cooling Heating Home Weatherization Construction Commercial Weatherization Design & Remodeling Appliances & Electronics Water Heating Program Info State Utah Program Type Utility Rebate Program Rebate Amount Exterior Wall Insulation: $350 (single family), $150 (multifamily) Windows: $2.50/sq. ft. Gas Furnace: $200 - $400 Gas Storage Water Heater: $50-$100 Gas Condensing Water Heater: $350 Gas Boiler: $400 -$600 Tankless Gas Water Heater: $350 Single Family Homes (New Construction): $50 - $500 Multifamily Homes (New Construction): $50 - $300/unit

223

Natural Gas Regulation - Other Gas-Related Information Sources | Department  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Natural Gas Regulation - Other Gas-Related Information Sources Natural Gas Regulation - Other Gas-Related Information Sources Natural Gas Regulation - Other Gas-Related Information Sources The single largest source of energy information available is the Department of Energy's Energy Information Administration (EIA). The EIA publishes extensive reports on natural gas and other energy sources. Domestic natural gas markets are regulated in part by the Federal Energy Regulatory Commission. The commission's chief area of concern is the interstate natural gas market. Natural gas moves for the most part by pipeline in the United States. The safety of those pipelines is the concern of the Department of Transportation's Office of Pipeline Safety. In Canada the regulation of interprovincial and international natural gas is the responsibility of the National Energy Board. Their areas of

224

EIA - Natural Gas Analysis Basics  

Gasoline and Diesel Fuel Update (EIA)

for Natural Gas Basics for Natural Gas Basics Where Our Natural Gas Comes From Natural Gas Prices Natural Gas Statistics Natural Gas Kid's Page (Not Just for Kids) How natural gas was formed, how we get it, how it is stored and delivered, how it is measured, what it is used for, how it affects the environment and more. Natural Gas Residential Choice This site provides an overview of the status of natural gas industry restructuring in each state, focusing on the residential customer class. About U.S. Natural Gas Pipelines State Energy Profiles What role does liquefied natural gas (LNG) play as an energy source for the United States? This Energy In Brief discusses aspects of LNG industry in the United States. LNG is natural gas that has been cooled to about minus 260 degrees Fahrenheit for shipment and/or storage as a liquid. Growth in LNG imports to the United States has been uneven in recent years, with substantial changes in year-over-year imports as a result of suppliersÂ’ decisions to either bring spare cargos to the United States or to divert cargos to countries where prices may be higher. Categories: Imports & Exports/Pipelines (Released, 12/11/2009)

225

Natural Gas Annual, 2004  

Gasoline and Diesel Fuel Update (EIA)

4 4 EIA Home > Natural Gas > Natural Gas Data Publications Natural Gas Annual, 2004 Natural Gas Annual 2004 Release date: December 19, 2005 Next release date: January 2007 The Natural Gas Annual, 2004 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2004. Summary data are presented for each State for 2000 to 2004. The data that appear in the tables of the Natural Gas Annual, 2004 is available as self-extracting executable file or CSV file format. This volume emphasizes information for 2004, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file.

226

The Development of Warm Gas Cleanup Technologies for the Removal of Sulfur Containing Species from Steam Hydrogasification  

E-Print Network (OSTI)

economic comparison of IGCC power plants with cold gas cleanup and hot gas cleanup units using Indian coals.

Luo, Qian

2012-01-01T23:59:59.000Z

227

Carbon Dioxide Capture from Flue Gas Using Dry, Regenerable Sorbents  

SciTech Connect

This report describes research conducted between July 1, 2006 and September 30, 2006 on the use of dry regenerable sorbents for removal of carbon dioxide (CO{sub 2}) from coal combustion flue gas. Modifications to the integrated absorber/ sorbent regenerator/ sorbent cooler system were made to improve sorbent flow consistency and measurement reliability. Operation of the screw conveyor regenerator to achieve a sorbent temperature of at least 120 C at the regenerator outlet is necessary for satisfactory carbon dioxide capture efficiencies in succeeding absorption cycles. Carbon dioxide capture economics in new power plants can be improved by incorporating increased capacity boilers, efficient flue gas desulfurization systems and provisions for withdrawal of sorbent regeneration steam in the design.

David A. Green; Thomas O. Nelson; Brian S. Turk; Paul D. Box Raghubir P. Gupta

2006-09-30T23:59:59.000Z

228

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

174 10 12 92 UNIT NAME: C-745-K Low Level Storage Area REGULATORY STAU: -AOC LOCATION: Inside Security Fence , South of C-333 Cascade Building. APPROXIMATE...

229

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

4 UNIT NAME C-611 Underaround Diesel Tank REGULATORY STATUS: AOC LOCATION: Immediately southeast of C-611 APPROXIMATE DIMENSIONS: 1000 gallon FUNCTION: Diesel storage OPERATIONAL...

230

UNIT NUMBER:  

NLE Websites -- All DOE Office Websites (Extended Search)

7 KOW Toluene SDill Area UNIT NAME: REGULATORY STATUS: AOC LOCATION: Southwest of plant site APPROXIMATE DIMENSIONS: 200 feet wide by 800 feet ong FUNCTION: Storage of Toluene...

231

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

9 UNIT NAME C-746-Al REGULATORY STATUS: AOC LOCATION: Northwest corner of C-746-A APPROXIMATE DIMENSIONS: 4000 gallons FUNCTION: Underground storage tanks OPERATIONAL STATUS:...

232

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

1 UNIT NAME C-611 Underaround Gasoline Tank REGULATORY STATUS: AOC LOCATION: Immediately east of C-61l APPROXIMATE DIMENSIONS: 50 ga on FUNCTION: Gasoline storage OPERATIONAL...

233

Ammonia synthesis gas purification  

SciTech Connect

This patent describes the purification of a reformed gas mixture following water gas shift conversion to produce a purified ammonia synthesis gas stream. The improved processing sequence consisting essentially of: (A) Selectively catalytically oxidizing the residual carbon monoxide content of the gas mixture to carbon dioxide so as to reduce the carbon monoxide content of the gas mixture to less than about 20 ppm, the selective catalytic oxidation being carried out with an excess of air, with the excess oxygen being catalytically reacted with a small amount of hydrogen so that the residual oxygen level is reduced to less than about 3 ppm; (B) removing the bulk of the carbon dioxide content of the gas mixture by liquid absorption; (C) Removing residual amounts of carbon monoxide, carbon dioxide and water by selective adsorption on the fixed beds of a thermal swing adsorption system, a dry, purified ammonia ammonia synthesis gas stream containing less than a total of 10 ppm of carbon monoxide and carbon dioxide being recovered from the thermal swing adsorption system; (D) Passing the resulting dry, purified ammonia synthesis gas stream having a low content of methane to an ammonia production operation without intermediate passage of the ammonia synthesis gas stream to a methanation unit or to a cryogenic unit for removal of carbon monoxide and carbon dioxide therefrom; whereby the efficiency of the overall purification operation and the effective utilization of hydrogen are enhanced.

Fuderer, A.

1986-02-25T23:59:59.000Z

234

Liquefied Natural Gas | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Liquefied Natural Gas Liquefied Natural Gas Liquefied Natural Gas Liquefied Natural Gas Natural gas plays a vital role in the U.S. energy supply and in achieving the nation's economic and environmental goals. One of several supply options involves increasing imports of liquefied natural gas (LNG) to ensure that American consumers have adequate supplies of natural gas for the future. Natural gas consumption in the United States is expected to increase slightly from about 24.3 trillion cubic feet (Tcf) in 2011 to 26.6 Tcf by 2035. Currently, most of the demand for natural gas in the United States is met with domestic production and imports via pipeline from Canada. A small percentage of gas supplies are imported and received as liquefied natural gas. A significant portion of the world's natural gas resources are

235

Reducing water freshwater consumption at coal-fired power plants : approaches used outside the United States.  

SciTech Connect

Coal-fired power plants consume huge quantities of water, and in some water-stressed areas, power plants compete with other users for limited supplies. Extensive use of coal to generate electricity is projected to continue for many years. Faced with increasing power demands and questionable future supplies, industries and governments are seeking ways to reduce freshwater consumption at coal-fired power plants. As the United States investigates various freshwater savings approaches (e.g., the use of alternative water sources), other countries are also researching and implementing approaches to address similar - and in many cases, more challenging - water supply and demand issues. Information about these non-U.S. approaches can be used to help direct near- and mid-term water-consumption research and development (R&D) activities in the United States. This report summarizes the research, development, and deployment (RD&D) status of several approaches used for reducing freshwater consumption by coal-fired power plants in other countries, many of which could be applied, or applied more aggressively, at coal-fired power plants in the United States. Information contained in this report is derived from literature and Internet searches, in some cases supplemented by communication with the researchers, authors, or equipment providers. Because there are few technical, peer-reviewed articles on this topic, much of the information in this report comes from the trade press and other non-peer-reviewed references. Reducing freshwater consumption at coal-fired power plants can occur directly or indirectly. Direct approaches are aimed specifically at reducing water consumption, and they include dry cooling, dry bottom ash handling, low-water-consuming emissions-control technologies, water metering and monitoring, reclaiming water from in-plant operations (e.g., recovery of cooling tower water for boiler makeup water, reclaiming water from flue gas desulfurization [FGD] systems), and desalination. Some of the direct approaches, such as dry air cooling, desalination, and recovery of cooling tower water for boiler makeup water, are costly and are deployed primarily in countries with severe water shortages, such as China, Australia, and South Africa. Table 1 shows drivers and approaches for reducing freshwater consumption in several countries outside the United States. Indirect approaches reduce water consumption while meeting other objectives, such as improving plant efficiency. Plants with higher efficiencies use less energy to produce electricity, and because the greater the energy production, the greater the cooling water needs, increased efficiency will help reduce water consumption. Approaches for improving efficiency (and for indirectly reducing water consumption) include increasing the operating steam parameters (temperature and pressure); using more efficient coal-fired technologies such as cogeneration, IGCC, and direct firing of gas turbines with coal; replacing or retrofitting existing inefficient plants to make them more efficient; installing high-performance monitoring and process controls; and coal drying. The motivations for increasing power plant efficiency outside the United States (and indirectly reducing water consumption) include the following: (1) countries that agreed to reduce carbon emissions (by ratifying the Kyoto protocol) find that one of the most effective ways to do so is to improve plant efficiency; (2) countries that import fuel (e.g., Japan) need highly efficient plants to compensate for higher coal costs; (3) countries with particularly large and growing energy demands, such as China and India, need large, efficient plants; (4) countries with large supplies of low-rank coals, such as Germany, need efficient processes to use such low-energy coals. Some countries have policies that encourage or mandate reduced water consumption - either directly or indirectly. For example, the European Union encourages increased efficiency through its cogeneration directive, which requires member states to assess their

Elcock, D. (Environmental Science Division)

2011-05-09T23:59:59.000Z

236

Natural Gas Annual, 2000  

Gasoline and Diesel Fuel Update (EIA)

Natural Gas Annual, 2000 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2000. Summary data are presented for each Census Division and State for 1996 to 2000. A section of historical data at the National level shows industry activities back to the 1930's. Natural Gas Annual, 2000 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2000. Summary data are presented for each Census Division and State for 1996 to 2000. A section of historical data at the National level shows industry activities back to the 1930's. The data that appear in the tables of the Natural Gas Annual, 2000 are available as self-extracting executable files in ASCII TXT or CSV file formats. This volume emphasizes information for 2000, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file. Also available are files containing the following data: Summary Statistics - Natural Gas in the United States, 1996-2000 (Table 1) ASCII TXT, and Natural Gas Supply and Disposition by State, 2000 (Table 2) ASCII TXT, are also available.

237

NATURAL GAS FROM SHALE: Questions and Answers  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Where is shale gas found Where is shale gas found in the United States? Shale gas is located in many parts of the United States. These deposits occur in shale "plays" - a set of discovered, undiscovered or possible natural gas accumulations that exhibit similar geological characteristics. Shale plays are located within large-scale basins or accumulations of sedimentary rocks, often hundreds of miles across, that also may contain other oil and gas resources. 1 Shale gas production is currently occurring in 16 states. 1 U.S. Government Accountability Office, Report to Congressional Requesters, "Oil and Gas: Information on Shale Resources, Development, and

238

Task 4.7 - diesel fuel desulfurization. Semi-annual report, July 1, 1995--December 31, 1995  

SciTech Connect

Reductions in the maximum permissible sulfur content of diesel fuel to less than 0.05 wt% will require deep desulfurization to meet these standards. In some refineries, a new hydrogenation catalyst may be required for diesel fuel production. The work very briefly described in this document is on the use of hydrotalcite-supported molybdenum sulfide in the catalysis of ethanol. The catalyst reaction was highly selective for 1-butanol, providing a very clean reaction. Since the catalysis contains the MoS{sub 2} needed for the dehydrogenation and hydrogenation steps, the reaction can be performed at lower temperatures and higher selectivity. The catalyst was very stable and not destroyed by the water produced in the reaction.

Olson, E.S.

1998-12-31T23:59:59.000Z

239

Economics of Electric Compressors for Gas Transmission  

E-Print Network (OSTI)

) option. Outside of these regions, new electric drives as well as gas fueled reciprocating engines and turbines are being considered for replacement of older reciprocating gas engines and compressor units, based on improved operating efficiency. We review...

Schmeal, W. R.; Hibbs, J. J.

240

A New Global Unconventional Natural Gas Resource Assessment  

E-Print Network (OSTI)

. Very little is known publicly about technically recoverable unconventional gas resource potential on a global scale. Driven by a new understanding of the size of gas shale resources in the United States, we estimated original gas in place (OGIP...

Dong, Zhenzhen

2012-10-19T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Shale Gas Production: Potential versus Actual GHG Emissions  

E-Print Network (OSTI)

Estimates of greenhouse gas (GHG) emissions from shale gas production and use are controversial. Here we assess the level of GHG emissions from shale gas well hydraulic fracturing operations in the United States during ...

O'Sullivan, Francis

242

UNITED STATES NATURAL GAS PRICES TO 2015  

E-Print Network (OSTI)

The contents of this paper are the sole responsibility of the author. They do not necessarily represent the views of the Oxford Institute for Energy Studies or any of its Members. Copyright © 2007 Oxford Institute for Energy Studies (Registered Charity, No. 286084) This publication may be reproduced in part for educational or non-profit purposes without special permission from the copyright holder, provided acknowledgment of the source is made. No use of this publication may be made for resale or for any other commercial purpose whatsoever without prior

Michelle Michot Foss, Ph.D.

2007-01-01T23:59:59.000Z

243

Natural gas pipeline technology overview.  

SciTech Connect

The United States relies on natural gas for one-quarter of its energy needs. In 2001 alone, the nation consumed 21.5 trillion cubic feet of natural gas. A large portion of natural gas pipeline capacity within the United States is directed from major production areas in Texas and Louisiana, Wyoming, and other states to markets in the western, eastern, and midwestern regions of the country. In the past 10 years, increasing levels of gas from Canada have also been brought into these markets (EIA 2007). The United States has several major natural gas production basins and an extensive natural gas pipeline network, with almost 95% of U.S. natural gas imports coming from Canada. At present, the gas pipeline infrastructure is more developed between Canada and the United States than between Mexico and the United States. Gas flows from Canada to the United States through several major pipelines feeding U.S. markets in the Midwest, Northeast, Pacific Northwest, and California. Some key examples are the Alliance Pipeline, the Northern Border Pipeline, the Maritimes & Northeast Pipeline, the TransCanada Pipeline System, and Westcoast Energy pipelines. Major connections join Texas and northeastern Mexico, with additional connections to Arizona and between California and Baja California, Mexico (INGAA 2007). Of the natural gas consumed in the United States, 85% is produced domestically. Figure 1.1-1 shows the complex North American natural gas network. The pipeline transmission system--the 'interstate highway' for natural gas--consists of 180,000 miles of high-strength steel pipe varying in diameter, normally between 30 and 36 inches in diameter. The primary function of the transmission pipeline company is to move huge amounts of natural gas thousands of miles from producing regions to local natural gas utility delivery points. These delivery points, called 'city gate stations', are usually owned by distribution companies, although some are owned by transmission companies. Compressor stations at required distances boost the pressure that is lost through friction as the gas moves through the steel pipes (EPA 2000). The natural gas system is generally described in terms of production, processing and purification, transmission and storage, and distribution (NaturalGas.org 2004b). Figure 1.1-2 shows a schematic of the system through transmission. This report focuses on the transmission pipeline, compressor stations, and city gates.

Folga, S. M.; Decision and Information Sciences

2007-11-01T23:59:59.000Z

244

United States  

Office of Legacy Management (LM)

- I - I United States Department of Energy D lSCk Al M E R "This book 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 herein 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 Government or any agency

245

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

5 UNIT NAME C-333 North Side PCB Soil Contamination REGULATORY STATUS: AOC LOCATION: North side of C-333 Building APPROXIMATE OIMENSIONS: 150 ft by 100 ft FUNCTION: Dust Palliative...

246

UNIT NUMBER:  

NLE Websites -- All DOE Office Websites (Extended Search)

4 KPDES Outfall Ditch 017 Flume- Soil Backfill UNIT NAME: - REGULATORY STATUS: AOC LOCATION: South of plant on the west side of the access road APPROXIMATE DIMENSIONS: 30 feet wide...

247

UNIT NUMBER:  

NLE Websites -- All DOE Office Websites (Extended Search)

2 C-617-A Sanitarv Waterline- Soil Backfill UNIT NAME: - REGULATORY STATUS: AOC LOCATION: Between southeast corner of C-531 Switchyard and C-617-A Water Treatment Facility. 4 feet...

248

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

1 UNIT NAME C-720 Inactive TCE Oegreaser REGULATORY STATUS: AOC LOCATION: C-720 Building APPROXIMATE DIMENSIONS: Approx. 10 ft by 10 ft by 20 f1: deep FUNCTION: Used for cleaning...

249

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

2 UNIT NAME Rubble Dile 46 REGULATORY STATUS: AOC LOCATION: 2000 ft southwest of curve on Kentucky Highway 473- near east end of Mitchell Lake APPROXIMATE DIMENSIONS: About 100 ft...

250

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

1 UNIT NAME Rubble oile 45 REGULATORY STATUS AOC LOCATION: West end of Mitche Lake APPROXIMATE DIMENSIONS: 2000 ft long, ft thick 4 ft wide FUNCTION: Control erosion on face of dam...

251

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

9 UNIT NAME Rubble Dile 43 REGULATORY STATUS: AOC LOCATION: West end of Happy Ho ow Lake APPROXIMATE DIMENSIONS: 200 ft long by 4 ft wide -concrete 4-6 in thickness FUNCTION:...

252

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

6 UNIT NAME C-740 TCE Soill Site REGULATORY STATUS: AOC LOCATION: Northwest corner C-740 concrete pad area) APPROXIMATE DIMENSIONS: 5 ft by 5 ft spill FUNCTION: Drum storage area...

253

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

8 C-I00 South Side Berms UNIT NAME REGULATORY STATUS: AOC LOCATION: South Side C-IOO APPROXIMATE DIMENSIONS: 2 berms approximately 200 ft long by SO ft wide eac FUNCTION:...

254

UNIT NUMBER:  

NLE Websites -- All DOE Office Websites (Extended Search)

3 UNIT NAME: C-331 PCB Soil Contamination -West Side REGULATORY STATUS: AOC LOCATION: West side C-331 building APPROXIMATE DIMENSIONS: 100 feet wide by 420 feet long FUNCTION: Dust...

255

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

3 C-750B Diesel UST UNIT NAME REGULATORY STATUS: AOC LOCATION: Southeast corner of C-750 APPROXIMATE DIMENSIONS: 10,000 gallon FUNCTION: Diesel storage OPERATIONAL STATUS: Removed...

256

UNIT NUMBER  

NLE Websites -- All DOE Office Websites (Extended Search)

5 UNIT NAME C-633 PCB So111 Site REGULATORY STATUS CERCLA LOCATION C-633 Transformer area (Mac location 75) APPROXIMATE DIMENSIONS I Unknown FUNCTION Soill site OPERATIONAL STATUS...

257

Natural Gas Annual 2007  

Gasoline and Diesel Fuel Update (EIA)

7 7 Released: January 28, 2009 The Natural Gas Annual 2007 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2007. Summary data are presented for each State for 2003 to 2007. The Natural Gas Annual 2007 Summary Highlights provides an overview of the supply and disposition of natural gas in 2007 and is intended as a supplement to the Natural Gas Annual 2007. Natural Gas Annual --- Full report in PDF (5 MB) Special Files --- All CSV files contained in a self-extracting executable file. Respondent/Company Level Natural Gas Data Files Annual Natural and Supplemental Gas Supply and Disposition Company level data (1996 to 2007) as reported on Form EIA-176 are provided in the EIA-176 Query System and selected data files. EIA-191A Field Level Underground Natural Gas Storage Data: Detailed annual data (2005 to 2007) of storage field capacity, field type, and maximum deliverability as of December 31st of the report year, as reported by operators of all U.S. underground natural gas storage fields.

258

Natural Gas Annual, 2003  

Gasoline and Diesel Fuel Update (EIA)

3 3 EIA Home > Natural Gas > Natural Gas Data Publications Natural Gas Annual, 2003 Natural Gas Annual 2003 Release date: December 22, 2004 Next release date: January 2006 The Natural Gas Annual, 2003 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2003. Summary data are presented for each State for 1999 to 2003. “The Natural Gas Industry and Markets in 2003” is a special report that provides an overview of the supply and disposition of natural gas in 2003 and is intended as a supplement to the Natural Gas Annual 2003. The data that appear in the tables of the Natural Gas Annual, 2003 is available as self-extracting executable file or CSV file format. This volume emphasizes information for 2003, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file.

259

Natural Gas Annual, 2002  

Gasoline and Diesel Fuel Update (EIA)

2 2 EIA Home > Natural Gas > Natural Gas Data Publications Natural Gas Annual, 2002 Natural Gas Annual 2002 Release date: January 29, 2004 Next release date: January 2005 The Natural Gas Annual, 2002 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2002. Summary data are presented for each State for 1998 to 2002. “The Natural Gas Industry and Markets in 2002” is a special report that provides an overview of the supply and disposition of natural gas in 2002 and is intended as a supplement to the Natural Gas Annual 2002. Changes to data sources for this Natural Gas Annual, as a result of ongoing data quality efforts, have resulted in revisions to several data series. Production volumes have been revised for the Federal offshore and several States. Several data series based on the Form EIA-176, including deliveries to end-users in several States, were also revised. Additionally, revisions have been made to include updates to the electric power and vehicle fuel end-use sectors.

260

Natural Gas Annual 2009  

Gasoline and Diesel Fuel Update (EIA)

9 9 Released: December 28, 2010 The Natural Gas Annual 2009 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2009. Summary data are presented for each State for 2005 to 2009. The Natural Gas Annual 2009 Summary Highlights provides an overview of the supply and disposition of natural gas in 2009 and is intended as a supplement to the Natural Gas Annual 2009. Natural Gas Annual --- Full report in PDF (5 MB) Special Files --- All CSV files contained in a self-extracting executable file. Respondent/Company Level Natural Gas Data Files Annual Natural and Supplemental Gas Supply and Disposition Company level data (1996 to 2009) as reported on Form EIA-176 are provided in the EIA-176 Query System and selected data files. EIA-191A Field Level Underground Natural Gas Storage Data: Detailed annual data (2005 to 2009) of storage field capacity, field type, and maximum deliverability as of December 31st of the report year, as reported by operators of all U.S. underground natural gas storage fields.

Note: This page contains sample records for the topic "gas desulfurization units" 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

Natural Gas Annual 2008  

Gasoline and Diesel Fuel Update (EIA)

8 8 Released: March 2, 2010 The Natural Gas Annual 2008 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 2008. Summary data are presented for each State for 2004 to 2008. The Natural Gas Annual 2008 Summary Highlights provides an overview of the supply and disposition of natural gas in 2008 and is intended as a supplement to the Natural Gas Annual 2008. Natural Gas Annual --- Full report in PDF (5 MB) Special Files --- All CSV files contained in a self-extracting executable file. Respondent/Company Level Natural Gas Data Files Annual Natural and Supplemental Gas Supply and Disposition Company level data (1996 to 2008) as reported on Form EIA-176 are provided in the EIA-176 Query System and selected data files. EIA-191A Field Level Underground Natural Gas Storage Data: Detailed annual data (2005 to 2008) of storage field capacity, field type, and maximum deliverability as of December 31st of the report year, as reported by operators of all U.S. underground natural gas storage fields.

262

Chapter 10 - Natural Gas Sweetening  

Science Journals Connector (OSTI)

Abstract Acid gas constituents present in most natural gas streams are mainly hydrogen sulfide (H2S) and carbon dioxide (CO2). Many gas streams, however, particularly those in a refinery or manufactured gases, may contain mercaptans, carbon sulfide, or carbonyl sulfide. The level of acid gas concentration in the sour gas is an important consideration for selecting the proper sweetening process. Some processes are applicable for removal of large quantities of acid gas, and other processes have the capacity for removing acid gas constituents to ppm range. This chapter covers the minimum process requirements, criteria, and features for accomplishment of process design of gas sweetening units. The basic principles for process design of main equipment, piping, and instrumentation together with guidelines on present developments and process selection in the gas sweetening process are the main objectives throughout this chapter.

Alireza Bahadori

2014-01-01T23:59:59.000Z

263

Current status of MHI CO2 capture plant technology, large scale demonstration project and road map to commercialization for coal fired flue gas application  

Science Journals Connector (OSTI)

(1) It is becoming increasingly evident that the prolonged utilization of fossil fuels for primary energy production, especially coal which is relatively cheap and abundant, is inevitable and that Carbon Capture and Storage (CCS) technology can significantly reduce CO2 emissions from this sector thus allowing the continued environmentally sustainable use of this important energy commodity on a global basis. (2) MHI has co-developed the Kansai Mitsubishi Carbon Dioxide Recovery Process (KM-CDR Process™) and KS-1™ absorbent, which has been deployed in seven CO2 capture plants, now under commercial operation operating at a CO2 capture capacity of 450 metric tons per day (tpd). In addition, a further two commercial plants are now under construction all of which capture CO2 from natural gas fired flue gas boilers and steam reformers. Accordingly this technology is now available for commercial scale CO2 capture for gas boiler and gas turbine application. (3) However before offering commercial CO2 capture plants for coal fired flue gas application, it is necessary to verify the influence of, and develop countermeasures for, related impurities contained in coal fired flue gas. This includes the influence on both the absorbent and the entire system of the CO2 capture plant to achieve high operational reliability and minimize maintenance requirements. (4) Preventing the accumulation of impurities, especially the build up of dust, is very important when treating coal fired flue gas and MHI has undertaken significant work to understand the impact of impurities in order to achieve reliable and stable operating conditions and to efficiently optimize integration between the CO2 capture plant, the coal fired power plant and the flue gas clean up equipment. (5) To achieve this purpose, MHI constructed a 10 tpd CO2 capture demonstration plant at the Matsushima 1000 MW Power Station and confirmed successful, long term demonstration following ?5000 hours of operation in 2006–07 with 50% financial support by RITE, as a joint program to promote technological development with the private sector, and cooperation from J-POWER. (6) Following successful demonstration testing at Matsushima, additional testing was undertaken in 2008 to examine the impact of entrainment of higher levels of flue gas impurities (primarily \\{SOx\\} and dust by bypassing the existing FGD) and to determine which components of the CO2 recovery process are responsible for the removal of these impurities. Following an additional 1000 demonstration hours, results indicated stable operational performance in relation to the following impurities; (1) SO2: Even at higher SO2 concentrations were almost completely removed from the flue gas before entering the CO2 absorber. (2) Dust: The accumulation of dust in the absorbent was higher, leading to an advanced understanding of the behavior of dust in the CO2 capture plant and the dust removal efficiency of each component within the CO2 recovery system. The data obtained is useful for the design of large-scale units and confirms the operating robustness of the CO2 capture plant accounting for wide fluctuations in impurity concentrations. (7) This important coal fired flue gas testing showed categorically that minimizing the accumulation of large concentrations of impurities, and to suppress dust concentrations below a prescribed level, is important to achieve long-term stable operation and to minimize maintenance work for the CO2 capture plant. To comply with the above requirement, various countermeasures have been developed which include the optimization of the impurity removal technology, flue gas pre treatment and improved optimization with the flue gas desulfurization facility. (8) In case of a commercial scale CO2 capture plant applied for coal fired flue gas, its respective size will be several thousand tpd which represents a considerable scale-up from the 10 tpd demonstration plant. In order to ensure the operational reliability and to accurately confirm the influence and the behavior of the impurities in coal fired fl

Takahiko Endo; Yoshinori Kajiya; Hiromitsu Nagayasu; Masaki Iijima; Tsuyoshi Ohishi; Hiroshi Tanaka; Ronald Mitchell

2011-01-01T23:59:59.000Z

264

Historical Natural Gas Annual  

Gasoline and Diesel Fuel Update (EIA)

6 6 The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-1996 and detailed annual historical information by State for 1967-1996. The Historical Natural Gas Annual tables are available as self-extracting executable files in ASCII TXT or CDF file formats. Tables 1-3 present annual historical data at the national level for 1930-1996. The remaining tables contain detailed annual historical information, by State, for 1967-1996. Please read the file entitled READMEV2 for a description and documentation of information included in this file.

265

Historical Natural Gas Annual  

Gasoline and Diesel Fuel Update (EIA)

7 7 The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-1997 and detailed annual historical information by State for 1967-1997. The Historical Natural Gas Annual tables are available as self-extracting executable files in ASCII TXT or CDF file formats. Tables 1-3 present annual historical data at the national level for 1930-1997. The remaining tables contain detailed annual historical information, by State, for 1967-1997. Please read the file entitled READMEV2 for a description and documentation of information included in this file.

266

Historical Natural Gas Annual  

Gasoline and Diesel Fuel Update (EIA)

8 8 The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-1998 and detailed annual historical information by State for 1967-1998. The Historical Natural Gas Annual tables are available as self-extracting executable files in ASCII TXT or CDF file formats. Tables 1-3 present annual historical data at the national level for 1930-1998. The remaining tables contain detailed annual historical information, by State, for 1967-1998. Please read the file entitled READMEV2 for a description and documentation of information included in this file.

267

United States  

Office of Legacy Management (LM)

Office of Research and EPA 600/R-941209 Environmental Protection Development January 1993 Agency Washington, DC 20460 Offsite Environmental 57,,7 Monitoring Report Radiation Monitoring Around United States Nuclear Test Areas, Calendar Year 1992 UNITED STATES ENVIRONMENTAL PROTECTION AGENCY OFFICE OF RESEARCH AND DEVELOPMENT ENVIRONMENTAL MONITORING SYSTEMS LABORATORY-LAS VEGAS P.O. BOX 93478 LAS VEGAS. NEVADA 891 93-3478 702/798-2100 Dear Reader: Since 1954, the U.S. Environmental Protection Agency (EPA) and its predecessor the U.S, Public Health Service (PHs) has conducted radiological monitoring in the offsite areas around United States nuclear test areas. The primary objective of this monitoring has been the protection of the health and safety of

268

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

BP Energy Company BP Energy Company OE Docket No. EA- 3 14 Order Authorizing Electricity Exports to Mexico Order No. EA-3 14 February 22,2007 BP Energy Company Order No. EA-314 I. BACKGROUND Exports of electricity from the United States to a foreign country are regulated by the Department of Energy (DOE) pursuant to sections 301(b) and 402(Q of the Department of Energy Organization Act (42 U.S.C. 7 15 l(b), 7172(f)) and require authorization under section 202(e) of the Federal Power Act (FPA) (16 U.S.C.S24a(e)) . On May 22,2006, BP Energy Company (BP Energy) applied to DOE for an authorization to transmit electric energy from the United States to Mexico as a power marketer. BP Energy proposes to purchase surplus electric energy from electric utilities and other suppliers within the United States and to export that energy to ~Mexico. The cnergy

269

EIA - Natural Gas Pipeline Network - Underground Natural Gas Storage  

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

Storage Storage About U.S. Natural Gas Pipelines - Transporting Natural Gas based on data through 2007/2008 with selected updates Underground Natural Gas Storage Overview | Regional Breakdowns Overview Underground natural gas storage provides pipelines, local distribution companies, producers, and pipeline shippers with an inventory management tool, seasonal supply backup, and access to natural gas needed to avoid imbalances between receipts and deliveries on a pipeline network. There are three principal types of underground storage sites used in the United States today. They are: · depleted natural gas or oil fields (326), · aquifers (43), or · salt caverns (31). In a few cases mine caverns have been used. Most underground storage facilities, 82 percent at the beginning of 2008, were created from reservoirs located in depleted natural gas production fields that were relatively easy to convert to storage service, and that were often close to consumption centers and existing natural gas pipeline systems.

270

Oil and Gas Supply Module  

Gasoline and Diesel Fuel Update (EIA)

States, acquire natural gas from foreign producers for resale States, acquire natural gas from foreign producers for resale in the United States, or sell U.S. gas to foreign consumers. OGSM encompasses domestic crude oil and natural gas supply by both conventional and nonconventional recovery techniques. Nonconventional recovery includes unconventional gas recovery from low permeability formations of sandstone and shale, and coalbeds. Foreign gas transactions may occur via either pipeline (Canada or Mexico) or transport ships as liquefied natural gas (LNG). Energy Information Administration/Assumptions to the Annual Energy Outlook 2006 89 Figure 7. Oil and Gas Supply Model Regions Source: Energy Information Administration, Office of Integrated Analysis and Forecasting. Report #:DOE/EIA-0554(2006) Release date: March 2006

271

Natural Gas  

Science Journals Connector (OSTI)

30 May 1974 research-article Natural Gas C. P. Coppack This paper reviews the world's existing natural gas reserves and future expectations, together with natural gas consumption in 1972, by main geographic...

1974-01-01T23:59:59.000Z

272

EIA - Natural Gas Pipeline Network - Natural Gas Imports/Exports Pipelines  

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

Pipelines Pipelines About U.S. Natural Gas Pipelines - Transporting Natural Gas based on data through 2007/2008 with selected updates Natural Gas Import/Export Pipelines As of the close of 2008 the United States has 58 locations where natural gas can be exported or imported. 24 locations are for imports only 18 locations are for exports only 13 locations are for both imports and exports 8 locations are liquefied natural gas (LNG) import facilities Imported natural gas in 2007 represented almost 16 percent of the gas consumed in the United States annually, compared with 11 percent just 12 years ago. Forty-eight natural gas pipelines, representing approximately 28 billion cubic feet (Bcf) per day of capacity, import and export natural gas between the United States and Canada or Mexico.

273

United States  

Office of Legacy Management (LM)

WASHINGTON, TUESDAY, JUNE 28, 1983 @nngmeional Ruord United States of America .__ -- . . ,- PROCEEDINGS AND DEBATES OF THE 9@ CONGRESS, FIRST SESSION United States Government Printing Office SUPERINTENDENT OF DOCUMENTS Washmgton, D C 20402 OFFICIAL BUSINESS Penalty Ior pwate use. $xX Congresstonal Record (USPS 087-390) Postage and Fees Pad U S Government Prlnhng 0ffv.X 375 SECOND CLASS NEWSPAPER H.4578 ' C.QNGRESSIONAL RECORD - HOUSE June 28, 1983 H.J. Res. 273: Mr. BOUND. Mr. W~.XMAN. Mr. OBERSTAR, Mr. BEDELL. Mr. BONER of Tennessee, Mr. OWENS. Mr. DAUB, Mr. CONTE. Mr. RAHALL; Mr. GRAY, Mr. VANDER JACT. Mr. TRAKLER, and Mr. Vxrrro. H. Con. Res. 107: Mr. KASICH. Mr. AUCOIN. Mr. CARPER, and Mr. SIZHFIJER. H. Con. Res. 118: Mr. FISH. Mr. LANTOS.

274

United States  

Office of Legacy Management (LM)

ongrees;ional Record ongrees;ional Record United States of America __._ -.. I. :- PROCEEDINGS AND DEBATES OF THE 9tth CONGRESS, FIRST SESSION United States Government Printing Office SUPERINTENDENT OF DOCUMENTS Washmcqton. Cl C 20402 OFFICIAL BUSINESS Penalty Ior pwate use. $300 Congressmal Record (USPS 087-390) Postage and Fees Pad U S Governme3n:jPnntmg OfIce SECOND CLASS NEWSPAPER H.4578 ' June 28, 1983 -: I H.J. Res. 273: Mr. BOLAND, Mr. WA-. Mr. OBERSTAFC, M' r. BEDELL, Mr. BONER of Tennessee, Mr. OWENS. Mr. DAUB. Mr. CONTE. Mr. RAHALL,. Mr. GRAY, Mr. VANDER JAGT. Mr. TRAKLER. and Mr. VENTO. H. Con. Res. iO7: Mr. KASICH. Mr. ALCOIN. Mr. CARPER. and Mr. SCHEUER. H. Con. Res. 118: Mr. FISH, Mr. LANTOS. Mr. KILDEE. Mr. SOLARZ Mr. Bmrr, Mr. BELWLL, Mr. RANG~L, Mr. DYMALLY. Mr.

275

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

E-T Global Energy, LLC E-T Global Energy, LLC OE Docket No. EA-381 Order Authorizing Electricity Exports to Mexico Order No. EA-381 June 10, 2011 I. BACKGROUND E-T Global Energy, LLC Order No. EA-381 Exports of electricity from the United States to a foreign country are regulated by the Department of Energy (DOE) pursuant to sections 301(b) and 402(f) of the Department ofEnergy Organization Act (42 U.S.C. 7151(b), 7172(f)) and require authorization under section 202(e) ofthe Federal Power Act (FPA) (16 U.S.C.824a(e)) 1 * On May 10,2011, DOE received an application from E-T Global Energy, LLC (E-T Global) for authority to transmit electric energy from the United States to Mexico for five years as a power marketer using existing international transmission facilities. E-

276

Response of Different Types of Sulfur Compounds to Oxidative Desulfurization of Jet Fuel  

Science Journals Connector (OSTI)

Michael T. Timko *†, Ezequiel Schmois ‡, Pushkaraj Patwardhan ‡, Yuko Kida ‡, Caleb A. Class ‡, William H. Green ‡, Robert K. Nelson §, and Christopher M. Reddy § ... Refer to ref 3 for a summary of our previous efforts to identify specific BT isomers in jet fuel using one-dimensional gas chromatography and mass spectrometry (GC–MS), and ref 44 provides even greater detail. ... We then analyzed the JP-8 samples using GC×GC–SCD to resolve the UCM and identify specific compound classes within it. ...

Michael T. Timko; Ezequiel Schmois; Pushkaraj Patwardhan; Yuko Kida; Caleb A. Class; William H. Green; Robert K. Nelson; Christopher M. Reddy

2014-04-24T23:59:59.000Z

277

Investigation of the effects of various water mediums on desulfurization and deashing of a coal sample by flotation  

SciTech Connect

The aim of this study was to investigate the effects of various water mediums on desulfurization and deashing of a coal sample using flotation. For this purpose, experimental studies were conducted on a coal sample containing high ash and sulfur contents. The effects of pH, solid concentration, collector amount and frother amount on the flotation were investigated separately in Mediterranean Sea water, Cermik thermal spring water, snow water and tap water. Flotation, results indicated that, when comparing the various water mediums, the following order for the ash content was obtained: snow water < Cermik thermal spring water < tap water < the Mediterranean Sea water. For the reduction of total sulfur, the following order was obtained: snow water > Cermik thermal spring water > Mediterranean Sea water > tap water. When snow water was used as a flotation medium, it was found that a concentrate containing 3.01% total sulfur and 27.64% ash with a total sulfur reduction of 57.06% was obtained from a feed containing 7.01% total sulfur and 4.1.17% ash.

Ayhan, F.D. [Dicle University, Diyarbakir (Turkey)

2009-08-15T23:59:59.000Z

278

Desulfurization and de-ashing of a mixture of subbituminous coal and gangue minerals by selective oil agglomeration  

SciTech Connect

The aim of this study was to investigate desulfurization and de-ashing of a mixture of subbituminous coal and gangue minerals by the agglomeration method. For this purpose, experimental studies were conducted on a mixture containing subbituminous coal, pyrite, quartz and calcite. The effects of some parameters that markedly influence the effectiveness of selective oil agglomeration, such as solid concentration, pH, bridging liquid type and concentration, and depressant type and amount, were investigated. Agglomeration results showed that the usage of various depressants (Na{sub 2}SiO{sub 3}, FeCl3, corn starch, wheat starch) in the agglomeration medium has a positive effect on the reduction of ash and total sulfur content of agglomerates. It was found that an agglomerate product containing 3.03% total sulfur and 25.01% ash with a total sulfur reduction of 56.71% was obtained from a feed that contained 7% total sulfur and 43.58% ash when FeCl{sub 3} was used in the agglomeration medium.

Ayhan, F.D. [Dicle University, Diyarbakir (Turkey). Dept. of Mining Engineering

2009-11-15T23:59:59.000Z

279

Adsorptive desulfurization of low sulfur diesel fuel using palladium containing mesoporous silica synthesized via a novel in-situ approach  

Science Journals Connector (OSTI)

Abstract In this work, a novel in-situ synthesis route was applied for preparation of an adsorbent, i.e. palladium containing MCM-41. At first, a hydrophobic palladium precursor was added to the ethanolic micellar solution followed by vacuum distillation of ethanol which decreases the hydrophobic characteristic of the solution. Distillation caused diffusion of hydrophobic palladium precursor into the hydrophobic core of the micelles. Then, tetraethyl orthosilicate was added to the above solution and the silicate spices arranged around the palladium containing micelles. The XRD, N2 physisorption and TEM studies revealed that 4 wt.% palladium loading was achieved without considerable loss of pore ordering. H2-TPR showed that the palladium nanoparticles were accessible for hydrogen molecules. Adsorptive desulfurization of low sulfur diesel fuel was then investigated using synthesized samples. The effect of three valuable parameters, i.e., temperature (25, 75, 150 and 200 °C), concentration of palladium (2, 4 and 5 wt.%) and feed flow rate (0.3 and 1 mL/min) were tested using a fixed-bed flowing device. The highest sulfur break through adsorption capacity and total sulfur adsorption capacity obtained at 200 °C, 0.3 mL/min of feed flow rate and 4 wt.% of palladium concentration were 1.67 and 2.35 mg sulfur/g adsorbent, respectively.

Mohammad Teymouri; Abdolraouf Samadi-Maybodi; Amir Vahid; Aliakbar Miranbeigi

2013-01-01T23:59:59.000Z

280

Total Petroleum Systems and Assessment Units (AU)  

E-Print Network (OSTI)

Total Petroleum Systems (TPS) and Assessment Units (AU) Field type Surface water Groundwater X X X X X X X X AU 00000003 Oil/ Gas X X X X X X X X Total X X X X X X X Total Petroleum Systems (TPS) and Assessment Units (AU) Field type Total undiscovered petroleum (MMBO or BCFG) Water per oil

Torgersen, Christian

Note: This page contains sample records for the topic "gas desulfurization units" 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

Montana-Dakota Utilities (Gas) - Commercial Natural Gas Efficiency Rebate  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

(Gas) - Commercial Natural Gas Efficiency (Gas) - Commercial Natural Gas Efficiency Rebate Program Montana-Dakota Utilities (Gas) - Commercial Natural Gas Efficiency Rebate Program < Back Eligibility Commercial Savings Category Other Heating & Cooling Commercial Heating & Cooling Heating Program Info State South Dakota Program Type Utility Rebate Program Rebate Amount Furnace: $150 - $300 Custom: Varies by project Provider Montana-Dakota Utilities Co. Montana-Dakota Utilities (MDU) offers rebates on energy efficient natural gas furnaces to its eligible commercial customers. New furnaces are eligible for a rebate incentive between $150 and $300, if the equipment meets program efficiency standards. Furnaces with AFUE between 92% of 95% are eligible for rebates if they are being installed as replacement units

282

Impacts of Imported Liquefied Natural Gas on Residential Appliance Components: Literature Review  

E-Print Network (OSTI)

of Interchangeability of Vaporized LNG and Natural Gas. Deswith Domestic Natural Gas. LNG and the Changing U.S. NaturalInterchangeability, and LNG Utilization in the United

Lekov, Alex

2010-01-01T23:59:59.000Z

283

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

9, 2011 at 2:00 P.M. 9, 2011 at 2:00 P.M. Next Release: Thursday, June 16, 2011 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (For the Week Ending Wednesday, June 8, 2011) Natural gas prices rose on the week across the board, with somewhat moderate increases in most areas and steep increases in the Northeast United States. The Henry Hub spot price rose 20 cents on the week from $4.63 per million Btu (MMBtu) last Wednesday, June 1, to $4.83 per MMBtu yesterday. At the New York Mercantile Exchange, the price of the near-month (July 2011) contract rose about 5 percent, from $4.692 last Wednesday to $4.847 yesterday. Working natural gas in storage rose to 2,187 billion cubic feet (Bcf) as of Friday, June 3, according to EIAÂ’s Weekly Natural Gas Storage

284

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

3, 2008 3, 2008 Next Release: October 30, 2008 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (For the week ending Wednesday, October 22) Natural gas spot prices in the Lower 48 States this report week increased as a result of cold weather in some major gas consuming areas of the country, several ongoing pipeline maintenance projects, and the continuing production shut-ins in the Gulf of Mexico region. At the New York Mercantile Exchange (NYMEX), the price of the near-month contract (November 2008) increased on the week to $6.777 per million British thermal units (MMBtu) as of yesterday (October 22). The net weekly increase occurred during a week in which the price increased in three trading sessions. As of Friday, October 17, working gas in underground storage totaled

285

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

2, 2011 at 2:00 P.M. 2, 2011 at 2:00 P.M. Next Release: Thursday, September 29, 2011 Overview Prices Storage Other Market Trends Overview (For the Week Ending Wednesday, September 21, 2011) Natural gas spot prices declined at most market locations across the United States, as moderate temperatures led to declines in demand. Prices at the Henry Hub fell from $4.01 per MMBtu last Wednesday, September 14, to $3.78 per MMBtu yesterday. At the New York Mercantile Exchange, the price of the near-month futures contract (October 2011) dropped from $4.039 per MMBtu last Wednesday to $3.73 per MMBtu yesterday. Working natural gas in storage rose to 3,201 billion cubic feet (Bcf) as of Friday, September 16, according to EIAÂ’s Weekly Natural Gas Storage Report (WNGSR). The natural gas rotary rig count, as reported by Baker Hughes

286

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

5 5 United States Department of Energy Southeastern Power Administration Wholesale Power Rate Schedule CC-1-I Availability: This rate schedule shall be available to public bodies and cooperatives served through the facilities of Carolina Power & Light Company, Western Division (hereinafter called the Customers). Applicability: This rate schedule shall be applicable to electric capacity and energy available from the Dale Hollow, Center Hill, Wolf Creek, Cheatham, Old Hickory, Barkley, J. Percy Priest, and Cordell Hull Projects (all of such projects being hereinafter called collectively the "Cumberland Projects") and sold in wholesale quantities. Character of Service: The electric capacity and energy supplied hereunder will be three-phase alternating

287

Proceedings of the 1st Annual Gas Processing Symposium  

E-Print Network (OSTI)

pretreatment units, a gas-fired power plant, a CO2 separation unit and storage tanks. LNG and condensateProceedings of the 1st Annual Gas Processing Symposium H. Alfadala, G.V. Rex Reklaitis and M.M. El. An example of the latter arises if part of the gas output from the separation plant is fed back

Foss, Bjarne A.

288

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

TexMex Energy, LLC TexMex Energy, LLC OE Docket No. EA-294-A Order Authorizing Electricity Exports to Mexico Order No. EA-294-A February 22, 2007 TexMex Energy, LLC Order No. EA-294-A I. BACKGROUND Exports of electricity from the United States to a foreign count~y are regulated by the Department of Energy (DOE) pursuant to sections 301(b) and 402(f) of the Department of Energy Organization Act (42 U.S.C. 7 15 1 (b), 71 72(f)) and require authorization under section 202(e) of the Federal Power Act (FPA) (16 U.S.C.824a(e)) . On August 25,2004, DOE issued Order No. EA-294 authorizing TexMex Energy LLC (TexMex) to transmit electric energy fiom the United States to Mexico as a power marketer. That authority expired on August 25, 2006. On September 8, 2006, TexMex applied to renew the electricity export authority

289

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Tenaslta Power Services Co. Tenaslta Power Services Co. OE Docket No. EA-243-A Order Authorizing Electricity Exports to Canada Order No. EA-243-A March 1,2007 Tenaska Power Services Co. Order No. EA-243-A I. BACKGROUND Exports of elcctricity from the United States to a foreign country are regulated by the Department of Energy (DOE) pursuant to sections 30 I(b) and 402(f) of the Departrncnt of' Energy Organizatio~l Act (42 U, S.C. 7 15 1 (b), 7 1 72Cf)) and rcquirc authorization under section 202(e) of the Federal Power Act (FPA) ( Z 6 U. s.c.824a(e)j1. On August 16,2001, DOE issued Order No. EA-243 authorizing Tenaska Power Scrvices Co. (Tenaska) to transmit electric cncrgy from the United States to Canada as a power marketer. That authority expired on August 16,2003. On August 14,2006, Teilaska applied to renew the electricity export authority

290

NETL: Gasification Systems - Integrated Warm Gas Multicontaminant Cleanup  

NLE Websites -- All DOE Office Websites (Extended Search)

Integrated Warm Gas Multicontaminant Cleanup Technologies for Coal-Derived Syngas Integrated Warm Gas Multicontaminant Cleanup Technologies for Coal-Derived Syngas Project Number: DE-FC26-05NT42459 Integrated Warm Gas Multicontaminant Cleanup Technologies for Coal-Derived Syngas Project ID: DE-FC26-05NT42459 Objective: The objective is to develop a warm multi-contaminant syngas cleaning system for operation between 300 and 700° F. This project will continue development of the RTI warm syngas cleanup technology suite. Based on the field testing results with real syngas from Eastman Chemical Company's gasifier under DOE Contract DE-AC26-99FT40675, additional technical issues need to be addressed to move the technologies used in warm syngas cleaning further towards commercial deployment especially for chemical/fuels production. These issues range from evaluation of startup and standby options for the more developed desulfurization processes to integration and actual pilot plant testing with real coal-derived syngas for the technologies that were tested at bench scale during Phase I. Development shall continue of the warm gas syngas cleaning technology platform through a combination of lab-scale R&D and larger integrated pilot plant testing with real coal-derived syngas as well as process/systems analysis and simulation for optimization of integration and intensification.

291

Barriers to the increased utilization of coal combustion/desulfurization by-products by government & commercial sectors - update 1998,7/99,3268845  

NLE Websites -- All DOE Office Websites (Extended Search)

BARRIERS TO THE INCREASED UTILIZATION BARRIERS TO THE INCREASED UTILIZATION OF COAL COMBUSTION/DESULFURIZATION BY-PRODUCTS BY GOVERNMENT AND COMMERCIAL SECTORS - UPDATE 1998 EERC Topical Report DE-FC21-93MC-30097--79 Submitted by: Debra F. Pflughoeft-Hassett Everett A. Sondreal Edward N. Steadman Kurt E. Eylands Bruce A. Dockter Energy & Environmental Research Center PO Box 9018 Grand Forks, ND 58202-9018 99-EERC-07-08 July 1999 i TABLE OF CONTENTS LIST OF FIGURES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . iv LIST OF TABLES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . v ACKNOWLEDGMENTS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . vi LIST OF ACRONYMS AND ABBREVIATIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . vii TERMINOLOGY AND DEFINITIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . .

292

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

2-E 2-E Availability: This rate schedule shall be available public bodies and cooperatives (any one of which is hereinafter called the Customer) in South Carolina to whom power may be wheeled pursuant to contracts between the Government and the South Carolina Electric & Gas Company (hereinafter called the Company). The customer is responsible for providing a scheduling arrangement with the Government. Nothing in this rate schedule shall preclude an eligible customer from electing service under another rate schedule. Applicability: This rate schedule shall be applicable to the sale at wholesale of power and accompanying energy generated at the Allatoona, Buford, J. Strom Thurmond, Walter F. George, Hartwell, Millers Ferry, West Point, Robert F. Henry, Carters and Richard B.

293

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

4-E 4-E Availability: This rate schedule shall be available public bodies and cooperatives (any one of which is hereinafter called the Customer) in South Carolina served through the transmission facilities of South Carolina Electric & Gas Company (hereinafter called the Company). The customer is responsible for providing a scheduling arrangement with the Government and for providing a transmission arrangement. Nothing in this rate schedule shall preclude an eligible customer from electing service under another rate schedule. Applicability: This rate schedule shall be applicable to the sale at wholesale of power and accompanying energy generated at the Allatoona, Buford, J. Strom Thurmond, Walter F. George, Hartwell, Millers Ferry, West Point, Robert F. Henry, Carters and Richard B.

294

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

SCE&G-1-E SCE&G-1-E Availability: This rate schedule shall be available public bodies and cooperatives (any one of which is hereinafter called the Customer) in South Carolina to whom power may be wheeled and scheduled pursuant to contracts between the Government and the South Carolina Electric & Gas Company (hereinafter called the Company). Nothing in this rate schedule shall preclude an eligible customer from electing service under another rate schedule. Applicability: This rate schedule shall be applicable to the sale at wholesale of power and accompanying energy generated at the Allatoona, Buford, J. Strom Thurmond, Walter F. George, Hartwell, Millers Ferry, West Point, Robert F. Henry, Carters and Richard B. Russell Projects and sold under appropriate contracts between the Government and

295

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

7 7 United States Department of Energy Southeastern Power Administration Wholesale Power Rate Schedule CTV-1-H Availability: This rate schedule shall be available to the Tennessee Valley Authority (hereinafter called TVA). Applicability: This rate schedule shall be applicable to electric capacity and energy generated at the Dale Hollow, Center Hill, Wolf Creek, Old Hickory, Cheatham, Barkley, J. Percy Priest, and Cordell Hull Projects (all of such projects being hereafter called collectively the "Cumberland Projects") and the Laurel Project sold under agreement between the Department of Energy and TVA. Character of Service: The electric capacity and energy supplied hereunder will be three-phase alternating current at a frequency of approximately 60 hertz at the outgoing terminals of the Cumberland

296

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

United States Department of Energy Southeastern Power Administration Wholesale Power Rate Schedule CTVI-1-A Availability: This rate schedule shall be available to customers (hereinafter called the Customer) who are or were formerly in the Tennessee Valley Authority (hereinafter called TVA) service area. Applicability: This rate schedule shall be applicable to electric capacity and energy generated at the Dale Hollow, Center Hill, Wolf Creek, Old Hickory, Cheatham, Barkley, J. Percy Priest, and Cordell Hull Projects (all of such projects being hereafter called collectively the "Cumberland Projects") and the Laurel Project sold under agreement between the Department of Energy and the Customer. Character of Service: The electric capacity and energy supplied hereunder will be three-phase alternating

297

UNITED STATES  

Office of Legacy Management (LM)

f).~<~~ \--\c :y-,ai F p"- KG f).~<~~ \--\c :y-,ai F p"- KG WASHINOTDN 28.0. C. ' -lr ' \ ' ' --- ".I ?--" ' z I. .~;-4.' J frr*o& 2 ii, - - -4 70-147 LRL:JCD JAN !! 8 1958 Oregon Metallurgical Corporation P. 0. Box 484 Albany, Oregon Attention: Mr. Stephen M. Shelton General Manager Gentlemen: Enclosed is Special Nuclear Material License No. SNM-144, as amended. Very 33uly yours, r:; I,;, ll)~gQ""d".- Lyall Johnson Chief, Licensing Branch Division of Licensing & Regulation Enclosure: SNM-144, as amended Distribution: bRO0 Attn: Dr. H.M.Roth DFMusser NMM MMMann INS JCRyan FIN (2) HSteele LRL SRGustavson LRL Document room Formal file Suppl. file Br & Div rf's ' .b liwwArry s/VW- ' q+ ' yj/ 2; 2-' , COP' 1 J JAM01958 -- UNITED STATES ATOMIC ENERGY COMMISSION

298

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

United States Department of Energy Southeastern Power Administration Wholesale Power Rate Schedule JW-2-F Availability: This rate schedule shall be available to the Florida Power Corporation (or Progress Energy Florida, hereinafter called the Company). Applicability: This rate schedule shall be applicable to electric energy generated at the Jim Woodruff Project (hereinafter called the Project) and sold to the Company in wholesale quantities. Points of Delivery: Power sold to the Company by the Government will be delivered at the connection of the Company's transmission system with the Project bus. Character of Service: Electric power delivered to the Company will be three-phase alternating current at a nominal frequency of 60 cycles per second.

299

United States  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Bangor Hydro-Electric Company Bangor Hydro-Electric Company OE Docket No. PP-89-1 Amendment to Presidential Permit Order No. PP-89-1 December 30,2005 PRESIDENTIAL PERMIT AMENDMENT Bangor Hydro-Electric Company Order No. PP-89-1 I. BACKGROUND The Department of Energy (DOE) has responsibility for implementing Executive Order (E.O.) 10485, as amended by E.O. 12038, which requires the issuance of a Presidential permit by DOE before electric trans~nission facilities may be constructed, operated, maintained, or connected at the borders of the United States. DOE may issue such a permit if it determines that the permit is in the public interest and after obtaining favorable recommendations from the U.S. Departments of State and Defense. On December 16, 1988, Bangor Hydro-Electric Company (BHE) applied to DOE

300

Using high temperature baghouses to enhance desulfurization following economizer sorbent injection  

SciTech Connect

In order to explore the potential of using high temperature baghouses to enhance SO{sub 2} removal following upstream sorbent injection, an integrated two-stage reactor system has been built. It consists of an injection stage and a filtration stage. Distinct from one-stage fixed-bed reactors, sorbent particles in this system are initially converted under controlled injection conditions before entering the filtration reactor chamber. By the aid of the system, several unique features regarding the gas-solid reactions in the baghouse after economizer zone sorbent injection have been revealed. Results have shown that the appropriate usage of a high temperature baghouse may substantially enhance the performance of the process. The further SO{sub 2} removal in the baghouse is comprehensively affected by both the conditions in the injection zone and those in the baghouse.

Li, G.; Keener, T.C. [Univ. of Cincinnati, OH (United States). Dept. of Civil and Environmental Engineering

1995-12-31T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

CHEMICAL PROCESS RESEARCH AND DEVELOPMENT PROGRAM. Chapter from the Energy and Environment Division Annual Report 1980  

E-Print Network (OSTI)

removal is flue- gas desulfurization, Under investigation are fundamental chemistry and transport mechanisms underlying reagent additive

Authors, Various

2014-01-01T23:59:59.000Z

302

Gas Turbines  

Science Journals Connector (OSTI)

When the gas turbine generator was introduced to the power generation ... fossil-fueled power plant. Twenty years later, gas turbines were established as an important means of ... on utility systems. By the early...

Jeffrey M. Smith

1996-01-01T23:59:59.000Z

303

EIA - Natural Gas Pipeline Network - Major Natural Gas Transportation  

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

Natural Gas Transportation Corridors Natural Gas Transportation Corridors About U.S. Natural Gas Pipelines - Transporting Natural Gas based on data through 2007/2008 with selected updates Major Natural Gas Transportation Corridors Corridors from the Southwest | From Canada | From Rocky Mountain Area | Details about Transportation Corridors The national natural gas delivery network is intricate and expansive, but most of the major transportation routes can be broadly categorized into 11 distinct corridors or flow patterns. 5 major routes extend from the producing areas of the Southwest 4 routes enter the United States from Canada 2 originate in the Rocky Mountain area. A summary of the major corridors and links to details about each corridor are provided below. Corridors from the Southwest Region

304

Gas Storage Technology Consortium  

SciTech Connect

Gas storage is a critical element in the natural gas industry. Producers, transmission and distribution companies, marketers, and end users all benefit directly from the load balancing function of storage. The unbundling process has fundamentally changed the way storage is used and valued. As an unbundled service, the value of storage is being recovered at rates that reflect its value. Moreover, the marketplace has differentiated between various types of storage services and has increasingly rewarded flexibility, safety, and reliability. The size of the natural gas market has increased and is projected to continue to increase towards 30 trillion cubic feet (TCF) over the next 10 to 15 years. Much of this increase is projected to come from electric generation, particularly peaking units. Gas storage, particularly the flexible services that are most suited to electric loads, is crucial in meeting the needs of these new markets. To address the gas storage needs of the natural gas industry, an industry-driven consortium was created - the Gas Storage Technology Consortium (GSTC). The objective of the GSTC is to provide a means to accomplish industry-driven research and development designed to enhance the operational flexibility and deliverability of the nation's gas storage system, and provide a cost-effective, safe, and reliable supply of natural gas to meet domestic demand. This report addresses the activities for the quarterly period of January1, 2007 through March 31, 2007. Key activities during this time period included: {lg_bullet} Drafting and distributing the 2007 RFP; {lg_bullet} Identifying and securing a meeting site for the GSTC 2007 Spring Proposal Meeting; {lg_bullet} Scheduling and participating in two (2) project mentoring conference calls; {lg_bullet} Conducting elections for four Executive Council seats; {lg_bullet} Collecting and compiling the 2005 GSTC Final Project Reports; and {lg_bullet} Outreach and communications.

Joel L. Morrison; Sharon L. Elder

2007-03-31T23:59:59.000Z

305

Gas Storage Technology Consortium  

SciTech Connect

Gas storage is a critical element in the natural gas industry. Producers, transmission and distribution companies, marketers, and end users all benefit directly from the load balancing function of storage. The unbundling process has fundamentally changed the way storage is used and valued. As an unbundled service, the value of storage is being recovered at rates that reflect its value. Moreover, the marketplace has differentiated between various types of storage services and has increasingly rewarded flexibility, safety, and reliability. The size of the natural gas market has increased and is projected to continue to increase towards 30 trillion cubic feet over the next 10 to 15 years. Much of this increase is projected to come from electric generation, particularly peaking units. Gas storage, particularly the flexible services that are most suited to electric loads, is crucial in meeting the needs of these new markets. To address the gas storage needs of the natural gas industry, an industry-driven consortium was created--the Gas Storage Technology Consortium (GSTC). The objective of the GSTC is to provide a means to accomplish industry-driven research and development designed to enhance the operational flexibility and deliverability of the nation's gas storage system, and provide a cost-effective, safe, and reliable supply of natural gas to meet domestic demand. This report addresses the activities for the quarterly period of April 1, 2007 through June 30, 2007. Key activities during this time period included: (1) Organizing and hosting the 2007 GSTC Spring Meeting; (2) Identifying the 2007 GSTC projects, issuing award or declination letters, and begin drafting subcontracts; (3) 2007 project mentoring teams identified; (4) New NETL Project Manager; (5) Preliminary planning for the 2007 GSTC Fall Meeting; (6) Collecting and compiling the 2005 GSTC project final reports; and (7) Outreach and communications.

Joel L. Morrison; Sharon L. Elder

2007-06-30T23:59:59.000Z

306

Gas Turbines  

Science Journals Connector (OSTI)

... the time to separate out the essentials and the irrelevancies in a text-book. The gas ...gasturbine ...

H. CONSTANT

1950-10-21T23:59:59.000Z

307

" Million Housing Units, Final"  

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

Fuels Used and End Uses in U.S. Homes, by Housing Unit Type, 2009" Fuels Used and End Uses in U.S. Homes, by Housing Unit Type, 2009" " Million Housing Units, Final" ,,"Housing Unit Type" ,,"Single-Family Units",,"Apartments in Buildings With" ,"Total U.S.1 (millions)" ,," Detached"," Attached"," 2 to 4 Units","5 or More Units","Mobile Homes" "Fuels Used and End Uses" "Total Homes",113.6,71.8,6.7,9,19.1,6.9 "Fuels Used for Any Use" "Electricity",113.6,71.8,6.7,9,19.1,6.9 "Natural Gas",69.2,45.6,4.7,6.1,11,1.8 "Propane/LPG",48.9,39.6,2.4,1.7,2,3.2 "Wood",13.1,11.4,0.3,0.2,0.5,0.7 "Fuel Oil",7.7,5.1,0.4,0.7,1.3,0.1

308

New packing in absorption systems for trapping benzene from coke-oven gas  

SciTech Connect

The efficiency of benzene removal from coke-oven gas in absorption units OAO Alchevskkoks with new packing is assessed.

V.V. Grabko; V.M. Li; T.A. Shevchenko; M.A. Solov'ev [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

309

Energy Resources Available to the United States, 1985 to 2000  

Science Journals Connector (OSTI)

...a point, we can substitute mon-ey in the...4 a ton, and natural gas at /$0.16 a...world petroleum and gas produc-tion has...Btu's); and Syngas he United States...Btu's. Alaskan natural gas will cost $4 to...

Earl T. Hayes

1979-01-19T23:59:59.000Z

310

United States Government Memorandum  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Department of Energy Department of Energy United States Government Memorandum DATE: March 21, 2008 Audit Report Number: OAS-L-08-08 REPLY TO ATTN OF: IG-321 (A07LV042) SUBJECT: Audit Report on "Accountability of Sensitive and High Risk Property at the Nevada Site Office" TO: Acting Manager, Nevada Site Office INTRODUCTION AND OBJECTIVE and control over sensitive and high risk property because of the vulnerability to loss, theft or misuse and its potential impact on national security interests or proliferation concerns. Items such as portable and desktop computers, ammunition. and firearms are examples of sensitive property. In addition, federal regulations require that Departmental organizations and designated contractors account for and control govemroent-owned high risk property, such as body armor and gas masks,

311

What is shale gas and why is it important?  

Reports and Publications (EIA)

Shale gas refers to natural gas that is trapped within shale formations. Shales are fine-grained sedimentary rocks that can be rich sources of petroleum and natural gas. Over the past decade, the combination of horizontal drilling and hydraulic fracturing has allowed access to large volumes of shale gas that were previously uneconomical to produce. The production of natural gas from shale formations has rejuvenated the natural gas industry in the United States.

2012-01-01T23:59:59.000Z

312

Water management technologies used by Marcellus Shale Gas Producers.  

SciTech Connect

Natural gas represents an important energy source for the United States. According to the U.S. Department of Energy's (DOE's) Energy Information Administration (EIA), about 22% of the country's energy needs are provided by natural gas. Historically, natural gas was produced from conventional vertical wells drilled into porous hydrocarbon-containing formations. During the past decade, operators have increasingly looked to other unconventional sources of natural gas, such as coal bed methane, tight gas sands, and gas shales.

Veil, J. A.; Environmental Science Division

2010-07-30T23:59:59.000Z

313

Termination unit  

DOE Patents (OSTI)

This invention relates to a termination unit comprising an end-section of a cable. The end section of the cable defines a central longitudinal axis and comprising end-parts of N electrical phases, an end-part of a neutral conductor and a surrounding thermally insulation envelope adapted to comprising a cooling fluid. The end-parts of the N electrical phases and the end-part of the neutral conductor each comprising at least one electrical conductor and being arranged in the cable concentrically around a core former with a phase 1 located relatively innermost, and phase N relatively outermost in the cable, phase N being surrounded by the neutral conductor, electrical insulation being arrange between neighboring electrical phases and between phase N and the neutral conductor, and wherein the end-parts of the neutral conductor and the electrical phases each comprise a contacting surface electrically connected to at least one branch current lead to provide an electrical connection: The contacting surfaces each having a longitudinal extension, and being located sequentially along the longitudinal extension of the end-section of the cable. The branch current leads being individually insulated from said thermally insulation envelope by individual electrical insulators.

Traeholt, Chresten [Frederiksberg, DK; Willen, Dag [Klagshamn, SE; Roden, Mark [Newnan, GA; Tolbert, Jerry C [Carrollton, GA; Lindsay, David [Carrollton, GA; Fisher, Paul W [Heiskell, TN; Nielsen, Carsten Thidemann [Jaegerspris, DK

2014-01-07T23:59:59.000Z

314

EIA - Natural Gas Year-In-Review 2009  

Annual Energy Outlook 2012 (EIA)

9 Natural Gas Year-In-Review 2009 Released: July 2010 Next Release: November 2011 This report provides an overview of the natural gas industry and markets in the United States in...

315

Task Order Awarded to Small Business for Natural Gas Services...  

Office of Environmental Management (EM)

Pike Natural Gas, located in Hillsboro, Ohio for natural gas services. A firm fixed unit rate task order will be awarded with a not to exceed amount of 5.250 million value and a...

316

Natural gas pricing in the Northeastern U.S.  

E-Print Network (OSTI)

This paper examines natural gas pricing at five citygate locations in the northeastern United States using daily and weekly price series for the years 1994-97. In particular, the effects of the natural gas price at Henry ...

Gunnarshaug, Jasmin

1998-01-01T23:59:59.000Z

317

Reduced Nitrogen and Natural Gas Consumption at Deepwell Flare  

E-Print Network (OSTI)

Facing both an economic downturn and the liklihood of steep natural gas price increases, company plants were challenged to identify and quickly implement energy saving projects that would reduce natural gas usage. Unit operating personnel...

Williams, C.

2004-01-01T23:59:59.000Z

318

Blending Hydrogen into Natural Gas Pipeline Networks: A Review...  

Energy Savers (EERE)

Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues The United States has 11...

319

A Microscale Gas Trapping Investigation Markus Buchgraber, Anthony R. Kovscek  

E-Print Network (OSTI)

A Microscale Gas Trapping Investigation Markus Buchgraber, Anthony R. Kovscek Department of Energy unit Residual Trapping Sgi Sg,max krg krg Sgt(Soi) Sgt,max Gas Saturation Gas relative Land Model * * ** 1 )( gi gi gigt CS S SS + = Sgf Sg Sgt,max kd rg Sg Gas Saturation

Stanford University

320

Impact of Natural Gas Infrastructure on Electric Power Systems  

E-Print Network (OSTI)

Impact of Natural Gas Infrastructure on Electric Power Systems MOHAMMAD SHAHIDEHPOUR, FELLOW, IEEE of electricity has introduced new risks associated with the security of natural gas infrastructure on a sig the essence of the natural gas infrastructure for sup- plying the ever-increasing number of gas-powered units

Fu, Yong

Note: This page contains sample records for the topic "gas desulfurization units" 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

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

9, 2010 at 2:00 P.M. 9, 2010 at 2:00 P.M. Next Release: Thursday, December 16, 2010 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (For the Week Ending Wednesday, December 8, 2010) In response to cold weather across much of the United States, natural gas spot prices increased across the board this report week (December 1 – December 8). Though most increases were less than 50 cents per million Btu (MMBtu), prices at a number of trading points (notably in the Northeast and Florida) increased by several dollars. The Henry Hub spot price rose 25 cents, from $4.21 per MMBtu to $4.46 per MMBtu. At the New York Mercantile Exchange (NYMEX), the price of the natural gas near-month contract (January 2011) also increased, rising from $4.269 per MMBtu on December 1 to $4.606 per MMBtu on December 8.

322

Natural Gas Annual, 1998  

Gasoline and Diesel Fuel Update (EIA)

8 8 Historical The Natural Gas Annual, 1998 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 1998. Summary data are presented for each Census Division and State for 1994 to 1998. A section of historical data at the National level shows industry activities back to the 1930's. The data that appear in the tables of the Natural Gas Annual, 1998 are available as self-extracting executable files in ASCII TXT or CDF file formats. This volume emphasizes information for 1998, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file.

323

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

6, 2011 at 2:00 P.M. 6, 2011 at 2:00 P.M. Next Release: Thursday, October 13, 2011 Overview Prices Storage Other Market Trends Overview (For the Week Ending Wednesday, October 5, 2011) Like autumn leaves floating down to earth, natural gas prices dropped decidedly from their $4 support branch this past week. In a whirlwind of generally unsupportive market fundamentals, the Henry Hub price closed down 25 cents for the week to $3.63 per million British thermal units (MMBtu) on October 5. At the New York Mercantile Exchange (NYMEX), the November 2011 natural gas contract dropped nearly 23 cents per MMBtu to close at $3.570 per MMBtu over the week. Working natural gas in storage rose last week to 3,409 billion cubic feet (Bcf) as of Friday, September 30, according to the U.S. Energy

324

Natural Gas Annual, 1997  

Gasoline and Diesel Fuel Update (EIA)

7 7 Historical The Natural Gas Annual, 1997 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 1997. Summary data are presented for each Census Division and State for 1993 to 1997. A section of historical data at the National level shows industry activities back to the 1930's. The data that appear in the tables of the Natural Gas Annual, 1997 are available as self-extracting executable files in ASCII TXT or CDF file formats. This volume emphasizes information for 1997, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file.

325

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

8, 2009 at 2:00 P.M. 8, 2009 at 2:00 P.M. Next Release: October 15, 2009 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (For the Week Ending Wednesday, October 7, 2009) Since last Wednesday, September 30, natural gas prices rose across the board, with increases ranging between 37 cents and $1.32 per million Btu (MMBtu). Natural gas prices oscillated by large amounts at most market locations across the United States. The Henry Hub began the report week at $3.24 per MMBtu, fell to $2.32 on October 2, and ended trading yesterday at $3.70 per MMBtu. At the New York Mercantile Exchange (NYMEX), the near-month contract for November ended the week at $4.904 per MMBtu, a slight increase from the previous weekÂ’s value of $4.841 per MMBtu.

326

Gas turbine noise control  

Science Journals Connector (OSTI)

The use of gas turbine powered generators and pumping stations are likely to increase over the next two decades. Alternative fuel systems utilizing fluidized coal beds are likely in the near future and direct combustion of pulverized coal is also a possibility. The primary problem of generally unacceptable noise levels from gas turbine powered equipment affects both community noise and hearing conservation alike. The noise criteria of such plant remain a significant design factor. The paper looks at the technical and historical aspects associated with the noise generation process and examines past present and possible future approaches to the problem of silencing gas turbine units; adequately specifying the acoustical criteria and ratings; evaluates the techniques by which these criteria should be measured; and correlates these with the typical results achieved in the field.

Louis A. Challis and Associates Pty. Ltd.

1979-01-01T23:59:59.000Z

327

Colorado Natural Gas Number of Gas and Gas Condensate Wells ...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) Colorado Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

328

California Natural Gas Number of Gas and Gas Condensate Wells...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) California Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

329

Louisiana Natural Gas Number of Gas and Gas Condensate Wells...  

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

Gas and Gas Condensate Wells (Number of Elements) Louisiana Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

330

Michigan Natural Gas Number of Gas and Gas Condensate Wells ...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) Michigan Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

331

Oklahoma Natural Gas Number of Gas and Gas Condensate Wells ...  

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

Gas and Gas Condensate Wells (Number of Elements) Oklahoma Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

332

Virginia Natural Gas Number of Gas and Gas Condensate Wells ...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) Virginia Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

333

Tennessee Natural Gas Number of Gas and Gas Condensate Wells...  

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

Gas and Gas Condensate Wells (Number of Elements) Tennessee Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

334

Pennsylvania Natural Gas Number of Gas and Gas Condensate Wells...  

Gasoline and Diesel Fuel Update (EIA)

Gas and Gas Condensate Wells (Number of Elements) Pennsylvania Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

335

Arkansas Natural Gas Number of Gas and Gas Condensate Wells ...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) Arkansas Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

336

Maryland Natural Gas Number of Gas and Gas Condensate Wells ...  

Gasoline and Diesel Fuel Update (EIA)

Gas and Gas Condensate Wells (Number of Elements) Maryland Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

337

Illinois Natural Gas Number of Gas and Gas Condensate Wells ...  

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

Gas and Gas Condensate Wells (Number of Elements) Illinois Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

338

Missouri Natural Gas Number of Gas and Gas Condensate Wells ...  

Gasoline and Diesel Fuel Update (EIA)

Gas and Gas Condensate Wells (Number of Elements) Missouri Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

339

Mississippi Natural Gas Number of Gas and Gas Condensate Wells...  

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

Gas and Gas Condensate Wells (Number of Elements) Mississippi Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

340

Nebraska Natural Gas Number of Gas and Gas Condensate Wells ...  

Annual Energy Outlook 2012 (EIA)

Gas and Gas Condensate Wells (Number of Elements) Nebraska Natural Gas Number of Gas and Gas Condensate Wells (Number of Elements) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

Note: This page contains sample records for the topic "gas desulfurization units" 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

Greenhouse Gas Programs, Energy Efficiency, and the Industrial Sector  

E-Print Network (OSTI)

The United States has made significant progress in reducing total energy use through energy efficiency improvements over the past decade, yet the United States still ranks as the highest absolute greenhouse gas (GHG) emitter in the world with 23...

Zhou, A.; Tutterow, V.; Harris, J.

342

Gas Network Optimization: A comparison of Piecewise Linear Models  

E-Print Network (OSTI)

aXM, Compañía de Expertos en Mercados, Colombian Power System Operator, Medellín, ...... rate of heat transfer per unit time and unit mass of the gas [W/kg].

2014-06-22T23:59:59.000Z

343

Pressure Transient Analysis and Production Analysis for New Albany Shale Gas Wells  

E-Print Network (OSTI)

Shale gas has become increasingly important to United States energy supply. During recent decades, the mechanisms of shale gas storage and transport were gradually recognized. Gas desorption was also realized and quantitatively described. Models...

Song, Bo

2010-10-12T23:59:59.000Z

344

GEOLOGIC ASSESSMENT OF DRILLING, COMPLETION, AND STIMULATION METHODS IN SELECTED GAS SHALE PLAYS WORLDWIDE  

E-Print Network (OSTI)

The United States regularly imports majority of the transportation oil, and several TCF of natural gas annually. Nevertheless, there is very large resource of natural gas in unconventional reservoirs, with over 2,200 TCF of natural gas in just...

Patel, Harsh Jay

2014-04-11T23:59:59.000Z

345

RESEARCH AND DEVELOPMENT OF AN INTEGRAL SEPARATOR FOR A CENTRIFUGAL GAS PROCESSING FACILITY  

SciTech Connect

A COMPACT GAS PROCESSING DEVICE WAS INVESTIGATED TO INCREASE GAS PRODUCTION FROM REMOTE, PREVIOUSLY UN-ECONOMIC RESOURCES. THE UNIT WAS TESTED ON AIR AND WATER AND WITH NATURAL GAS AND LIQUID. RESULTS ARE REPORTED WITH RECOMMENDATIONS FOR FUTURE WORK.

LANCE HAYS

2007-02-27T23:59:59.000Z

346

DOE's Program Regulating Liquefied Natural Gas Export Applications...  

Energy Savers (EERE)

and Global Freedom Act." Recent Developments in LNG Exports The boom in domestic shale gas provides unprecedented opportunities for the United States. Over the last several...

347

Request for Information on Efficiency Standards for Natural Gas Compressors  

Energy.gov (U.S. Department of Energy (DOE))

Ormat Technologies is headquartered in Reno Nevada and designs and manufactures waste heat recovery units that are commonly applied on natural gas pipeline compressor stations

348

Pacific Gas and Electric Company | Open Energy Information  

Open Energy Info (EERE)

Company Jump to: navigation, search Name: Pacific Gas and Electric Company Address: PO Box 770000 Place: San Francisco Zip: 94177 Region: United States Sector: Marine and...

349

Annual Greenhouse Gas and Sustainability Data Report | Department...  

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

agency-aggregated data necessary for calculating scope 1, 2, and 3 greenhouse gas (GHG) emissions in the commonly used, native units of energy consumption and fugitive...

350

Natural Gas Weekly Update, Printer-Friendly Version  

Annual Energy Outlook 2012 (EIA)

supply to MRT's East Line or reduce applicable delivery volumes. Colorado Interstate Gas Company announced on December 6 that the Cheyenne Compressor Stations unit that had...

351

,,,"Electricity","from Sources",,"Natural Gas","from Sources...  

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

3 Relative Standard Errors for Table 7.3;" " Unit: Percents." ,,,"Electricity","Components",,"Natural Gas","Components",,"Steam","Components" ,,,,"Electricity",,,"Natural...

352

BP Gas Power and Renewables | Open Energy Information  

Open Energy Info (EERE)

Renewables Jump to: navigation, search Name: BP Gas, Power and Renewables Place: Central Milton Keynes, United Kingdom Zip: MK9 1ES Sector: Renewable Energy Product: Subsidiary of...

353

Agriculture and Land Use National Greenhouse Gas Inventory Software | Open  

Open Energy Info (EERE)

Agriculture and Land Use National Greenhouse Gas Inventory Software Agriculture and Land Use National Greenhouse Gas Inventory Software Jump to: navigation, search Tool Summary LAUNCH TOOL Name: Agriculture and Land Use National Greenhouse Gas Inventory Software Agency/Company /Organization: Colorado State University Partner: United States Agency for International Development, United States Forest Service, United States Environmental Protection Agency Sector: Land Focus Area: Forestry, Agriculture Topics: GHG inventory Resource Type: Software/modeling tools User Interface: Desktop Application Website: www.nrel.colostate.edu/projects/ghgtool/index.php Cost: Free Agriculture and Land Use National Greenhouse Gas Inventory Software Screenshot References: Agriculture and Land Use National Greenhouse Gas Inventory Software[1]

354

Unit Cost Electricity | OpenEI  

Open Energy Info (EERE)

8 8 Varnish cache server Browse Upload data GDR 429 Throttled (bot load) Error 429 Throttled (bot load) Throttled (bot load) Guru Meditation: XID: 2142281518 Varnish cache server Unit Cost Electricity Dataset Summary Description Provides annual energy usage for years 1989 through 2010 for UT at Austin; specifically, electricity usage (kWh), natural gas usage (Mcf), associated costs. Also provides water consumption for 2005 through 2010. Source University of Texas (UT) at Austin, Utilities & Energy Management Date Released Unknown Date Updated Unknown Keywords Electricity Consumption Natural Gas Texas Unit Cost Electricity Unit Cost Natural Gas University Water Data application/vnd.ms-excel icon Energy and Water Use Data for UT-Austin (xls, 32.8 KiB) Quality Metrics

355

Table 7.7 Quantity of Purchased Electricity, Natural Gas, and Steam, 2002  

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

7 Quantity of Purchased Electricity, Natural Gas, and Steam, 2002;" 7 Quantity of Purchased Electricity, Natural Gas, and Steam, 2002;" " Level: National and Regional Data;" " Row: NAICS Codes;" " Column: Supplier Sources of Purchased Electricity, Natural Gas, and Steam;" " Unit: Physical Units or Btu." ,,,"Electricity","Components",,"Natural Gas","Components",,"Steam","Components" " "," ",,,"Electricity",,,"Natural Gas",,,"Steam"," ",," " " "," ",,"Electricity","from Sources",,"Natural Gas","from Sources",,"Steam","from Sources"

356

Table 7.3 Average Prices of Purchased Electricity, Natural Gas, and Steam, 20  

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

3 Average Prices of Purchased Electricity, Natural Gas, and Steam, 2002;" 3 Average Prices of Purchased Electricity, Natural Gas, and Steam, 2002;" " Level: National and Regional Data; " " Row: NAICS Codes;" " Column: Supplier Sources of Purchased Electricity, Natural Gas, and Steam;" " Unit: U.S. Dollars per Physical Units." ,,,"Electricity","Components",,"Natural Gas","Components",,"Steam","Components" " "," ",,,"Electricity",,,"Natural Gas",,,"Steam"," ",," " " "," ",,"Electricity","from Sources",,"Natural Gas","from Sources",,"Steam","from Sources"

357

Historical Natural Gas Annual - 1930 Through 2000  

Gasoline and Diesel Fuel Update (EIA)

Historical Natural Gas Annual Historical Natural Gas Annual 1930 Through 2000 EIA Home > Natural Gas > Natural Gas Data Publications Historical Natural Gas Annual The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-2000 and detailed annual historical information by State for 1967-2000. To read reports in PDF format download a free copy of Adobe Acrobat Reader.

358

Activation of Noble Metals on Metal-Carbide Surfaces: Novel Catalysts for CO Oxidation, Desulfurization and Hydrogenation Reactions  

SciTech Connect

This perspective article focuses on the physical and chemical properties of highly active catalysts for CO oxidation, desulfurization and hydrogenation reactions generated by depositing noble metals on metal-carbide surfaces. To rationalize structure-reactivity relationships for these novel catalysts, well-defined systems are required. High-resolution photoemission, scanning tunneling microscopy (STM) and first-principles periodic density-functional (DF) calculations have been used to study the interaction of metals of Groups 9, 10 and 11 with MC(001) (M = Ti, Zr, V, Mo) surfaces. DF calculations give adsorption energies that range from 2 eV (Cu, Ag, Au) to 6 eV (Co, Rh, Ir). STM images show that Au, Cu, Ni and Pt grow on the carbide substrates forming two-dimensional islands at very low coverage, and three-dimensional islands at medium and large coverages. In many systems, the results of DF calculations point to the preferential formation of admetal-C bonds with significant electronic perturbations in the admetal. TiC(001) and ZrC(001) transfer some electron density to the admetals facilitating bonding of the adatom with electron-acceptor molecules (CO, O{sub 2}, C{sub 2}H{sub 4}, SO{sub 2}, thiophene, etc.). For example, the Cu/TiC(001) and Au/TiC(001) systems are able to cleave both S-O bonds of SO{sub 2} at a temperature as low as 150 K, displaying a reactivity much larger than that of TiC(001) or extended surfaces of bulk copper and gold. At temperatures below 200 K, Au/TiC is able to dissociate O{sub 2} and perform the 2CO + O{sub 2} {yields} 2CO{sub 2} reaction. Furthermore, in spite of the very poor hydrodesulfurization performance of TiC(001) or Au(111), a Au/TiC(001) surface displays an activity for the hydrodesulfurization of thiophene higher than that of conventional Ni/MoS{sub x} catalysts. In general, the Au/TiC system is more chemically active than systems generated by depositing Au nanoparticles on oxide surfaces. Thus, metal carbides are excellent supports for enhancing the chemical reactivity of noble metals.

Rodriguez J. A.; Illas, F.

2012-01-01T23:59:59.000Z

359

Tracy Power Station -- Unit No. 4, Pinon Pine Power Project Public Design Report  

SciTech Connect

This Public Design Report describes the Pinon Pine Project which will be located at the Sierra Pacific Power Company`s (SPPCO) Tracy Station near Reno, Nevada. The integrated gasification combined-cycle (IGCC) plant is designed to process 880 tones per day (TPD) of bituminous coal producing approximately 107 gross megawatts of electric power (MWe). This project is receiving cost-sharing from the US Department of Energy (DOE) in accordance with DOE Cooperative Agreement DE-FC2192MC29309. The plant incorporates the Kellogg-Rust-Westinghouse (KRW) fluidized bed gasification technology which produces a low-Btu gas which is used as fuel in a combined cycle power plant which has been modified to accommodate the fuel gas produced by an air-blown gasifier. The gasification system also includes hot gas removal of particulates and sulfur compounds from the fuel gas resulting in a plant with exceptionally low atmospheric emissions. Desulfurization is accomplished by a combination of limestone injection into the KRW fluidized bed gasifier and by a transport reactor system. Particulate removal is accomplished by high efficiency cyclones and a barrier filter. The Pinon Pine Project Schedule is divided into three phases. Phase I includes permitting and preliminary design. Phase II, which overlaps Phase I, covers detailed design, procurement, and construction. Phase III will cover the initial operation and demonstration portion of the project.

NONE

1994-12-01T23:59:59.000Z

360

Method for removing metal vapor from gas streams  

DOE Patents (OSTI)

A process for cleaning an inert gas contaminated with a metallic vapor, such as cadmium, involves withdrawing gas containing the metallic contaminant from a gas atmosphere of high purity argon; passing the gas containing the metallic contaminant to a mass transfer unit having a plurality of hot gas channels separated by a plurality of coolant gas channels; cooling the contaminated gas as it flows upward through the mass transfer unit to cause contaminated gas vapor to condense on the gas channel walls; regenerating the gas channels of the mass transfer unit; and, returning the cleaned gas to the gas atmosphere of high purity argon. The condensing of the contaminant-containing vapor occurs while suppressing contaminant particulate formation, and is promoted by providing a sufficient amount of surface area in the mass transfer unit to cause the vapor to condense and relieve supersaturation buildup such that contaminant particulates are not formed. Condensation of the contaminant is prevented on supply and return lines in which the contaminant containing gas is withdrawn and returned from and to the electrorefiner and mass transfer unit by heating and insulating the supply and return lines.

Ahluwalia, R. K. (6440 Hillcrest Dr., Burr Ridge, IL 60521); Im, K. H. (925 Lehigh Cir., Naperville, IL 60565)

1996-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Historical Natural Gas Annual 1999  

Gasoline and Diesel Fuel Update (EIA)

1999 1999 The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-1999 and detailed annual historical information by State for 1967-1999. The Historical Natural Gas Annual tables are available as self-extracting executable files in ASCII TXT or CSV file formats. Tables 1-3 present annual historical data at the national level for 1930-1999. The remaining tables contain detailed annual historical information, by State, for 1967-1999. Please read the file entitled READMEV2 for a description and documentation of information included in this file.

362

NETL: Gasification Systems - Gas Separation  

NLE Websites -- All DOE Office Websites (Extended Search)

Separation Separation Ion-Transport Membrane Oxygen Separation Modules Ion-Transport Membrane Oxygen Separation Modules Gas separation unit operations represent major cost elements in gasification plants. The gas separation technology being supported in the DOE program promises significant reduction in cost of electricity, improved thermal efficiency, and superior environmental performance. Gasification-based energy conversion systems rely on two gas separation processes: (1) separation of oxygen from air for feed to oxygen-blown gasifiers; and (2) post-gasification separation of hydrogen from carbon dioxide following (or along with) the shifting of gas composition when carbon dioxide capture is required or hydrogen is the desired product. Research efforts include development of advanced gas separation

363

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

,366 ,366 95,493 1.08 0 0.00 1 0.03 29,406 0.56 1,206 0.04 20,328 0.64 146,434 0.73 - Natural Gas 1996 Million Percent of Million Percent of Cu. Feet National Total Cu. Feet National Total Net Interstate Movements: Industrial: Marketed Production: Vehicle Fuel: Deliveries to Consumers: Electric Residential: Utilities: Commercial: Total: South Carolina South Carolina 88. Summary Statistics for Natural Gas South Carolina, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ...........................................

364

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

0,216 0,216 50,022 0.56 135 0.00 49 1.67 85,533 1.63 8,455 0.31 45,842 1.45 189,901 0.95 - Natural Gas 1996 Million Percent of Million Percent of Cu. Feet National Total Cu. Feet National Total Net Interstate Movements: Industrial: Marketed Production: Vehicle Fuel: Deliveries to Consumers: Electric Residential: Utilities: Commercial: Total: M a r y l a n d Maryland 68. Summary Statistics for Natural Gas Maryland, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... NA NA NA NA NA Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 9 7 7 7 8 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 33 28 26 22 135 From Oil Wells ...........................................

365

GAS STORAGE TECHNOLOGY CONSORTIUM  

SciTech Connect

Gas storage is a critical element in the natural gas industry. Producers, transmission and distribution companies, marketers, and end users all benefit directly from the load balancing function of storage. The unbundling process has fundamentally changed the way storage is used and valued. As an unbundled service, the value of storage is being recovered at rates that reflect its value. Moreover, the marketplace has differentiated between various types of storage services, and has increasingly rewarded flexibility, safety, and reliability. The size of the natural gas market has increased and is projected to continue to increase towards 30 trillion cubic feet (TCF) over the next 10 to 15 years. Much of this increase is projected to come from electric generation, particularly peaking units. Gas storage, particularly the flexible services that are most suited to electric loads, is critical in meeting the needs of these new markets. In order to address the gas storage needs of the natural gas industry, an industry-driven consortium was created--the Gas Storage Technology Consortium (GSTC). The objective of the GSTC is to provide a means to accomplish industry-driven research and development designed to enhance operational flexibility and deliverability of the Nation's gas storage system, and provide a cost effective, safe, and reliable supply of natural gas to meet domestic demand. To accomplish this objective, the project is divided into three phases that are managed and directed by the GSTC Coordinator. Base funding for the consortium is provided by the U.S. Department of Energy (DOE). In addition, funding is anticipated from the Gas Technology Institute (GTI). The first phase, Phase 1A, was initiated on September 30, 2003, and is scheduled for completion on March 31, 2004. Phase 1A of the project includes the creation of the GSTC structure, development of constitution (by-laws) for the consortium, and development and refinement of a technical approach (work plan) for deliverability enhancement and reservoir management. This report deals with the second 3-months of the project and encompasses the period December 31, 2003, through March 31, 2003. During this 3-month, the dialogue of individuals representing the storage industry, universities and the Department of energy was continued and resulted in a constitution for the operation of the consortium and a draft of the initial Request for Proposals (RFP).

Robert W. Watson

2004-04-17T23:59:59.000Z

366

Gas Storage Technology Consortium  

SciTech Connect

Gas storage is a critical element in the natural gas industry. Producers, transmission and distribution companies, marketers, and end users all benefit directly from the load balancing function of storage. The unbundling process has fundamentally changed the way storage is used and valued. As an unbundled service, the value of storage is being recovered at rates that reflect its value. Moreover, the marketplace has differentiated between various types of storage services, and has increasingly rewarded flexibility, safety, and reliability. The size of the natural gas market has increased and is projected to continue to increase towards 30 trillion cubic feet (TCF) over the next 10 to 15 years. Much of this increase is projected to come from electric generation, particularly peaking units. Gas storage, particularly the flexible services that are most suited to electric loads, is critical in meeting the needs of these new markets. In order to address the gas storage needs of the natural gas industry, an industry-driven consortium was created-the Gas Storage Technology Consortium (GSTC). The objective of the GSTC is to provide a means to accomplish industry-driven research and development designed to enhance operational flexibility and deliverability of the Nation's gas storage system, and provide a cost effective, safe, and reliable supply of natural gas to meet domestic demand. This report addresses the activities for the quarterly period of July 1, 2006 to September 30, 2006. Key activities during this time period include: {lg_bullet} Subaward contracts for all 2006 GSTC projects completed; {lg_bullet} Implement a formal project mentoring process by a mentor team; {lg_bullet} Upcoming Technology Transfer meetings: {sm_bullet} Finalize agenda for the American Gas Association Fall Underground Storage Committee/GSTC Technology Transfer Meeting in San Francisco, CA. on October 4, 2006; {sm_bullet} Identify projects and finalize agenda for the Fall GSTC Technology Transfer Meeting, Pittsburgh, PA on November 8, 2006; {lg_bullet} Draft and compile an electronic newsletter, the GSTC Insider; and {lg_bullet} New members update.

Joel L. Morrison; Sharon L. Elder

2006-09-30T23:59:59.000Z

367

GAS STORAGE TECHNOLOGY CONSORTIUM  

SciTech Connect

Gas storage is a critical element in the natural gas industry. Producers, transmission and distribution companies, marketers, and end users all benefit directly from the load balancing function of storage. The unbundling process has fundamentally changed the way storage is used and valued. As an unbundled service, the value of storage is being recovered at rates that reflect its value. Moreover, the marketplace has differentiated between various types of storage services, and has increasingly rewarded flexibility, safety, and reliability. The size of the natural gas market has increased and is projected to continue to increase towards 30 trillion cubic feet (TCF) over the next 10 to 15 years. Much of this increase is projected to come from electric generation, particularly peaking units. Gas storage, particularly the flexible services that are most suited to electric loads, is critical in meeting the needs of these new markets. In order to address the gas storage needs of the natural gas industry, an industry-driven consortium was created--the Gas Storage Technology Consortium (GSTC). The objective of the GSTC is to provide a means to accomplish industry-driven research and development designed to enhance operational flexibility and deliverability of the Nation's gas storage system, and provide a cost effective, safe, and reliable supply of natural gas to meet domestic demand. To accomplish this objective, the project is divided into three phases that are managed and directed by the GSTC Coordinator. Base funding for the consortium is provided by the U.S. Department of Energy (DOE). In addition, funding is anticipated from the Gas Technology Institute (GTI). The first phase, Phase 1A, was initiated on September 30, 2003, and was completed on March 31, 2004. Phase 1A of the project included the creation of the GSTC structure, development and refinement of a technical approach (work plan) for deliverability enhancement and reservoir management. This report deals with Phase 1B and encompasses the period April 1, 2004, through June 30, 2004. During this 3-month period, a Request for Proposals (RFP) was made. A total of 17 proposals were submitted to the GSTC. A proposal selection meeting was held June 9-10, 2004 in Morgantown, West Virginia. Of the 17 proposals, 6 were selected for funding.

Robert W. Watson

2004-07-15T23:59:59.000Z

368

Optimizing hydrocarbon recoveries in nitrogen rejection units  

SciTech Connect

In order to address conceptual questions such as process selection and natural gas liquids plant integration, an understanding of the effects of several additional factors on nitrogen rejection unit design is important. These factors, which may influence optimum hydrocarbon recovery, installed compression, etc., include current and forecast values for natural gas and utilities, project life, plant size, feed gas composition and product specifications, feed pressure, and process variations. Prices, project life, and plant size are analyzed in detail and presented in terms of methane recoveries as a function of nitrogen content in the feed for both double and single column processes. Trends are qualitatively discussed for the remaining factors. 13 references.

Chesney, J.D.; Davis, R.A.; Hilton, M.F.; Vines, H.L.

1983-01-01T23:59:59.000Z

369

" Million Housing Units, Final...  

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

2 Fuels Used and End Uses in U.S. Homes, by OwnerRenter Status, 2009" " Million Housing Units, Final" ,,,,"Housing Unit Type" ,,,,"Single-Family Units",,,,"Apartments in Buildings...

370

" Million Housing Units, Final...  

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

2 Household Demographics of U.S. Homes, by OwnerRenter Status, 2009" " Million Housing Units, Final" ,,,,"Housing Unit Type" ,,,,"Single-Family Units",,,,"Apartments in Buildings...

371

" Million Housing Units, Final...  

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

Asked (Apartments in Buildings" "With 5 or More Units)",19.1,5.8,6.2,2.8,2.8,1.5 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

372

" Million Housing Units, Final...  

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

"Not Asked (Apartments in Buildings" "With 5 or More Units)",19.1,4.4,3.7,6.2,4.7 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

373

" Million Housing Units, Final...  

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

"Not Asked (Apartments in Buildings" "With 5 or More Units)",19.1,9.6,5,2.2,1.5,0.8 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

374

Historical Natural Gas Annual - 1930 Through 2000  

Gasoline and Diesel Fuel Update (EIA)

2000 2000 The Historical Natural Gas Annual contains historical information on supply and disposition of natural gas at the national, regional, and State level as well as prices at selected points in the flow of gas from the wellhead to the burner-tip. Data include production, transmission within the United States, imports and exports of natural gas, underground storage activities, and deliveries to consumers. The publication presents historical data at the national level for 1930-2000 and detailed annual historical information by State for 1967-2000. Entire . The entire report as a single file. PDF 1.5 MB Front Matter . Historical Natural Gas Annual Cover Page, Preface, Common Abbreviations Used, and Table of Contents PDF . . Tables . 1 Quantity and Average Price of Natural Gas Production in the United States, 1930-1998 PDF

375

Management of dry flue gas dsulfurization by-products in underground mines - an update  

SciTech Connect

In 1993, the U.S. produced about 100 million tons of coal combustion by-products (CCBs) primarily from conventional coal-fired boilers. The requirement to reduce SO{sub x} and NO{sub x} emissions to comply with the 1990 Clean Air Act Amendments (CAAA) force utilities to adopt advanced combustion and flue gas desulfurization (FGD) technologies, such as wet scrubbers, fluidized bed combustion (FBC), dry sorbent duct or furnace injection. These technologies will double to triple the amount of FGD by-products while only slightly increasing the amounts of conventional combustion residues, such as fly ash, bottom ash and boiler slag. This paper describes a program concerned with the underground disposal of combustion products in abandoned underground coal mines.

Chugh, Y.P.; Thomasson, E.M. [Southern Illinois Univ., Carbondale, IL (United States)

1996-09-01T23:59:59.000Z

376

EPA's Liquefied Natural Gas Regulatory Roadmap  

NLE Websites -- All DOE Office Websites (Extended Search)

Liquefied Natural Gas Liquefied Natural Gas Regulatory Roadmap July 2006 EPA230-B-06-001 About this Roadmap Natural gas continues to play an important role in meeting our nation's growing energy needs. In 2005, natural gas accounted for 23% of our nation's total energy consumption. 1 The Department of Energy's Energy Information Administration (EIA) projects that domestic consumption of natural gas will continue to increase and that imports of liquefied natural gas (LNG) will meet much of the increased demand. 2 LNG, created when natural gas is converted into a liquid state by cooling it to a temperature close to negative 260°F, presents an efficient way to transport natural gas via ship from foreign production areas to the United States. The cooling process reduces the

377

Study of Flue Gas Desulfurization Absorbent Prepared from Coal Fly Ash:? Effects of the Composition of the Absorbent on the Activity  

Science Journals Connector (OSTI)

The formation of calcium silicate is suggested to be predominant in a high concentration of silica, while the formation of ettringite was observed by the XRD only for the absorbent containing silica below 30%. ... ettringite ... With sample 1 containing no silica, the formation of ettringite (Ca6Al2(SO4)3(OH)12) was obvious. ...

Hiroaki Tsuchiai; Tomohiro Ishizuka; Hideki Nakamura; Tsutomu Ueno; Hideshi Hattori

1996-07-03T23:59:59.000Z

378

Estimated United States Transportation Energy Use 2005  

SciTech Connect

A flow chart depicting energy flow in the transportation sector of the United States economy in 2005 has been constructed from publicly available data and estimates of national energy use patterns. Approximately 31,000 trillion British Thermal Units (trBTUs) of energy were used throughout the United States in transportation activities. Vehicles used in these activities include automobiles, motorcycles, trucks, buses, airplanes, rail, and ships. The transportation sector is powered primarily by petroleum-derived fuels (gasoline, diesel and jet fuel). Biomass-derived fuels, electricity and natural gas-derived fuels are also used. The flow patterns represent a comprehensive systems view of energy used within the transportation sector.

Smith, C A; Simon, A J; Belles, R D

2011-11-09T23:59:59.000Z

379

STATEMENT OF CONSIDERATIONS REQUEST BY UNITED TECHNOLOGIES CORPORATION (UNITED  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

RTGHTS TO INVENTIONS MADE UNDER RTGHTS TO INVENTIONS MADE UNDER COOPERATIVE AGREEMENT NUMBER DE-FC04-02AL67628, DOE WAIVER NO. W(A) 02-038. The Petitioner, United Technologies, acting through the United Technologies Research Center (UTRC), has requested a waiver of all domestic and foreign patent iights to inventions that may be conceived or first actually reduced to practice in the course of UTRC's work as the prime contractor under Cooperative Agreement Number DI-FC04- 02AL67628 entitled "On-Board Vehicle, Cost Effective, Hydrogen Enhancement Technology PEM Fuel Cells" with the U S. Department of Energy (DOE). The work to be done will be the development and fabrication of an integrated high temperature water gas shift reactor/hydrogen separator for use in a PEM fuel cell power

380

Viability of an expanded United States nuclear power program and its effects on energy markets  

E-Print Network (OSTI)

The four biggest energy sources in the United States are coal, crude oil, natural gas, and nuclear power. While coal and nuclear power are produced domestically, more than 70% of crude oil and 20% of natural gas is imported. ...

Khan, Tanzeer S

2006-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Alternative formulations of regenerable flue gas cleanup catalysts  

SciTech Connect

The major source of man-made SO{sub 2} in the atmosphere is the burning of coal for electric power generation. Coal-fired utility plants are also large sources of NO{sub x} pollution. Regenerable flue gas desulfurization/NO{sub x} abatement catalysts provide one mechanism of simultaneously removing SO{sub 2} and NO{sub x} species from flue gases released into the atmosphere. The purpose of this project is to examine routes of optimizing the adsorption efficiency, the adsorption capacity, and the ease of regeneration of regenerable flue gas cleanup catalysts. We are investigating two different mechanisms for accomplishing this goal. The first involves the use of different alkali and alkaline earth metals as promoters for the alumina sorbents to increase the surface basicity of the sorbent and thus adjust the number and distribution of adsorption sites. The second involves investigation of non-aqueous impregnation, as opposed to aqueous impregnation, as a method to obtain an evenly dispersed monolayer of the promoter on the surface.

Mitchell, M.B.; White, M.G.

1991-01-01T23:59:59.000Z

382

,"Missouri Natural Gas Summary"  

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

Gas Wells (MMcf)","Missouri Natural Gas Gross Withdrawals from Oil Wells (MMcf)","Missouri Natural Gas Gross Withdrawals from Shale Gas (Million Cubic Feet)","Missouri Natural...

383

Gas-Fired Boilers and Furnaces | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Gas-Fired Boilers and Furnaces Gas-Fired Boilers and Furnaces Gas-Fired Boilers and Furnaces May 16, 2013 - 4:36pm Addthis A residential natural gas meter. A residential natural gas meter. What does this mean for me? Your gas boiler or furnace may be oversized, particularly if you've upgraded the energy efficiency of your home. Your gas boiler or furnace can be retrofitted to improve its energy efficiency. Gas boilers and furnaces can be fueled by either natural gas or propane with simple modifications accounting for the different characteristics of the fuels. Propane is usually more expensive as a fuel, but is available throughout the United States. Natural gas supplies depend on having a natural gas distribution system in your area, and areas at the end of the pipeline (such as the Northeast) tend to pay higher prices for natural gas.

384

Gas-Fired Boilers and Furnaces | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Gas-Fired Boilers and Furnaces Gas-Fired Boilers and Furnaces Gas-Fired Boilers and Furnaces May 16, 2013 - 4:36pm Addthis A residential natural gas meter. A residential natural gas meter. What does this mean for me? Your gas boiler or furnace may be oversized, particularly if you've upgraded the energy efficiency of your home. Your gas boiler or furnace can be retrofitted to improve its energy efficiency. Gas boilers and furnaces can be fueled by either natural gas or propane with simple modifications accounting for the different characteristics of the fuels. Propane is usually more expensive as a fuel, but is available throughout the United States. Natural gas supplies depend on having a natural gas distribution system in your area, and areas at the end of the pipeline (such as the Northeast) tend to pay higher prices for natural gas.

385

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

9, 2011 at 2:00 P.M. 9, 2011 at 2:00 P.M. Next Release: Thursday, October 6, 2011 Overview Prices Storage Other Market Trends Overview (For the Week Ending Wednesday, September 28, 2011) Natural gas spot prices at most market locations across the country this past week initially declined and then began to creep upwards as natural gas use for power generation increased. The upward trend was halted yesterday, as prices at nearly all points retreated, possibly due to forecasts for considerably colder weather. After declining from $3.78 per million British thermal units (MMBtu) last Wednesday to $3.72 per MMbtu on Thursday, the Henry Hub spot price increased to $3.92 per MMBtu on Tuesday and closed at $3.88 per MMBtu yesterday. At the New York Mercantile Exchange (NYMEX), the October 2011

386

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

3, 2011 at 2:00 P.M. 3, 2011 at 2:00 P.M. Next Release: Thursday, November 10, 2011 Overview Prices Storage Other Market Trends Overview (For the Week Ending Wednesday, November 2, 2011) The previous report week's increasing prices gave way to relatively consistent declines across a large part of the country over this report week. The Henry Hub spot price showed a slight increase over the weekend, but closed down 26 cents for the week to $3.39 per million British thermal units (MMBtu) on November 2. At the New York Mercantile Exchange (NYMEX), the higher valued December 2011 natural gas contract moved into position as the near-month contract and declined by 2.6 cents per MMBtu to close the week at $3.749 per MMBtu. Working natural gas in storage rose last week to 3794 billion cubic

387

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

1, 2008 1, 2008 Next Release: August 28, 2008 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (Wednesday, August 13, to Wednesday, August 20) During the report week (Wednesday-Wednesday, August 13-20), natural gas prices continued their overall declines in the Lower 48 States, with decreases ranging between 1 and 58 cents per million British thermal units (MMBtu). However, there were a few exceptions in the Rocky Mountains, where the only average regional price increase on the week was recorded. At the New York Mercantile Exchange (NYMEX), prices for the September delivery contract decreased 38 cents per MMBtu, settling yesterday at $8.077. On Monday and Tuesday, the September contract price dipped below $8 per MMBtu, reaching this level for the first time since

388

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

7, 2011 at 2:00 P.M. 7, 2011 at 2:00 P.M. Next Release: Thursday, November 3, 2011 Overview Prices Storage Other Market Trends Overview (For the Week Ending Wednesday, October 26, 2011) The weathermanÂ’s promise for chillier temperatures later this week and mention of the word "snow" in some forecasts was the likely catalyst propelling prices upwards this week. In an environment of generally supportive market fundamentals, the Henry Hub price closed up 7 cents for the week to $3.65 per million British thermal units (MMBtu) on October 26. At the New York Mercantile Exchange (NYMEX), the November 2011 natural gas contract rose just under half a cent per MMBtu for the week to close at $3.590 per MMBtu. Working natural gas in storage rose last week to 3,716 billion cubic

389

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

9, 2008 9, 2008 Next Release: June 26, 2008 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview Since Wednesday, June 11, natural gas spot prices increased at all markets in the Lower 48 States except one, despite the lack of weather-related demand in much of the country. The restoration of production at the Independence Hub to the level prevailing prior to the April 8 shut-in had limited effect on prices. For the week, the Henry Hub spot price increased 44 cents to $12.93 per million British thermal units (MMBtu). At the New York Mercantile Exchange (NYMEX), prices also increased on the week, with the weekly increase of the near-month contract exceeding those observed at spot market locations in the eastern half of the country.

390

Natural Gas Weekly Update  

Gasoline and Diesel Fuel Update (EIA)

26, 2009 26, 2009 Next Release: April 2, 2009 Overview Prices Storage Other Market Trends Natural Gas Transportation Update Overview (For the Week Ending Wednesday, March 25, 2009) Spot prices increased at all trading locations this week, with the biggest increases occurring in the Northeast. Many market locations ended the week with spot prices above $4 per million British thermal units (MMBtu). During the report week, the Henry Hub spot price increased by $0.38 to $4.13 per MMBtu. At the New York Mercantile Exchange (NYMEX), futures prices also increased, climbing by $0.65 to $4.329 for the April 2009 contract. Prices for the April 2009 contract reached their highest levels since February 13, 2009, on March 24. Natural gas in storage was 1,654 billion cubic feet (Bcf) as of

391

Viability of an expanded United States nuclear power program and its effects on energy markets .  

E-Print Network (OSTI)

??The four biggest energy sources in the United States are coal, crude oil, natural gas, and nuclear power. While coal and nuclear power are produced… (more)

Khan, Tanzeer S

2006-01-01T23:59:59.000Z

392

Efficiency of Energy Use in the United States  

Science Journals Connector (OSTI)

...at the power plant. Conversely...by nuclear plants for this purpose...required at the power plant for each unit...Comparison of insulation requirements...Insulation specification Gas Electric...ample use of thermal insulation...

Eric Hirst; John C. Moyers

1973-03-30T23:59:59.000Z

393

NNSA Small Business Week Day 2: United Drilling, Inc. | National...  

National Nuclear Security Administration (NNSA)

Inc., a small minority-owned business based in Roswell, N.M. United Drilling drills oil, gas, water, geothermal, and environmental wells throughout the southwestern U.S. The...

394

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

68,747 68,747 34,577 0.39 0 0.00 34 1.16 14,941 0.29 0 0.00 11,506 0.36 61,058 0.31 I d a h o Idaho 60. Summary Statistics for Natural Gas Idaho, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation.......................... 0 0 0 0 0 Vented

395

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

0 0 0 0.00 0 0.00 0 0.00 540 0.01 0 0.00 2,132 0.07 2,672 0.01 H a w a i i Hawaii 59. Summary Statistics for Natural Gas Hawaii, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation.......................... 0 0 0 0 0 Vented and Flared

396

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

483,052 483,052 136,722 1.54 6,006 0.03 88 3.00 16,293 0.31 283,557 10.38 41,810 1.32 478,471 2.39 F l o r i d a Florida 57. Summary Statistics for Natural Gas Florida, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 47 50 98 92 96 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 7,584 8,011 8,468 7,133 6,706 Total.............................................................. 7,584 8,011 8,468 7,133 6,706 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ...............

397

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

291,898 291,898 113,995 1.29 0 0.00 4 0.14 88,078 1.68 3,491 0.13 54,571 1.73 260,140 1.30 I o w a Iowa 63. Summary Statistics for Natural Gas Iowa, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation.......................... 0 0 0

398

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

Vehicle Fuel: Vehicle Fuel: Deliveries to Consumers: Electric Residential: Utilities: Commercial: Total: New England New England 36. Summary Statistics for Natural Gas New England, 1992-1996 Table 691,089 167,354 1.89 0 0.00 40 1.36 187,469 3.58 80,592 2.95 160,761 5.09 596,215 2.98 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................

399

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

29,693 29,693 0 0.00 0 0.00 6 0.20 17,290 0.33 0 0.00 16,347 0.52 33,644 0.17 District of Columbia District of Columbia 56. Summary Statistics for Natural Gas District of Columbia, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

400

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

42,980 42,980 14,164 0.16 0 0.00 1 0.03 9,791 0.19 23,370 0.86 6,694 0.21 54,020 0.27 D e l a w a r e Delaware 55. Summary Statistics for Natural Gas Delaware, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

Note: This page contains sample records for the topic "gas desulfurization units" 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

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-49,536 -49,536 7,911 0.09 49,674 0.25 15 0.51 12,591 0.24 3 0.00 12,150 0.38 32,670 0.16 North Dakota North Dakota 82. Summary Statistics for Natural Gas North Dakota, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 496 525 507 463 462 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 104 101 104 99 108 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 12,461 18,892 19,592 16,914 16,810 From Oil Wells ........................................... 47,518 46,059 43,640 39,760 38,906 Total.............................................................. 59,979 64,951 63,232 56,674 55,716 Repressuring ................................................

402

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

21,547 21,547 4,916 0.06 0 0.00 0 0.00 7,012 0.13 3 0.00 7,099 0.22 19,031 0.10 N e w H a m p s h i r e New Hampshire 77. Summary Statistics for Natural Gas New Hampshire, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

403

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

139,881 139,881 26,979 0.30 463 0.00 115 3.92 27,709 0.53 19,248 0.70 28,987 0.92 103,037 0.52 A r i z o n a Arizona 50. Summary Statistics for Natural Gas Arizona, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... NA NA NA NA NA Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 6 6 6 7 7 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 721 508 711 470 417 From Oil Wells ........................................... 72 110 48 88 47 Total.............................................................. 794 618 759 558 464 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease

404

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

Middle Middle Atlantic Middle Atlantic 37. Summary Statistics for Natural Gas Middle Atlantic, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 1,857 1,981 2,042 1,679 1,928 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 36,906 36,857 26,180 37,159 38,000 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 161,372 152,717 140,444 128,677 152,494 From Oil Wells ........................................... 824 610 539 723 641 Total.............................................................. 162,196 153,327 140,982 129,400 153,134 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed

405

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

386,690 386,690 102,471 1.16 0 0.00 43 1.47 142,319 2.72 5,301 0.19 98,537 3.12 348,671 1.74 M i n n e s o t a Minnesota 71. Summary Statistics for Natural Gas Minnesota, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

406

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

1,108,583 1,108,583 322,275 3.63 298 0.00 32 1.09 538,749 10.28 25,863 0.95 218,054 6.90 1,104,972 5.52 I l l i n o i s Illinois 61. Summary Statistics for Natural Gas Illinois, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... NA NA NA NA NA Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 382 385 390 372 370 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 337 330 323 325 289 From Oil Wells ........................................... 10 10 10 10 9 Total.............................................................. 347 340 333 335 298 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ...............

407

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

286,485 286,485 71,533 0.81 25 0.00 31 1.06 137,225 2.62 5,223 0.19 72,802 2.31 286,814 1.43 M i s s o u r i Missouri 73. Summary Statistics for Natural Gas Missouri, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... NA NA NA NA NA Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 5 8 12 15 24 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 27 14 8 16 25 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 27 14 8 16 25 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

408

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

411,951 411,951 100,015 1.13 0 0.00 5 0.17 114,365 2.18 45,037 1.65 96,187 3.05 355,609 1.78 Massachusetts Massachusetts 69. Summary Statistics for Natural Gas Massachusetts, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

409

Gas vesicles.  

Science Journals Connector (OSTI)

...in the suspending water, of concentration...MPa and balances the atmospheric pressure. Note that...versely, liquid water could not form by condensation inside the gas vesicle...presumably surrounded by water on all sides. At...

A E Walsby

1994-03-01T23:59:59.000Z

410

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

226,798 226,798 104,124 1.17 0 0.00 0 0.00 58,812 1.12 2,381 0.09 40,467 1.28 205,783 1.03 North Carolina North Carolina 81. Summary Statistics for Natural Gas North Carolina, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 0 0 0 0 0 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 0 0 0 0 0 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 0 0 0 0 0 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 0 0 0 0 0 Repressuring ................................................ 0 0 0 0 0 Nonhydrocarbon Gases Removed ............... 0 0 0 0 0 Wet After Lease Separation..........................

411

United States Department of Agriculture General Technical  

E-Print Network (OSTI)

Research Station January 2014 Past and Prospective Carbon Stocks in Forests of Northern Wisconsin A Report or greenhouse gas registries and receive some credit for additional actions to reduce emissions or increase Foresight and Rapid Response research unit with the U.S. Forest Service, Northern Research Station, 11

412

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

E-Print Network (OSTI)

cost Flue gas desulfurization (FGD) Selective catalytic reduction (SCR) Gas turbine combined cycle (GTCC) Pulverized coal (PC) boilers LNG production

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

2007-01-01T23:59:59.000Z

413

Liberty Utilities (Gas) - Commercial Energy Efficiency Programs |  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Liberty Utilities (Gas) - Commercial Energy Efficiency Programs Liberty Utilities (Gas) - Commercial Energy Efficiency Programs Liberty Utilities (Gas) - Commercial Energy Efficiency Programs < Back Eligibility Commercial Industrial Institutional Local Government Schools State Government Savings Category Heating & Cooling Commercial Heating & Cooling Heating Home Weatherization Commercial Weatherization Other Construction Manufacturing Appliances & Electronics Water Heating Windows, Doors, & Skylights Maximum Rebate Custom Projects: $100,000 (existing facilities); $250,000 (new construction) Energy Efficiency Engineering Study: $10,000 Steam Traps: $2500 Programmable Thermostats: up to five units Boiler Reset Controls: up to two units Program Info State New Hampshire Program Type Utility Rebate Program Rebate Amount

414

Reduction of Utility Usage in a Glyphosate Intermediate (GI) Unit  

E-Print Network (OSTI)

Reduction of Utility Usage in a Glyphosate Intermediate (GI) Unit Michael L. Sander Manufacturing Technologist Monsanto Company Luling, Louisiana Plant ABSTRACT The Monsanto Company Luling Plant produces glyphosate intermediate (GI... the Utilities area brainstormed ideas and then implemented them across the units. While all utilities were addressed, the group’s primary focus areas were natural gas, nitrogen, and compressed air. Natural gas usage was reduced 28% by optimizing...

Sander, M. L.

2006-01-01T23:59:59.000Z

415

Desulfurization Fuel Filter  

Energy.gov (U.S. Department of Energy (DOE))

Presentation given at DEER 2006, August 20-24, 2006, Detroit, Michigan. Sponsored by the U.S. DOE's EERE FreedomCar and Fuel Partnership and 21st Century Truck Programs.

416

Revisiting the Long-Term Hedge Value of Wind Power in an Era of Low Natural Gas Prices  

E-Print Network (OSTI)

leaking of methane from shale gas development: response to2012. “The Influence of Shale Gas on U.S. Energy andthe United States’ vast shale gas reserves in recent years

Bolinger, Mark

2014-01-01T23:59:59.000Z

417

Energy Calculator- Common Units and Conversions  

NLE Websites -- All DOE Office Websites (Extended Search)

Energy Calculator - Common Units and Conversions Energy Calculator - Common Units and Conversions Calculators for Energy Used in the United States: Coal Electricity Natural Gas Crude Oil Gasoline Diesel & Heating Oil Coal Conversion Calculator Short Tons Btu Megajoules Metric Tons Clear Calculate 1 Short Ton = 20,169,000 Btu (based on U.S. consumption, 2007) Electricity Conversion Calculator KilowattHours Btu Megajoules million Calories Clear Calculate 1 KilowattHour = 3,412 Btu Natural Gas Conversion Calculator Cubic Feet Btu Megajoules Cubic Meters Clear Calculate 1 Cubic Foot = 1,028 Btu (based on U.S. consumption, 2007); 1 therm = 100,000 Btu; 1 terajoule = 1,000,000 megajoules Crude Oil Conversion Calculator Barrels Btu Megajoules Metric Tons* Clear Calculate 1 Barrel = 42 U.S. gallons = 5,800,000 Btu (based on U.S. consumption,

418

Liquefied Natural Gas Safety Research  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

| May 2012 | May 2012 Liquefied Natural Gas (LNG) Safety Research | Page 1 Liquefied Natural Gas Safety Research Report to Congress May 2012 United States Department of Energy Washington, DC 20585 Department of Energy | May 2012 Liquefied Natural Gas (LNG) Safety Research | Page i Message from the Assistant Secretary for Fossil Energy The Explanatory Statement accompanying the Consolidated Appropriations Act, 2008 1 and the House Report on the House of Representatives version of the related bill 2 requested the Department of Energy to submit a report to Congress addressing several key liquefied natural gas (LNG) research priorities. These issues are identified in the February 2007 Government Accountability Office Report (GAO Report 07-316), Public Safety Consequences of a Terrorist

419

Separation of CO2 from flue gas using electrochemical cells  

SciTech Connect

ABSTRACT Past research with high temperature molten carbonate electrochemical cells has shown that carbon dioxide can be separated from flue gas streams produced by pulverized coal combustion for power generation, However, the presence of trace contaminants, i.e" sulfur dioxide and nitric oxides, will impact the electrolyte within the cell. If a lower temperature cell could be devised that would utilize the benefits of commercially-available, upstream desulfurization and denitrification in the power plant, then this CO2 separation technique can approach more viability in the carbon sequestration area, Recent work has led to the assembly and successful operation of a low temperature electrochemical cell. In the proof-of-concept testing with this cell, an anion exchange membrane was sandwiched between gas-diffusion electrodes consisting of nickel-based anode electrocatalysts on carbon paper. When a potential was applied across the cell and a mixture of oxygen and carbon dioxide was flowed over the wetted electrolyte on the cathode side, a stream of CO2 to O2 was produced on the anode side, suggesting that carbonate/ bicarbonate ions are the CO2 carrier in the membrane. Since a mixture of CO 2 and 02 is produced, the possibility exists to use this stream in oxy-firing of additional fuel. From this research, a novel concept for efficiently producing a carbon dioxide rich effiuent from combustion of a fossil fuel was proposed. Carbon dioxide and oxygen are captured from the flue gas of a fossilfuel combustor by one or more electrochemical cells or cell stacks. The separated stream is then transferred to an oxy-fired combustor which uses the gas stream for ancillary combustion, ultimately resulting in an effluent rich in carbon dioxide, A portion of the resulting flow produced by the oxy-fired combustor may be continuously recycled back into the oxy-fired combustor for temperature control and an optimal carbon dioxide rich effluent.

Pennline, H.W; Granite, E.J.; Luebke, D.R; Kitchin, J.R; Landon, J.; Weiland, L.M.

2010-06-01T23:59:59.000Z

420

Gas turbine generators from India for Asian and world markets  

SciTech Connect

Bharat Heavy Electricals Ltd. (BHEL), in India, is an important producer of large industrial gas turbines in the Asian area. The company produces both GE frame type industrial gas turbines and Siemens design gas turbines for power generation service. Up to this time, BHEL has manufactured and supplied 68 gas turbine power generation units of GE design, ranging from Frame 1 to Frame 6 sizes, and two Siemens V94.2 gas turbines rated at 150 MW ISO. In addition, 15 gas turbine generating units are currently being manufactured. These include a large Frame 9 unit and a V94.2 gas turbine. This paper describes briefly some of the projects completed by the company.

NONE

1996-07-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

Measurements of Methane Emissions at Natural Gas Production Sites  

E-Print Network (OSTI)

Measurements of Methane Emissions at Natural Gas Production Sites in the United States #12;Why = 21 #12;Need for Study · Estimates of methane emissions from natural gas production , from academic in assumptions in estimating emissions · Measured data for some sources of methane emissions during natural gas

Lightsey, Glenn

422

Natural Gas Pipeline Research: Best Practices in Monitoring Technology  

E-Print Network (OSTI)

Natural Gas Pipeline Research: Best Practices in Monitoring Technology Energy Systems Research/index.html January 2012 The Issue California is the secondlargest natural gas consuming state in the United States, just behind Texas. About 85% of the natural gas consumed in California is delivered on interstate

423

Greater focus needed on methane leakage from natural gas infrastructure  

Science Journals Connector (OSTI)

...Fort Worth Natural Gas Air Quality Study...Fort Worth Natural Gas Air Quality Study...of SO2 from coal-fired power plants in the United...the U.S. natural gas industry. Chemosphere...SNG for Electricity Generation. Environ Sci Technol...

Ramón A. Alvarez; Stephen W. Pacala; James J. Winebrake; William L. Chameides; Steven P. Hamburg

2012-01-01T23:59:59.000Z

424

Neutron microdosimetric response of a gas electron multiplier  

Science Journals Connector (OSTI)

......avalanching structure called the gas electron multiplier...MSGC including its high cost per unit area, the inability...metallic strips, a counting gas region and a cathode...below 10 keV microm1. The production of alpha particles, through...heavy recoil ions in the gas produced the high LET......

J. Dubeau; A. J. Waker

2008-03-01T23:59:59.000Z

425

Prices for Natural Gas | Open Energy Information  

Open Energy Info (EERE)

Prices for Natural Gas Prices for Natural Gas Jump to: navigation, search Tool Summary LAUNCH TOOL Name: Prices for Natural Gas Agency/Company /Organization: Google Sector: Energy Focus Area: Economic Development Resource Type: Software/modeling tools User Interface: Website Website: www.google.com/publicdata/explore?ds=m49d2j928087j_ Country: United States Web Application Link: www.google.com/publicdata/explore?ds=m49d2j928087j_ Cost: Free Northern America Prices for Natural Gas Screenshot References: Public Data Explorer[1] EIA[2] Logo: Prices for Natural Gas Prices for Natural Gas Dollars per Thousand Cubic Feet and Percent in U.S. Total Represented by the Price. Overview A graphing tool that displays prices for natural gas dollars per thousand cubic feet and percent in U.S. Total represented by the price, using data

426

Ground Gas Handbook  

Science Journals Connector (OSTI)

...pathways of least resistance to gas transport, and applications are discussed, such as migrating landfill gas emissions, also from leaking landfill gas collection systems, as well as natural gas and oil-field gas leakage from abandoned production...

Allen W Hatheway

427

Small gas turbine technology  

Science Journals Connector (OSTI)

Small Gas Turbine Technology: Small gas turbine, in the power range up to 500 kW, requires a recuperated thermodynamic cycle to achieve an electrical efficiency of about 30%. This efficiency is the optimum, which is possible for a cycle pressure ratio of about 4–1. The cycle airflow is function of the power requirement. To increase the efficiency, in view to reduce the CO2 emission, it is mandatory to develop a more efficient thermodynamic cycle. Different thermodynamic cycles were examined and the final choice was made for an Intercooled, Recuperated cycle. The advantage of this cycle, for the same final electrical efficiency of about 35%, is the smaller cycle airflow, which is the most dimensional parameter for the important components as the heat exchanger recuperator and the combustion chamber. In parallel with the thermodynamic cycle it is necessary to develop the High Speed Alternator technology, integrated on the same shaft that the gas turbine rotating components, to achieve the constant efficiency at part loads, from 50% up to 100%, by the capacity to adjust the engine speed at the required load. To satisfy the stringent requirement in pollutant emissions of \\{NOx\\} and CO, the catalytic combustion system is the most efficient and this advance technology has to be proven. The major constraints for the small gas turbine technology development are the production cost and the maintenance cost of the unit. In the power range of 0–500 kW the gas turbine technology is in competition with small reciprocating engines, which are produced in large quantity for automotive industry, at a very low production cost.

Andre Romier

2004-01-01T23:59:59.000Z

428

Gas Delivered  

Gasoline and Diesel Fuel Update (EIA)

. Average . Average Price of Natural Gas Delivered to Residential Consumers, 1980-1996 Figure 1980 1982 1984 1986 1988 1990 1992 1994 1996 0 2 4 6 8 10 0 40 80 120 160 200 240 280 320 Dollars per Thousand Cubic Feet Dollars per Thousand Cubic Meters Nominal Dollars Constant Dollars Sources: Nominal dollars: Energy Information Administration (EIA), Form EIA-176, "Annual Report of Natural and Supplemental Gas Supply and Disposition." Constant dollars: Prices were converted to 1995 dollars using the chain-type price indexes for Gross Domestic Product (1992 = 1.0) as published by the U. S. Department of Commerce, Bureau of Economic Analysis. Residential: Prices in this publication for the residential sector cover nearly all of the volumes of gas delivered. Commercial and Industrial: Prices for the commercial and industrial sectors are often associated with

429

MS_NatGas_Studyguide.indd  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

GAS-FUELING THE GAS-FUELING THE BLUE FLAME Natural Gas: It is colorless, shapeless, and in its pure form, odorless. For many years, it was discarded as worthless. Even today, some countries (although not the United States) still get rid of it by burning it in giant fl ares, so large they can be seen from the Space Shuttle. Yet, it is one of the most valuable fuels we have. Natural gas is made up mainly of a chemical called methane: a simple compound that has a carbon atom surrounded by four hydrogen atoms. Methane is highly fl ammable and burns almost completely. Th ere is no ash and very little air pollution. Natural gas provides nearly one-quarter of all the energy used in the United States. It is especially important in homes, where it supplies nearly half of all the energy used for cooking,

430

Natural gas vehicles : Status, barriers, and opportunities.  

SciTech Connect

In the United States, recent shale gas discoveries have generated renewed interest in using natural gas as a vehicular fuel, primarily in fleet applications, while outside the United States, natural gas vehicle use has expanded significantly in the past decade. In this report for the U.S. Department of Energy's Clean Cities Program - a public-private partnership that advances the energy, economic, and environmental security of the U.S. by supporting local decisions that reduce petroleum use in the transportation sector - we have examined the state of natural gas vehicle technology, current market status, energy and environmental benefits, implications regarding advancements in European natural gas vehicle technologies, research and development efforts, and current market barriers and opportunities for greater market penetration. The authors contend that commercial intracity trucks are a prime area for advancement of this fuel. Therefore, we examined an aggressive future market penetration of natural gas heavy-duty vehicles that could be seen as a long-term goal. Under this scenario using Energy Information Administration projections and GREET life-cycle modeling of U.S. on-road heavy-duty use, natural gas vehicles would reduce petroleum consumption by approximately 1.2 million barrels of oil per day, while another 400,000 barrels of oil per day reduction could be achieved with significant use of natural gas off-road vehicles. This scenario would reduce daily oil consumption in the United States by about 8%.

Rood Werpy, M.; Santini, D.; Burnham, A.; Mintz, M.; Energy Systems

2010-11-29T23:59:59.000Z

431

From Solution to the Gas Phase: Factors That Influence Kinetic Trapping of Substance P in the Gas Phase  

E-Print Network (OSTI)

From Solution to the Gas Phase: Factors That Influence Kinetic Trapping of Substance P in the Gas, and David H. Russell*, Department of Chemistry, Texas A&M University, College Station, Texas 77843, United of gas-phase, solvent-free biomolecule ions provide a means to investigate conformational preferences

Clemmer, David E.

432

United States-Sustainable Communities Leadership Academy (SCLA) | Open  

Open Energy Info (EERE)

United States-Sustainable Communities Leadership Academy (SCLA) United States-Sustainable Communities Leadership Academy (SCLA) Jump to: navigation, search Logo: United States-Sustainable Communities Leadership Academy (SCLA) Name United States-Sustainable Communities Leadership Academy (SCLA) Agency/Company /Organization Institute for Sustainable Communities (ISC) Partner Smart Growth America, Housing and Urban Development (HUD) Sector Climate, Energy Focus Area Buildings, Economic Development, Energy Efficiency, Food Supply, Greenhouse Gas, Land Use, People and Policy, Transportation, Water Conservation Topics Adaptation, Finance, Implementation, Low emission development planning, Policies/deployment programs Program Start 2008 Program End 2015 Country United States Northern America References Sustainable Communities Leadership Academy[1]

433

Actual operating experience with a new NRU unit  

SciTech Connect

The Baker Gas Plant in the Oklahoma Panhandle is a turbo-expander plant combined with a nitrogen rejection unit (NRU). The NRU unit was installed to remove nitrogen and recover helium. Operating problems and solutions of the NRU are discussed.

McKenzie, D. [Williams Field Services, Houston, TX (United States); Brown, B.D. [ABB Randall Corp., Houston, TX (United States)

1997-12-31T23:59:59.000Z

434

Externality Regulation in Oil and Gas Encyclopedia of Energy, Natural Resource, and  

E-Print Network (OSTI)

Externality Regulation in Oil and Gas Chapter 56 Encyclopedia of Energy, Natural Resource Unitization: Compulsory unitization legislation enables a majority of producers on an oil or gas field resource, congestion exter- nality, minimum oil/gas ratio, monopsony power, pipeline transportation, no

Garousi, Vahid

435

EIA - Natural Gas Pipeline Network - Natural Gas Import/Export Locations  

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

Pipelines > Import/Export Location List Pipelines > Import/Export Location List About U.S. Natural Gas Pipelines - Transporting Natural Gas based on data through 2007/2008 with selected updates Currently, there are 58 locations at which natural gas can be exported or imported into the United States, including 9 LNG (liquefied natural gas) facilities in the continental United States and Alaska (There is a tenth U.S. LNG import facility located in Puerto Rico). At 28 of these locations natural gas or LNG currently can only be imported; while at 17 they may only be exported (1 LNG export facility is located in Alaska). At 13 of the 58 locations natural gas may, and sometimes does, flow in both directions, although at each of these sites the flow is primarily either import or export.

436

Natural Gas Processing: The Crucial Link Between Natural Gas Production and Its Transportation to Market  

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

Processing: The Crucial Link Between Natural Gas Production Processing: The Crucial Link Between Natural Gas Production and Its Transportation to Market Energy Information Administration, Office of Oil and Gas, January 2006 1 The natural gas product fed into the mainline gas transportation system in the United States must meet specific quality measures in order for the pipeline grid to operate properly. Consequently, natural gas produced at the wellhead, which in most cases contains contaminants 1 and natural gas liquids, 2 must be processed, i.e., cleaned, before it can be safely delivered to the high-pressure, long-distance pipelines that transport the product to the consuming public. Natural gas that is not within certain specific gravities, pressures, Btu content range, or water content levels will

437

Natural Gas Annual, 1999 (HISTORICAL)  

Gasoline and Diesel Fuel Update (EIA)

9 9 The Natural Gas Annual, 1999 provides information on the supply and disposition of natural gas in the United States. Production, transmission, storage, deliveries, and price data are published by State for 1999. Summary data are presented for each Census Division and State for 1995 to 1999. A section of historical data at the National level shows industry activities back to the 1930's. The data that appear in the tables of the Natural Gas Annual, 1999 are available as self-extracting executable files in ASCII TXT or CSV file formats. This volume emphasizes information for 1999, although some tables show a five-year history. Please read the file entitled README.V1 for a description and documentation of information included in this file. Also available are files containing the following data: Summary Statistics - Natural Gas in the United States, 1995-1999 (Table 1) ASCII TXT, and Natural Gas Supply and Disposition by State, 1999 (Table 2) ASCII TXT, are also available.

438

Chapter 10 - Coal and Coalbed Gas: Outlook  

Science Journals Connector (OSTI)

Abstract The future of coal and coalbed gas future is intertwined as source and reservoir rocks. Coal generates coalbed gas during coalification (e.g. thermogenic gas) and methanogenesis (biogenic gas). These gas types occur as singular and mixed accumulations. Accumulation of biogenic coalbed gas has received worldwide research and development interests on sustaining production. The new coal-to-biogenic coalbed gas technology centers on stimulating indigenous microbes in coal and associated groundwater with bioengineered nutrients and amendments to “farm” gas from abandoned wells and non-gas-producing coals. Coal mainly as a basic fuel for electric power generation since the Industrial Revolution continues to be utilized despite environmental concerns. The outlook of coal is dimmed in the United States where natural gas has replaced power generation. However, in Asia and Europe continued economic growth is going to be fueled by coal and coalbed gas as liquefied natural gas will rely on combustion from more efficient, high-temperature power plants in the future.

Romeo M. Flores

2014-01-01T23:59:59.000Z

439

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

73,669 73,669 141,300 1.59 221,822 1.12 3 0.10 46,289 0.88 33,988 1.24 31,006 0.98 252,585 1.26 A r k a n s a s Arkansas 51. Summary Statistics for Natural Gas Arkansas, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 1,750 1,552 1,607 1,563 1,470 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 3,500 3,500 3,500 3,988 4,020 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 171,543 166,273 161,967 161,390 182,895 From Oil Wells ........................................... 39,364 38,279 33,446 33,979 41,551 Total.............................................................. 210,906 204,552 195,413 195,369 224,446 Repressuring ................................................

440

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-1,080,240 -1,080,240 201,024 2.27 1,734,887 8.78 133 4.54 76,629 1.46 136,436 4.99 46,152 1.46 460,373 2.30 O k l a h o m a Oklahoma 84. Summary Statistics for Natural Gas Oklahoma, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 13,926 13,289 13,487 13,438 13,074 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 28,902 29,118 29,121 29,733 29,733 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 1,674,405 1,732,997 1,626,858 1,521,857 1,467,695 From Oil Wells ........................................... 342,950 316,945 308,006 289,877 267,192 Total.............................................................. 2,017,356 2,049,942 1,934,864

Note: This page contains sample records for the topic "gas desulfurization units" 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

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

7,038,115 7,038,115 3,528,911 39.78 13,646,477 69.09 183 6.24 408,861 7.80 1,461,718 53.49 281,452 8.91 5,681,125 28.40 West South Central West South Central 42. Summary Statistics for Natural Gas West South Central, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 87,198 84,777 88,034 88,734 62,357 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 92,212 95,288 94,233 102,525 102,864 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 11,599,913 11,749,649 11,959,444 11,824,788 12,116,665 From Oil Wells ........................................... 2,313,831 2,368,395 2,308,634 2,217,752 2,151,247 Total..............................................................

442

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

77,379 77,379 94,481 1.07 81,435 0.41 8 0.27 70,232 1.34 1,836 0.07 40,972 1.30 207,529 1.04 K e n t u c k y Kentucky 65. Summary Statistics for Natural Gas Kentucky, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 1,084 1,003 969 1,044 983 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 12,483 12,836 13,036 13,311 13,501 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 79,690 86,966 73,081 74,754 81,435 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. 79,690 86,966 73,081 74,754 81,435 Repressuring ................................................

443

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-67,648 -67,648 75,616 0.85 480,828 2.43 0 0.00 16,720 0.32 31,767 1.16 29,447 0.93 153,549 0.77 Pacific Noncontiguous Pacific Noncontiguous 45. Summary Statistics for Natural Gas Pacific Noncontiguous, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 9,638 9,907 9,733 9,497 9,294 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 112 113 104 100 102 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 198,603 190,139 180,639 179,470 183,747 From Oil Wells ........................................... 2,427,110 2,588,202 2,905,261 3,190,433 3,189,837 Total.............................................................. 2,625,713 2,778,341

444

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-310,913 -310,913 110,294 1.24 712,796 3.61 2 0.07 85,376 1.63 22,607 0.83 57,229 1.81 275,508 1.38 K a n s a s Kansas 64. Summary Statistics for Natural Gas Kansas, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 9,681 9,348 9,156 8,571 7,694 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 18,400 19,472 19,365 22,020 21,388 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 580,572 605,578 628,900 636,582 629,755 From Oil Wells ........................................... 79,169 82,579 85,759 86,807 85,876 Total.............................................................. 659,741 688,157 714,659 723,389 715,631 Repressuring ................................................

445

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

819,046 819,046 347,043 3.91 245,740 1.24 40 1.36 399,522 7.62 32,559 1.19 201,390 6.38 980,555 4.90 M i c h i g a n Michigan 70. Summary Statistics for Natural Gas Michigan, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 1,223 1,160 1,323 1,294 2,061 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 3,257 5,500 6,000 5,258 5,826 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 120,287 126,179 136,989 146,320 201,123 From Oil Wells ........................................... 80,192 84,119 91,332 97,547 50,281 Total.............................................................. 200,479 210,299 228,321 243,867 251,404 Repressuring ................................................

446

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

W W y o m i n g -775,410 50,253 0.57 666,036 3.37 14 0.48 13,534 0.26 87 0.00 9,721 0.31 73,609 0.37 Wyoming 98. Summary Statistics for Natural Gas Wyoming, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 10,826 10,933 10,879 12,166 12,320 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 3,111 3,615 3,942 4,196 4,510 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 751,693 880,596 949,343 988,671 981,115 From Oil Wells ........................................... 285,125 142,006 121,519 111,442 109,434 Total.............................................................. 1,036,817 1,022,602 1,070,862 1,100,113 1,090,549 Repressuring

447

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-67,648 -67,648 75,616 0.85 480,828 2.43 0 0.00 16,179 0.31 31,767 1.16 27,315 0.86 150,877 0.75 A l a s k a Alaska 49. Summary Statistics for Natural Gas Alaska, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 9,638 9,907 9,733 9,497 9,294 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 112 113 104 100 102 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 198,603 190,139 180,639 179,470 183,747 From Oil Wells ........................................... 2,427,110 2,588,202 2,905,261 3,190,433 3,189,837 Total.............................................................. 2,625,713 2,778,341 3,085,900 3,369,904 3,373,584 Repressuring

448

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

628,189 628,189 449,511 5.07 765,699 3.88 100 3.41 528,662 10.09 39,700 1.45 347,721 11.01 1,365,694 6.83 West North Central West North Central 39. Summary Statistics for Natural Gas West North Central, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 10,177 9,873 9,663 9,034 8,156 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 18,569 19,687 19,623 22,277 21,669 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 594,551 626,728 651,594 655,917 648,822 From Oil Wells ........................................... 133,335 135,565 136,468 134,776 133,390 Total.............................................................. 727,886 762,293

449

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

1,048,760 1,048,760 322,661 3.64 18,131 0.09 54 1.84 403,264 7.69 142,688 5.22 253,075 8.01 1,121,742 5.61 N e w Y o r k New York 80. Summary Statistics for Natural Gas New York, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 329 264 242 197 232 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 5,906 5,757 5,884 6,134 6,208 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 22,697 20,587 19,937 17,677 17,494 From Oil Wells ........................................... 824 610 539 723 641 Total.............................................................. 23,521 21,197 20,476 18,400 18,134 Repressuring ................................................

450

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

1,554,530 1,554,530 311,229 3.51 3,094,431 15.67 442 15.08 299,923 5.72 105,479 3.86 210,381 6.66 927,454 4.64 Mountain Mountain 43. Summary Statistics for Natural Gas Mountain, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 38,711 38,987 37,366 39,275 38,944 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 30,965 34,975 38,539 38,775 41,236 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 2,352,729 2,723,393 3,046,159 3,131,205 3,166,689 From Oil Wells ........................................... 677,771 535,884 472,397 503,986 505,903 Total.............................................................. 3,030,499 3,259,277 3,518,556

451

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

1,592,465 1,592,465 716,648 8.08 239,415 1.21 182 6.21 457,792 8.73 334,123 12.23 320,153 10.14 1,828,898 9.14 South Atlantic South Atlantic 40. Summary Statistics for Natural Gas South Atlantic, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 3,307 3,811 4,496 4,427 4,729 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 39,412 35,149 41,307 37,822 36,827 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 206,766 208,892 234,058 236,072 233,409 From Oil Wells ........................................... 7,584 8,011 8,468 7,133 6,706 Total.............................................................. 214,349 216,903 242,526 243,204 240,115

452

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

1,999,161 1,999,161 895,529 10.10 287,933 1.46 1,402 47.82 569,235 10.86 338,640 12.39 308,804 9.78 2,113,610 10.57 Pacific Contiguous Pacific Contiguous 44. Summary Statistics for Natural Gas Pacific Contiguous, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 3,896 3,781 3,572 3,508 2,082 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 1,142 1,110 1,280 1,014 996 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... 156,635 124,207 117,725 96,329 88,173 From Oil Wells ........................................... 294,800 285,162 282,227 289,430 313,581 Total.............................................................. 451,435 409,370

453

Natural Gas  

Gasoline and Diesel Fuel Update (EIA)

-122,394 -122,394 49,997 0.56 178,984 0.91 5 0.17 37,390 0.71 205 0.01 28,025 0.89 115,622 0.58 West Virginia West Virginia 96. Summary Statistics for Natural Gas West Virginia, 1992-1996 Table 1992 1993 1994 1995 1996 Reserves (billion cubic feet) Estimated Proved Reserves (dry) as of December 31 ....................................... 2,356 2,439 2,565 2,499 2,703 Number of Gas and Gas Condensate Wells Producing at End of Year.............................. 38,250 33,716 39,830 36,144 35,148 Production (million cubic feet) Gross Withdrawals From Gas Wells ......................................... E 182,000 171,024 183,773 186,231 178,984 From Oil Wells ........................................... 0 0 0 0 0 Total.............................................................. E 182,000 171,024 183,773 186,231 178,984 Repressuring ................................................

454

Gas vesicles.  

Science Journals Connector (OSTI)

...the gas vesicles simply reduce their sinking rates and...remaining suspended in the water column. A microorganism...phenomena as stratification, water- bloom formation, and...the many proteins that make up the phycobilisome (73...flagellate bacteria in natural waters. The natural selection...

A E Walsby

1994-03-01T23:59:59.000Z

455

Gas sensor  

DOE Patents (OSTI)

A gas sensor is described which incorporates a sensor stack comprising a first film layer of a ferromagnetic material, a spacer layer, and a second film layer of the ferromagnetic material. The first film layer is fabricated so that it exhibits a dependence of its magnetic anisotropy direction on the presence of a gas, That is, the orientation of the easy axis of magnetization will flip from out-of-plane to in-plane when the gas to be detected is present in sufficient concentration. By monitoring the change in resistance of the sensor stack when the orientation of the first layer's magnetization changes, and correlating that change with temperature one can determine both the identity and relative concentration of the detected gas. In one embodiment the stack sensor comprises a top ferromagnetic layer two mono layers thick of cobalt deposited upon a spacer layer of ruthenium, which in turn has a second layer of cobalt disposed on its other side, this second cobalt layer in contact with a programmable heater chip.

Schmid, Andreas K.; Mascaraque, Arantzazu; Santos, Benito; de la Figuera, Juan

2014-09-09T23:59:59.000Z

456

NETL: Oil & Natural Gas Technologies Reference Shelf - Presentation on Gas  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrate Energy resource Studies in the United States Hydrate Energy resource Studies in the United States Gas Hydrate Energy resource Studies in the United States Authors: T.Collett (USGS), R. Boswell (DOE), K. Rose (DOE), W. Agena (USGS), and R. Baker (DOE) Venue: American Chemical Society Meeting, March 22-26, 2009, Salt Lake City, Utah http://portal.acs.org/portal/acs/corg/content?_nfpb=true&_pageLabel=PP_MEETINGS&node_id=86&use_sec=false&__uuid=614acbfd-ce1c-4a0b-98de-348a14738f4e [external site] Abstract: In 1982, scientists onboard the Research Vessel Glomar Challenger retrieved a meter-long sample of massive gas hydrate off the coast of Guatemala. This sample became the impetus for the first United States national research and development program dedicated to gas hydrates. By the mid 1990s, it was widely accepted that gas hydrates represented a vast storehouse of gas. Recognizing the importance of gas hydrate research and the need for coordinated efforts, Congress and the President of the United States enacted Public Law 106-193, the Methane Hydrate Research and Development Act of 2000. Authorization for this program was extended to 2010 as part of the Energy Policy Act of 2005. Many of the current gas hydrate projects in the United States are conducted within this program, which is administered by the U. S. Department of Energy in collaboration with six other U.S. federal agencies, and conducted in partnership with private industry, academic institutions, and DOEÂ’s National Laboratories. In addition, other U.S. federal agencies conduct significant self-directed gas hydrate research; most notably the gas hydrate resource assessment activities conducted by U.S. Department of Interior agencies (the U.S. Geological Survey and the Minerals Management Service).

457

United States: Energy Resources | Open Energy Information  

Open Energy Info (EERE)

United States: Energy Resources United States: Energy Resources Jump to: navigation, search Click on a state to view that state's page. Country Profile Name United States Population Unavailable GDP Unavailable Energy Consumption 99.53 Quadrillion Btu 2-letter ISO code US 3-letter ISO code USA Numeric ISO code 840 UN Region[1] Northern America OpenEI Resources Energy Maps 1143 view Tools 94 view Programs 25 view Energy Organizations 8947 view Research Institutions 128 view References CIA World Factbook, Appendix D[2] Energy Resources Resource Value Units Rank Period Source Wind Potential 2,237,435 Area(km²) Class 3-7 Wind at 50m 3 1990 NREL Solar Potential 24,557,081,451 MWh/year 6 2008 NREL Coal Reserves 260,551.00 Million Short Tons 1 2008 EIA Natural Gas Reserves 6,928,000,000,000 Cubic Meters (cu m) 6 2010 CIA World Factbook

458

Natural Gas Monthly (NGM) - Energy Information Administration - November  

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

SEE CURRENT NATURAL GAS MONTHLY UPDATE SEE CURRENT NATURAL GAS MONTHLY UPDATE Natural Gas Monthly Data for September 2013 | Release Date: December 12, 2013 | Next Release: January 7, 2014 | full report  | Previous Issues Month: October 2013 September 2013 August 2013 July 2013 June 2013 May 2013 April 2013 March 2013 February 2013 January 2013 December 2012 November 2012 October 2012 September 2012 prior issues Go Table of Contentsall tables Tables 1 Summary of Natural Gas Supply and Disposition in the United States, 2008-2013 XLS PDF CSV 2 Natural Gas Consumption in the United States, 2008-2013 XLS PDF CSV 3 Selected National Average Natural Gas Prices, 2008-2013 XLS PDF CSV 4 U.S. Natural Gas Imports, 2011-2013 XLS PDF CSV 5 U.S. Natural Gas Exports, 2011-2013 XLS PDF CSV

459

Gas vesicles.  

Science Journals Connector (OSTI)

...vesicles use flagellar swimming for vertical migration...compared is in units of energy expenditure per time...produce many more; in energy-starved cells the rate...that on the basis of energy costs alone for maintaining...comparisons with flagellar swimming in eucaryotic algae...

A E Walsby

1994-03-01T23:59:59.000Z

460

Liquid Natural Gas  

Science Journals Connector (OSTI)

Liquid Natural Gas ... IN A new technique for storing natural gas at the East Ohio Gas Co. plant, Cleveland, Ohio, the gas is liquefied before passing to the gas holders. ... Natural gas contains moisture and carbon dioxide, both of which liquefy before the natural gas and are somewhat of a nuisance because upon solidification they clog the pipes. ...

W. F. SCHAPHORST

1941-04-25T23:59:59.000Z

Note: This page contains sample records for the topic "gas desulfurization units" 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

" Million Housing Units, Final...  

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

in Buildings" "With 5 or More Units)",19.1,4.4,1,0.5,0.5,3.4,2.4,0.6,0.5 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

462

" Million Housing Units, Final...  

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

"With 5 or More Units)",19.1,2.3,16.8,"N","N","N","N","N","N",2.3,16.8,"N","N" "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

463

" Million Housing Units, Final...  

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

in Buildings" "With 5 or More Units)",19.1,2,0.7,1.3,2.6,4.1,3.5,2.5,2.4 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

464

" Million Housing Units, Final...  

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

"With 5 or More Units)",19.1,6.2,3.5,0.5,0.5,1.1,0.6,"Q",0.7,0.4,0.2,2,1.4,0.6 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

465

" Million Housing Units, Final...  

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

Buildings" "With 5 or More Units)",19.1,4.7,0.9,0.4,0.3,"Q",0.6,0.4,"Q",3.8,2.9,0.9 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

466

" Million Housing Units, Final...  

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

in Buildings" "With 5 or More Units)",19.1,3.7,2.7,0.9,0.6,0.3,0.9,1,0.2,0.6,0.2 "FoundationBasement of Single-Family" "Units and Apartments in Buildings With" "2 to 4 Units...

467

Unit Testing Discussion C  

E-Print Network (OSTI)

Unit Testing Discussion C #12;Unit Test public Method is smallest unit of code Input/output transformation Test if the method does what it claims Not exactly black box testing #12;Test if (actual result Expected Computed Input #12;Functionality Computation ­ Easy to test Time based Asynchronous interaction

Massachusetts at Amherst, University of

468

NATURAL GAS MARKET ASSESSMENT  

E-Print Network (OSTI)

CALIFORNIA ENERGY COMMISSION NATURAL GAS MARKET ASSESSMENT PRELIMINARY RESULTS In Support.................................................................................... 6 Chapter 2: Natural Gas Demand.................................................................................................. 10 Chapter 3: Natural Gas Supply

469

,"Missouri Natural Gas Summary"  

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

Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)","Missouri Natural Gas Industrial Price (Dollars per Thousand Cubic Feet)","Missouri Natural Gas Price Sold to...

470

Natural Gas Weekly Update  

Annual Energy Outlook 2012 (EIA)

natural gas production output. Rigs Natural Gas Transportation Update Tennessee Gas Pipeline Company yesterday (August 4) said it is mobilizing equipment and manpower for...

471

Managing the National Greenhouse Gas Inventory Process | Open Energy  

Open Energy Info (EERE)

Managing the National Greenhouse Gas Inventory Process Managing the National Greenhouse Gas Inventory Process Jump to: navigation, search Tool Summary Name: Managing the National Greenhouse Gas Inventory Process Agency/Company /Organization: United Nations Development Programme, United Nations Environment Programme, Global Environment Facility Topics: GHG inventory Resource Type: Guide/manual, Training materials, Lessons learned/best practices Website: ncsp.undp.org/document/managing-national-greenhouse-gas-inventory-proc Managing the National Greenhouse Gas Inventory Process Screenshot References: Managing the National Greenhouse Gas Inventory Process[1] The objective of the handbook is to provide non-AnnexI Parties with a strategic and logical approach to a sustainable inventory process. About "The handbook was developed by United Nations Development Programme with

472

Shale gas is natural gas trapped inside  

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

Shale gas is natural gas trapped inside formations of shale - fine grained sedimentary rocks that can be rich sources of petroleum and natural gas. Just a few years ago, much of...

473

Gas Chromatography  

Science Journals Connector (OSTI)

Researchers from the University of Missouri and ICx Nomadics have reported on the use of a optofluidic ring resonator (OFRR) sensor for on-column detection ?. ... Although substantial differences were noted between fresh and aged (or oxidized) oils, many of the compounds in the oxidized oil went unidentified due to lack of library mass spectral data. ... A high resolution MEMS based gas chromatography column for the analysis of benzene and toluene gaseous mixtures ...

Frank L. Dorman; Joshua J. Whiting; Jack W. Cochran; Jorge Gardea-Torresdey

2010-05-26T23:59:59.000Z

474

NETL: Oil & Natural Gas Projects  

NLE Websites -- All DOE Office Websites (Extended Search)

Low Permeability Gas Low Permeability Gas Design and Implementation of Energized Fracture Treatment in Tight Gas Sands DE-FC26-06NT42955 Goal The goal of this project is to develop methods and tools that can enable operators to design, optimize, and implement energized fracture treatments in a systematic way. The simulator that will result from this work would significantly expand the use and cost-effectiveness of energized fracs and improve their design and implementation in tight gas sands. Performer University of Texas-Austin, Austin, TX Background A significant portion of U.S. natural gas production comes from unconventional gas resources such as tight gas sands. Tight gas sands account for 58 percent of the total proved natural gas reserves in the United States. As many of these tight gas sand basins mature, an increasing number of wells are being drilled or completed into nearly depleted reservoirs. This includes infill wells, recompletions, and field-extension wells. When these activities are carried out, the reservoir pressures encountered are not as high as the initial reservoir pressures. In these situations, where pressure drawdowns can be less than 2,000 psi, significant reductions in well productivity are observed, often due to water blocking and insufficient clean-up of fracture-fluid residues. In addition, many tight gas sand reservoirs display water sensitivity—owing to high clay content—and readily imbibe water due both to very high capillary pressures and low initial water saturations.

475

Table N11.4. Expenditures for Purchased Electricity, Natural Gas, and Steam, 19  

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

4. Expenditures for Purchased Electricity, Natural Gas, and Steam, 1998;" 4. Expenditures for Purchased Electricity, Natural Gas, and Steam, 1998;" " Level: National Data and Regional Totals; " " Row: NAICS Codes;" " Column: Supplier Sources of Purchased Electricity, Natural Gas, and Steam;" " Unit: Million U.S. Dollars." ,,,"Electricity","Components",,"Natural Gas","Components",,"Steam","Components" " "," ",,,"Electricity",,,"Natural Gas",,,"Steam"," ",," " " "," ",,"Electricity","from Sources",,"Natural Gas","from Sources",,"Steam","from Sources","RSE"

476

Table 7.10 Expenditures for Purchased Electricity, Natural Gas, and Steam, 2002  

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

0 Expenditures for Purchased Electricity, Natural Gas, and Steam, 2002;" 0 Expenditures for Purchased Electricity, Natural Gas, and Steam, 2002;" " Level: National and Regional Data; " " Row: NAICS Codes;" " Column: Supplier Sources of Purchased Electricity, Natural Gas, and Steam;" " Unit: Million U.S. Dollars." ,,,"Electricity","Components",,"Natural Gas","Components",,"Steam","Components" " "," ",,,"Electricity",,,"Natural Gas",,,"Steam"," ",," " " "," ",,"Electricity","from Sources",,"Natural Gas","from Sources",,"Steam","from Sources","RSE"

477

Monitoring and Assessment of Greenhouse Gas Emissions and Mitigation  

Open Energy Info (EERE)

Greenhouse Gas Emissions and Mitigation Greenhouse Gas Emissions and Mitigation Potential in Agriculture Jump to: navigation, search Logo: Monitoring and Assessment of Greenhouse Gas Emissions and Mitigation Potential in Agriculture (MAGHG) Name Monitoring and Assessment of Greenhouse Gas Emissions and Mitigation Potential in Agriculture (MAGHG) Agency/Company /Organization Food and Agriculture Organization of the United Nations Sector Climate, Land Focus Area Agriculture, Greenhouse Gas Topics GHG inventory, Low emission development planning, -LEDS Resource Type Dataset, Technical report Website http://www.fao.org/climatechan References MICCA Website[1] The overall objective of the MAGHG project is to support developing countries assess and report their greenhouse gas (GHG) emissions from

478

Rapid Gas Hydrate Formation Process Opportunity  

NLE Websites -- All DOE Office Websites (Extended Search)

Gas Hydrate Formation Process Gas Hydrate Formation Process Opportunity The Department of Energy's National Energy Technology Laboratory (NETL) is seeking collaborative research and licensing partners interested in implementing United States Non-provisional Patent Application entitled "Rapid Gas Hydrate Formation Process." Disclosed in this application is a method and device for producing gas hydrates from a two-phase mixture of water and a hydrate forming gas such as methane (CH 4 ) or carbon dioxide (CO 2 ). The two-phase mixture is created in a mixing zone, which may be contained within the body of the spray nozzle. The two-phase mixture is subsequently sprayed into a reaction vessel, under pressure and temperature conditions suitable for gas hydrate formation. The reaction

479

Clean Cities: Natural Gas Vehicle Technology Forum  

NLE Websites -- All DOE Office Websites (Extended Search)

Forum Forum Natural Gas Vehicle Technology Form (NGVTF) logo The Natural Gas Vehicle Technology Forum (NGVTF) supports development and deployment of commercially competitive natural gas engines, vehicles, and infrastructure. Learn about NGVTF's purpose, activities, meetings, stakeholders, steering committee, and webinars. Purpose Led by the National Renewable Energy Laboratory in partnership with the U.S. Department of Energy and the California Energy Commission, NGVTF unites a diverse group of stakeholders to: Share information and resources Identify natural gas engine, vehicle, and infrastructure technology targets Facilitate government-industry research, development, demonstration, and deployment (RDD&D) to achieve targets Communicate high-priority needs of natural gas vehicle end users to natural gas equipment and vehicle manufacturers

480

Gas Storage Act (Illinois) | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Gas Storage Act (Illinois) Gas Storage Act (Illinois) Gas Storage Act (Illinois) < Back Eligibility Agricultural Commercial Developer Fuel Distributor Industrial Utility Program Info State Illinois Program Type Environmental Regulations Safety and Operational Guidelines Siting and Permitting Provider Illinois Commerce Commission Any corporation which is engaged in or desires to engage in, the distribution, transportation or storage of natural gas or manufactured gas, which gas, in whole or in part, is intended for ultimate distribution to the public in the State of Illinois, if the said business of such corporation is regulated or subject to regulation under either the laws of the State of Illinois or the laws of the United States, shall have the right to enter upon, take or damage private property or any interest

Note: This page contains sample records for the topic "gas desulfurization units" 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.


481

NETL: Oil & Natural Gas Technologies Reference Shelf - Presentation on Gas  

NLE Websites -- All DOE Office Websites (Extended Search)

Gas Hydrate Research and Stratigraphic Test Results, Milne Point Unit, Alaska North Slope Gas Hydrate Research and Stratigraphic Test Results, Milne Point Unit, Alaska North Slope Gas Hydrate Research and Stratigraphic Test Results, Milne Point Unit, Alaska North Slope Authors: Robert Hunter (ASRC Energy), Scott Digert (BPXA), Tim Collett (USGS), Ray Boswell (USDOE) Venue: AAPG National Meeting Gas Hydrate session, Oral Presentation, San Antonio, TX, April 22, 2008 (http://www.AAPG.org [external site]) Abstract: This BP-DOE collaborative research project is helping determine whether or not gas hydrate can become a technically and economically recoverable gas resource. Reservoir characterization, development modeling, and associated studies indicate that 0-0.34 trillion cubic meters (TCM) gas may be technically recoverable from the estimated 0.92 TCM gas-in-place within the Eileen gas hydrate accumulation on the Alaska North Slope (ANS). Reservoir modeling indicates sufficient potential for technical recovery to justify proceeding into field operations to acquire basic reservoir and fluid data from the Mount Elbert gas hydrate prospect in the Milne Point Unit (MPU). Successful drilling and data acquisition in the Mount Elbert-01 stratigraphic test well was completed during February 3-19, 2007. Data was acquired from 131 meters of core (30.5 meters gas hydrate-bearing), extensive wireline logging, and wireline production testing operations using Modular Dynamics Testing (MDT). The stratigraphic test validated the 3D seismic interpretation of the MPU gas hydrate-bearing Mount Elbert prospect. Onsite core sub- sampling preserved samples for later analyses of interstitial water geochemistry, physical properties, thermal properties, organic geochemistry, petrophysics, and mechanical properties. MDT testing was accomplished within two gas hydrate-bearing intervals, and acquired during four long shut-in period tests. Four gas samples and one pre-gas hydrate dissociation formation water sample were collected. MDT analyses are helping to improve understanding of gas hydrate dissociation, gas production, formation cooling, and long-term production potential as well as help calibrate reservoir simulation models.

482

Natural gas dehydration by desiccant materials  

Science Journals Connector (OSTI)

Water vapor in a natural gas stream can result in line plugging due to hydrate formation, reduction of line capacity due to collection of free water in the line, and increased risk of damage to the pipeline due to the corrosive effects of water. Therefore, water vapor must be removed from natural gas to prevent hydrate formation and corrosion from condensed water. Gas dehydration is the process of removing water vapor from a gas stream to lower the temperature at which water will condense from the stream; this temperature is called the “dew point” of the gas. Molecular sieves are considered as one of the most important materials that are used as desiccant materials in industrial natural gas dehydration. This work shows a study of natural gas dehydration using 3A molecular sieve as a type of solid desiccant materials, the scope of this work was to build up a pilot scale unit for a natural gas dehydration as simulation of actual existing plant for Egyptian Western Desert Gas Company (WDGC). The effect of different operating conditions (water vapor concentration and gas flow rate) on dehydration of natural gas was studied. The experimental setup consists of cylinder filled with 3A molecular sieve to form a fixed bed, then pass through this bed natural gas with different water vapor concentration, The experimental setup is fitted with facilities to control bed pressure, flow rate, measure water vapor concentration and bed temperature, a gas heater was used to activate molecular sieve bed. Increasing water vapor concentration in inlet feed gas leads to a marked decrease in dehydration efficiency. As expected, a higher inlet flow rate of natural gas decrease dehydration efficiency. Increasing feed pressure leads to higher dehydration efficiency.

Hassan A.A. Farag; Mustafa Mohamed Ezzat; Hoda Amer; Adel William Nashed

2011-01-01T23:59:59.000Z

483

Barnett Shale Municipal Oil and Gas Ordinance Dynamics: A Spatial Perspective  

E-Print Network (OSTI)

with the recent optimization of horizontal drilling, has substantially increased United States oil and gas production. Hydrocarbon firms perfected and use hydraulic fracturing on the Barnett Shale in North Texas; due to the nature of the formation, gas companies...

Murphy, Trey Daniel-Aaron

2013-09-27T23:59:59.000Z

484

Fact #781: May 27, 2013 Top Ten Natural Gas Producing Countries...  

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

Countries Fact 781: May 27, 2013 Top Ten Natural Gas Producing Countries In 2011, Russia and the United States were by far the top natural gas producing countries, with more...

485

Utilization and Mitigation of VAM/CMM Emissions by a Catalytic Combustion Gas Turbine  

Science Journals Connector (OSTI)

A system configured with a catalytic combustion gas turbine generator unit is introduced. The system has ... Heavy Industries, Ltd., such as small gas turbines, recuperators and catalytic combustors, and catalyti...

K. Tanaka; Y. Yoshino; H. Kashihara; S. Kajita

2013-01-01T23:59:59.000Z

486

Do Americans Consume Too Little Natural Gas? An Empirical Test of Marginal Cost Pricing  

E-Print Network (OSTI)

production, and in particular, coal, are associated with considerably larger external costs than natural gas.costs of energy. In the United States, 81% of greenhouse gas emissions are derived directly from the production

Davis, Lucas; Muehlegger, Erich

2009-01-01T23:59:59.000Z

487

Real-World Greenhouse Gas Emissions from a MY2010 Diesel Truck...  

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

Real-World Greenhouse Gas Emissions from a MY2010 Diesel Truck Traveling Across the Continental United States Real-World Greenhouse Gas Emissions from a MY2010 Diesel Truck...

488

Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues  

SciTech Connect

The United States has 11 distinct natural gas pipeline corridors: five originate in the Southwest, four deliver natural gas from Canada, and two extend from the Rocky