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Note: This page contains sample records for the topic "gas processing plants" 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.


1

,"California Natural Gas Plant Processing"  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California Natural Gas Plant Processing",3,"Annual",2011,"6301967" ,"Release Date:","1031...

2

,"Texas Natural Gas Plant Processing"  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas Natural Gas Plant Processing",3,"Annual",2011,"6301967" ,"Release Date:","1031...

3

Natural Gas Processing Plant- Sulfur (New Mexico)  

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

This regulation establishes sulfur emission standards for natural gas processing plants. Standards are stated for both existing and new plants. There are also rules for stack height requirements,...

4

"NATURAL GAS PROCESSING PLANT SURVEY"  

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

2 3 "Operator Company:" "PART 3. CONTACTS" "Section A: Contact information during an emergency (such as a hurricane):" "Processing Plant Operations Contact:",,,...

5

,"New Mexico Natural Gas Plant Processing"  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","New Mexico Natural Gas Plant Processing",3,"Annual",2011,"6301967" ,"Release Date:","1031...

6

Tennessee Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

2007 2008 2009 2010 2011 View History Natural Gas Processed (Million Cubic Feet) 6,146 6,200 1989-2011 Total Liquids Extracted (Thousand Barrels) 347 356 2010-2011 Extraction Loss...

7

Natural Gas Processing Plants in the United States: 2010 Update...  

Gasoline and Diesel Fuel Update (EIA)

3. Natural Gas Processing Plants Utilization Rates Based on 2008 Flows Figure 3. Natural Gas Processing Plants Utilization Rates Based on 2008 Flows Note: Average utilization rates...

8

Natural Gas Processing Plants in the United States: 2010 ...  

U.S. Energy Information Administration (EIA)

Natural Gas Processing Plants and Production Basins, 2009 Source: U.S. Energy Information Administration, GasTran Natural Gas Transportation ...

9

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

10

CO2 Capture Membrane Process for Power Plant Flue Gas  

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

Membrane Process for Power Plant Flue Gas Background The mission of the U.S. Department of Energy's (DOE) Existing Plants, Emissions & Capture (EPEC) Research and Development (R&D)...

11

CO2 Capture Membrane Process for Power Plant Flue Gas  

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

CO CO 2 Capture Membrane Process for Power Plant Flue Gas Background The U.S. Department of Energy's (DOE) Existing Plants, Emissions & Capture (EPEC) Program is performing research to develop advanced technologies focusing on carbon dioxide (CO 2 ) emissions control for existing pulverized coal-fired plants. This new focus on post-combustion and oxy-combustion CO 2 emissions control technology, CO 2 compression, and beneficial reuse is in response to the priority for advanced

12

Demonstration plant for IGCC using the U-GAS process  

SciTech Connect

Tampella, Ltd., in cooperation with the Institute of Gas Technology (IGT), is developing the gasification technology for U-GAS{reg_sign} to produce electricity from coal using the integrated gasification combined-cycle (IGCC). The concept of IGCC is to join the clean burning gasification island with a more efficient gas and stream turbine island to produce electric power with minimal environmental impact. IGT has developed the U-GAS process to produce a low- or medium-Btu gas from different types of coal feedstocks. The process uses a combination of fluidized=bed gasification and ash agglomeration in a single-stage reactor. A 30-tons/day-capacity pilot plant located in Chicago has been used to develop the process. Feedstocks ranging from relatively unreactive metallurgical coke to highly reactive peat have been gasified successfully in the this pilot plant, indicating its ability to handle a feedstock with widely varying properties. A new 10 megawatt pilot plant has been designed and is under construction in Tampere, Finland, as the first step toward the commercialization of this technology. Tampella is planning to design and deliver a commercial-scale IGCC demonstration plant by 1994. 7 refs., 5 figs.

Lau, F.S. [Institute of Gas Technology, Chicago, IL (United States); Salo, K. [Tampella Power, Tampere (Finland)

1991-12-01T23:59:59.000Z

13

Natural gas processing plant data now available - Today in ...  

U.S. Energy Information Administration (EIA)

The EIA-757 survey has a baseline portion, Schedule A, to track the country's population of natural gas plants, and an emergency activation portion, ...

14

"NATURAL GAS PROCESSING PLANT SURVEY"  

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

1.5 hours" 1.5 hours" "NATURAL GAS PROCESSING PLANT SURVEY" "FORM EIA-757" "Schedule B: Emergency Status Report" "This report is mandatory under the Federal Energy Administration Act of 1974 (Public Law 93-275). Failure to comply may result in criminal fines, civil penalties and other sanctions as provided by law. For further information concerning sanctions and data protections see the provision on sanctions and the provision concerning the confidentiality of information in the instructions. Title 18 USC 1001 makes it a criminal offense for any person knowingly and willingly to make to any Agency or Department of the United States any false, fictitious, or fraudulent statements as to any matter within its jurisdiction."

15

Michigan Natural Gas Plant Processing - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

Natural Gas Processed (Million Cubic Feet) 33,213: 29,436: 30,008: 23,819: 22,405: 21,518: 1967-2011: Total Liquids Extracted (Thousand Barrels) 2,335: 2,547: 2,840 ...

16

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

17

Membrane Process to Sequester CO2 from Power Plant Flue Gas  

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

MeMbrane Process to sequester co MeMbrane Process to sequester co 2 froM Power Plant flue Gas Background Carbon dioxide emissions from coal-fired power plants are believed to contribute significantly to global warming climate change. The direct approach to address this problem is to capture the carbon dioxide in flue gas and sequester it underground. However, the high cost of separating and capturing CO 2 with conventional technologies prevents the adoption of this approach. This project investigates the technical and economic feasibility of a new membrane process to capture CO 2 from power plant flue gas. Description Direct CO 2 capture from power plant flue gas has been the subject of many studies. Currently, CO 2 capture with amine absorption seems to be the leading candidate technology-although membrane processes have been suggested. The principal

18

Extraction Loss of Natural Gas at Processing Plants  

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

Withdrawals from Gas Wells Gross Withdrawals from Oil Wells Gross Withdrawals from Shale Gas Wells Gross Withdrawals from Coalbed Wells Repressuring Vented and Flared...

19

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

20

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

Note: This page contains sample records for the topic "gas processing plants" 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

Membrane Process to Capture CO2 from Power Plant Flue Gas  

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

Membrane Process to Capture CO Membrane Process to Capture CO 2 from Power Plant Flue Gas Background The U.S. Department of Energy's (DOE) Innovations for Existing Plants (IEP) Program is performing research to develop advanced technologies focusing on carbon dioxide (CO 2 ) emissions control for existing pulverized coal-fired plants. This new focus on post-combustion and oxy-combustion CO 2 emissions control technology, CO 2 compression, and beneficial reuse is in response to the priority for advanced

22

Direct chlorination process for geothermal power plant off-gas - hydrogen sulfide abatement  

DOE Green Energy (OSTI)

The Direct Chlorination Process removes hydrogen sulfide from geothermal off-gases by reacting hydrogen sulfide with chlorine in the gas phase. Hydrogen chloride and elemental sulfur are formed by this reaction. The Direct Chlorination Process has been successfully demonstrated by an on-site operation of a pilot plant at the 3 M We HPG-A geothermal power plant in the Puna District on the island of Hawaii. Over 99.5 percent hydrogen sulfide removal was achieved in a single reaction state. Chlorine gas did not escape the pilot plant, even when 90 percent excess chlorine gas was used. A preliminary economic evaluation of the Direct Chlorination Process indicates that it is very competitive with the Stretford Process. Compared to the Stretford Process, the Direct Chlorination Process requires about one-third the initial capital investment and about one-fourth the net daily expenditure.

Sims, A.V.

1983-06-01T23:59:59.000Z

23

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

24

Developing a water treatment system for Subsea Gas processing plant.  

E-Print Network (OSTI)

??The petroleum industry is currently moving to meet the ever-rising demand for oil and gas production. As onshore fields become depleted and decline in production,… (more)

Honer Badi M Nazhat, Dana

2006-01-01T23:59:59.000Z

25

Natural gas processing plant data now available - Today in ...  

U.S. Energy Information Administration (EIA)

This past summer, EIA activated the baseline survey (EIA-757, Schedule A), the results of which are published in EIA's Natural Gas Annual Respondent Query System.

26

Natural Gas Processing Plants in the United States: 2010 Update...  

Annual Energy Outlook 2012 (EIA)

Natural Gas - U.S. Energy Information Administration (EIA) - U.S. Energy Information Administration (EIA) U.S. Energy Information Administration - EIA - Independent Statistics and...

27

NATURAL GAS PROCESSING PLANT SURVEY FORM EIA-757 INSTRUCTIONS ...  

U.S. Energy Information Administration (EIA)

Schedule B is the “Emergency Status Report,” which will only be activated during an emergency situation that impacts the supply of natural gas to ...

28

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

29

Direct chlorination process for geothermal power plant off-gas - hydrogen sulfide abatement  

DOE Green Energy (OSTI)

The Direct Chlorination Process removes hydrogen sulfide from geothermal off-gases by reacting hydrogen sulfide with chlorine in the gas phase. Hydrogen chloride and elemental sulfur are formed by this reaction. The Direct Chlorination Process has been successfully demonstrated by an on-site operation of a pilot plant at the 3 M We HPG-A geothermal power plant in the Puna District on the island of Hawaii. Over 99.5 percent hydrogen sulfide removal was achieved in a single reaction stage. Chlorine gas did not escape the pilot plant, even when 90 percent excess chlorine gas was used. Because of the higher cost of chemicals and the restricted markets in Hawaii, the economic viability of this process in Hawaii is questionable.

Sims, A.V.

1983-06-01T23:59:59.000Z

30

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

31

Direct Chlorination Process for geothermal power plant off-gas - hydrogen sulfide abatement  

DOE Green Energy (OSTI)

The Direct Chlorination Process removes hydrogen sulfide from geothermal off-gases by reacting hydrogen sulfide with chlorine in the gas phase. Hydrogen chloride and elemental sulfur are formed by this reaction. The Direct Chlorination Process has been successfully demonstrated by an on-site operation of a pilot plant at the 3 M We HPG-A geothermal power plant in the Puna District on the island of Hawaii. Over 99.5% hydrogen sulfide removal was achieved in a single reaction stage. Chlorine gas did not escape the pilot plant, even when 90% excess chlorine gas was used. A preliminary economic evaluation of the Direct Chlorination Process indicates that it is very competitive with the Stretford Process Compared to the Stretford Process, the Direct Chlorination process requires about one-third the initial capital investment and about one-fourth the net daily expenditure. Because of the higher cost of chemicals and the restricted markets in Hawaii, the economic viability of this process in Hawaii is questionable.

Sims, A.V.

1983-06-01T23:59:59.000Z

32

MEMBRANE PROCESS TO SEQUESTER CO2 FROM POWER PLANT FLUE GAS  

Science Conference Proceedings (OSTI)

The objective of this project was to assess the feasibility of using a membrane process to capture CO2 from coal-fired power plant flue gas. During this program, MTR developed a novel membrane (Polaris™) with a CO2 permeance tenfold higher than commercial CO2-selective membranes used in natural gas treatment. The Polaris™ membrane, combined with a process design that uses a portion of combustion air as a sweep stream to generate driving force for CO2 permeation, meets DOE post-combustion CO2 capture targets. Initial studies indicate a CO2 separation and liquefaction cost of $20 - $30/ton CO2 using about 15% of the plant energy at 90% CO2 capture from a coal-fired power plant. Production of the Polaris™ CO2 capture membrane was scaled up with MTR’s commercial casting and coating equipment. Parametric tests of cross-flow and countercurrent/sweep modules prepared from this membrane confirm their near-ideal performance under expected flue gas operating conditions. Commercial-scale, 8-inch diameter modules also show stable performance in field tests treating raw natural gas. These findings suggest that membranes are a viable option for flue gas CO2 capture. The next step will be to conduct a field demonstration treating a realworld power plant flue gas stream. The first such MTR field test will capture 1 ton CO2/day at Arizona Public Service’s Cholla coal-fired power plant, as part of a new DOE NETL funded program.

Tim Merkel; Karl Amo; Richard Baker; Ramin Daniels; Bilgen Friat; Zhenjie He; Haiqing Lin; Adrian Serbanescu

2009-03-31T23:59:59.000Z

33

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

34

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

35

6000 tpd SRC-I Demonstration Plant gas systems. Design baseline package, Volume 8. [DEA process  

SciTech Connect

Volume 8 contains the design of the fuel gas desulfurization process (DEA) and of the liquefied petroleum gases (LPG) section of the plant. The removal of acid gases is accomplished by intimately contacting the feed stream with the descending DEA solution. A partially regenerated semi-lean DEA solution is fed to an intermediate tray of the column for the bulk removal of H/sub 2/S and CO/sub 2/ while a fully regenerated lean DEA solution is fed at the top tray for the removal of the remaining acid gases in the top section of the absorber. The lean solution stream temperature is maintained at 10 to 15/sup 0/F above the absorber feed gas temperature to prevent hydrocarbon condensation in the column with consequent foaming and flooding of the column. The overhead gas (Stream 6305) leaving the H.P. DEA absorber is cooled and passed through the Sweet Gas K.O. Drum (bottom section of V-15305) to separate any condensate. The gas leaving the drum is further contacted with a 3 weight percent caustic solution in the bottom section of the Treated Gas Wash Column (T-15303) for removal of residual acid gases in order to comply with the sweet gas specifications of 1 ppMv H/sub 2/S and 10 ppMv CO/sub 2/. The LPG Recovery Unit is designed to process 15.95 MMSCFD of low pressure fuel reject gas from the HPU to recover approximately 60 percent of the propane and most of the heavier hydrocarbons. The recovered hydrocarbons are produced as liquefied petroleum gas (LPG) product. Specifications for the LPG product are: (1) Ethane/Propane (Vol/Vol) 0.02; and (2) LPG product should meet GPA Publication 2140-77 Commercial B-P mixture specifications.

1983-01-27T23:59:59.000Z

36

Importance of Processing Plant Information  

U.S. Energy Information Administration (EIA)

... new survey instrument to collect information from natural gas processing plants during non-emergency and supply-emergency conditions. ...

37

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

38

Membrane Process to Capture CO{sub 2} from Coal-Fired Power Plant Flue Gas  

SciTech Connect

This final report describes work conducted for the U.S. Department of Energy National Energy Technology Laboratory (DOE NETL) on development of an efficient membrane process to capture carbon dioxide (CO{sub 2}) from power plant flue gas (award number DE-NT0005312). The primary goal of this research program was to demonstrate, in a field test, the ability of a membrane process to capture up to 90% of CO{sub 2} in coal-fired flue gas, and to evaluate the potential of a full-scale version of the process to perform this separation with less than a 35% increase in the levelized cost of electricity (LCOE). Membrane Technology and Research (MTR) conducted this project in collaboration with Arizona Public Services (APS), who hosted a membrane field test at their Cholla coal-fired power plant, and the Electric Power Research Institute (EPRI) and WorleyParsons (WP), who performed a comparative cost analysis of the proposed membrane CO{sub 2} capture process. The work conducted for this project included membrane and module development, slipstream testing of commercial-sized modules with natural gas and coal-fired flue gas, process design optimization, and a detailed systems and cost analysis of a membrane retrofit to a commercial power plant. The Polaris™ membrane developed over a number of years by MTR represents a step-change improvement in CO{sub 2} permeance compared to previous commercial CO{sub 2}-selective membranes. During this project, membrane optimization work resulted in a further doubling of the CO{sub 2} permeance of Polaris membrane while maintaining the CO{sub 2}/N{sub 2} selectivity. This is an important accomplishment because increased CO{sub 2} permeance directly impacts the membrane skid cost and footprint: a doubling of CO{sub 2} permeance halves the skid cost and footprint. In addition to providing high CO{sub 2} permeance, flue gas CO{sub 2} capture membranes must be stable in the presence of contaminants including SO{sub 2}. Laboratory tests showed no degradation in Polaris membrane performance during two months of continuous operation in a simulated flue gas environment containing up to 1,000 ppm SO{sub 2}. A successful slipstream field test at the APS Cholla power plant was conducted with commercialsize Polaris modules during this project. This field test is the first demonstration of stable performance by commercial-sized membrane modules treating actual coal-fired power plant flue gas. Process design studies show that selective recycle of CO{sub 2} using a countercurrent membrane module with air as a sweep stream can double the concentration of CO{sub 2} in coal flue gas with little energy input. This pre-concentration of CO{sub 2} by the sweep membrane reduces the minimum energy of CO{sub 2} separation in the capture unit by up to 40% for coal flue gas. Variations of this design may be even more promising for CO{sub 2} capture from NGCC flue gas, in which the CO{sub 2} concentration can be increased from 4% to 20% by selective sweep recycle. EPRI and WP conducted a systems and cost analysis of a base case MTR membrane CO{sub 2} capture system retrofitted to the AEP Conesville Unit 5 boiler. Some of the key findings from this study and a sensitivity analysis performed by MTR include: The MTR membrane process can capture 90% of the CO{sub 2} in coal flue gas and produce high-purity CO{sub 2} (>99%) ready for sequestration. CO{sub 2} recycle to the boiler appears feasible with minimal impact on boiler performance; however, further study by a boiler OEM is recommended. For a membrane process built today using a combination of slight feed compression, permeate vacuum, and current compression equipment costs, the membrane capture process can be competitive with the base case MEA process at 90% CO{sub 2} capture from a coal-fired power plant. The incremental LCOE for the base case membrane process is about equal to that of a base case MEA process, within the uncertainty in the analysis. With advanced membranes (5,000 gpu for CO{sub 2} and 50 for CO{sub 2}/N{sub 2}), operating with no feed compression and

Merkel, Tim; Wei, Xiaotong; Firat, Bilgen; He, Jenny; Amo, Karl; Pande, Saurabh; Baker, Richard; Wijmans, Hans; Bhown, Abhoyjit

2012-03-31T23:59:59.000Z

39

CO{sub 2} Capture Membrane Process for Power Plant Flue Gas  

Science Conference Proceedings (OSTI)

Because the fleet of coal-fired power plants is of such importance to the nationâ??s energy production while also being the single largest emitter of CO{sub 2}, the development of retrofit, post-combustion CO{sub 2} capture technologies for existing and new, upcoming coal power plants will allow coal to remain a major component of the U.S. energy mix while mitigating global warming. Post-combustion carbon capture technologies are an attractive option for coal-fired power plants as they do not require modification of major power-plant infrastructures, such as fuel processing, boiler, and steam-turbine subsystems. In this project, the overall objective was to develop an advanced, hollow-fiber, polymeric membrane process that could be cost-effectively retrofitted into current pulverized coal-fired power plants to capture at least 90% of the CO{sub 2} from plant flue gas with 95% captured CO{sub 2} purity. The approach for this project tackled the technology development on three different fronts in parallel: membrane materials R&D, hollow-fiber membrane module development, and process development and engineering. The project team consisted of RTI (prime) and two industrial partners, Arkema, Inc. and Generon IGS, Inc. Two CO{sub 2}-selective membrane polymer platforms were targeted for development in this project. For the near term, a next-generation, high-flux polycarbonate membrane platform was spun into hollow-fiber membranes that were fabricated into both lab-scale and larger prototype (~2,200 ft{sup 2}) membrane modules. For the long term, a new fluoropolymer membrane platform based on poly(vinylidene fluoride) [PVDF] chemistry was developed using a copolymer approach as improved capture membrane materials with superior chemical resistance to flue-gas contaminants (moisture, SO{sub 2}, NOx, etc.). Specific objectives were: ï?· Development of new, highly chemically resistant, fluorinated polymers as membrane materials with minimum selectivity of 30 for CO{sub 2} over N{sub 2} and CO{sub 2} permeance greater than 300 gas permeation units (GPU) targeted; ï?· Development of next-generation polycarbonate hollow-fiber membranes and membrane modules with higher CO{sub 2} permeance than current commercial polycarbonate membranes; ï?· Development and fabrication of membrane hollow fibers and modules from candidate polymers; ï?· Development of a CO{sub 2} capture membrane process design and integration strategy suitable for end-of-pipe, retrofit installation; and ï?· Techno-economic evaluation of the "best" integrated CO{sub 2} capture membrane process design package In this report, the results of the project research and development efforts are discussed and include the post-combustion capture properties of the two membrane material platforms and the hollow-fiber membrane modules developed from them and the multi-stage process design and analysis developed for 90% CO{sub 2} capture with 95% captured CO{sub 2} purity.

Lora Toy; Atish Kataria; Raghubir Gupta

2011-09-30T23:59:59.000Z

40

A Monte Carlo Analysis of Gas Centrifuge Enrichment Plant Process Load Cell Data  

Science Conference Proceedings (OSTI)

As uranium enrichment plants increase in number, capacity, and types of separative technology deployed (e.g., gas centrifuge, laser, etc.), more automated safeguards measures are needed to enable the IAEA to maintain safeguards effectiveness in a fiscally constrained environment. Monitoring load cell data can significantly increase the IAEA s ability to efficiently achieve the fundamental safeguards objective of confirming operations as declared (i.e., no undeclared activities), but care must be taken to fully protect the operator s proprietary and classified information related to operations. Staff at ORNL, LANL, JRC/ISPRA, and University of Glasgow are investigating monitoring the process load cells at feed and withdrawal (F/W) stations to improve international safeguards at enrichment plants. A key question that must be resolved is what is the necessary frequency of recording data from the process F/W stations? Several studies have analyzed data collected at a fixed frequency. This paper contributes to load cell process monitoring research by presenting an analysis of Monte Carlo simulations to determine the expected errors caused by low frequency sampling and its impact on material balance calculations.

Garner, James R [ORNL; Whitaker, J Michael [ORNL

2013-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Importance of Processing Plant Information  

Reports and Publications (EIA)

This presentation provides information about the importance of information about natural gas processing plants, particularly during periods of natural gas supply disruption, such as hurricanes. It also provides information about a relatively new survey instrument to collect information from natural gas processing plants during non-emergency and supply-emergency conditions.

Information Center

2009-06-22T23:59:59.000Z

42

Importance of Processing Plant Information  

U.S. Energy Information Administration (EIA)

During an Emergency. 12. Department of Energy Situation Reports During an Energy Emergency. 13. Why Survey Natural Gas Processing Plants? 14.

43

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

44

Sauget Plant Flare Gas Reduction Project  

E-Print Network (OSTI)

Empirical analysis of stack gas heating value allowed the Afton Chemical Corporation Sauget Plant to reduce natural gas flow to its process flares by about 50% while maintaining the EPA-required minimum heating value of the gas streams.

Ratkowski, D. P.

2007-01-01T23:59:59.000Z

45

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

46

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,

47

Gas turbine plant emissions  

SciTech Connect

Many cogeneration facilities use gas turbines combined with heat recovery boilers, and the number is increasing. At the start of 1986, over 75% of filings for new cogeneration plants included plans to burn natural gas. Depending on the geographic region, gas turbines are still one of the most popular prime movers. Emissions of pollutants from these turbines pose potential risks to the environment, particularly in geographical areas that already have high concentrations of cogeneration facilities. Although environmental regulations have concentrated on nitrogen oxides (NO/sub x/) in the past, it is now necessary to evaluate emission controls for other pollutants as well.

Davidson, L.N.; Gullett, D.E.

1987-03-01T23:59:59.000Z

48

Cold End Inserts for Process Gas Waste Heat Boilers Air Products, operates hydrogen production plants, which utilize large waste heat boilers (WHB)  

E-Print Network (OSTI)

Cold End Inserts for Process Gas Waste Heat Boilers Overview Air Products, operates hydrogen production plants, which utilize large waste heat boilers (WHB) to cool process syngas. The gas enters satisfies all 3 design criteria. · Correlations relating our experimental results to a waste heat boiler

Demirel, Melik C.

49

AVESTAR® - Shale Gas Processing (SGP)  

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

Shale Gas Processing (SGP) Shale Gas Processing (SGP) SPG The shale gas revolution is transforming America's energy landscape and economy. The shale gas boom, including the Marcellus play in Appalachia, is driving job creation and investment in the energy sector and is also helping to revive other struggling sectors of the economy like manufacturing. Continued growth in domestic shale gas processing requires that energy companies maximize the efficiency and profitability from their operations through excellent control and drive maximum business value from all their plant assets, all while reducing negative environmental impact and improving safety. Changing demographics and rapidly evolving plant automation and control technologies also necessitate training and empowering the next-generation of shale gas process engineering and

50

Catalytic seawater flue gas desulfurization process: an experimental pilot plant study  

SciTech Connect

In previous articles by the authors on seawater S(IV) oxidation kinetics, a significant catalytic effect was demonstrated by means of a commercially available activated carbon. The aims of this study carried out at pilot plant scale were to assess the use of high-efficiency structured packing and to validate the positive results obtained previously in laboratory studies. A comparison between a packed tower and a spray column was made by maintaining the same desulfurization efficiency. A 47% reduction in seawater flow can be obtained with a packed tower. This option seems to be more economical, with a reduction in operation costs of least of 33%. With the appropriate activated carbon, it is possible to reach a greater oxidation rate at a low pH level than by operating conventionally at a high pH level without a catalyst. A preliminary technical and financial comparison between the advanced seawater desulfurization process (equipped with a packed tower and a catalytic oxidation plant) and the conventional process (spray tower and noncatalytic oxidation) was carried out. 18 refs., 4 figs., 4 tabs.

F. Vidal B.; P. Ollero; F.J. Gutierrez Ortiz; A. Villanueva [University of Seville, Seville (Spain). Department of Chemical and Environmental Engineering

2007-10-15T23:59:59.000Z

51

U.S. natural gas processing capacity expands rapidly - Today ...  

U.S. Energy Information Administration (EIA)

... EIA tracks shut-in natural gas processing capacity through the emergency schedule on the survey of natural gas processing plants, Form EIA-757B.

52

Gas-separation process  

DOE Patents (OSTI)

A process for separating condensable organic components from gas streams. The process makes use of a membrane made from a polymer material that is glassy and that has an unusually high free volume within the polymer material.

Toy, Lora G. (San Francisco, CA); Pinnau, Ingo (Palo Alto, CA); Baker, Richard W. (Palo Alto, CA)

1994-01-01T23:59:59.000Z

53

Pilot-Scale Demonstration of hZVI Process for Treating Flue Gas Desulfurization Wastewater at Plant Wansley, Carrollton, GA  

E-Print Network (OSTI)

The hybrid Zero Valent Iron (hZVI) process is a novel chemical treatment platform that has shown great potential in our previous bench-scale tests for removing selenium, mercury and other pollutants from Flue Gas Desulfurization (FGD) wastewater. This integrated treatment system employs new iron chemistry to create highly reactive mixture of Fe^0, iron oxides (FeOx) and various forms of Fe (II) for the chemical transformation and mineralization of various heavy metals in water. To further evaluate and develop the hZVI technology, a pilot-scale demonstration had been conducted to continuously treat 1-2 gpm of the FGD wastewater for five months at Plant Wansley, a coal-fired power plant of Georgia Power. This demonstrated that the scaled-up system was capable of reducing the total selenium (of which most was selenate) in the FGD wastewater from over 2500 ppb to below 10 ppb and total mercury from over 100 ppb to below 0.01 ppb. This hZVI system reduced other toxic metals like Arsenic (III and V), Chromium (VI), Cadmium (II), Lead (II) and Copper (II) from ppm level to ppb level in a very short reaction time. The chemical consumption was estimated to be approximately 0.2-0.4 kg of ZVI per 1 m^3 of FGD water treated, which suggested the process economics could be very competitive. The success of the pilot test shows that the system is scalable for commercial application. The operational experience and knowledge gained from this field test could provide guidance to further improvement of technology for full scale applications. The hZVI technology can be commercialized to provide a cost-effective and reliable solution to the FGD wastewater and other metal-contaminated waste streams in various industries. This technology has the potential to help industries meet the most stringent environmental regulations for heavy metals and nutrients in wastewater treatment.

Peddi, Phani 1987-

2011-12-01T23:59:59.000Z

54

Gas-separation process  

DOE Patents (OSTI)

A process is described for separating condensable organic components from gas streams. The process makes use of a membrane made from a polymer material that is glassy and that has an unusually high free volume within the polymer material. 6 figures.

Toy, L.G.; Pinnau, I.; Baker, R.W.

1994-01-25T23:59:59.000Z

55

Unusual plant features gas turbines  

SciTech Connect

Gas turbines were chosen by Phillips Petroleum Co. to operate the first gas-injection plant in the world to use gas-type turbines to drive reciprocating compressors. The plant is located in Lake Maracaibo, Venezuela. Gas turbines were chosen because of their inherent reliability as prime movers and for their lack of vibration. Reciprocating compressors were decided upon because of their great flexibility. Now, for the first time, the advantages of both gas turbines and reciprocating compressors are coupled on a very large scale. In this installation, the turbines will operate at about 5,000 rpm, while the compressors will run at only 270 rpm. Speed will be reduced through the giant gear boxes. The compressor platform rests on seventy- eight 36-in. piles in 100 ft of water. Piles were driven 180 ft below water level. To dehydrate the gas, Phillips will install a triethylene glycol unit. Two nearby flow stations will gather associated gas produced at the field and will pipe the gas underwater to the gas injection platform. Lamar Field is in the S. central area of Lake Maracaibo. To date, it has produced a 150 million bbl in 10 yr. Studies have indicated that a combination of waterflooding and repressuring by gas injection could double final recovery. Waterflooding began in 1963.

Franco, A.

1967-08-01T23:59:59.000Z

56

EIA-816 MONTHLY NATURAL GAS PLANT LIQUIDS REPORT INSTRUCTIONS ...  

U.S. Energy Information Administration (EIA)

EIA-816, Monthly Natural Gas Plant Liquids Report Page 3 Inputs During Month Report only inputs of normal butane being converted by an isomerization process into ...

57

First U. S. sulfreen unit in Dakota gas plant  

SciTech Connect

This article describes the first natural gas processing plant in the U.S. that uses Sulfreen as the optimum process for tail gas cleanup. A minimum overall recovery of 98.9% is expected. The Sulfreen process appears to be a viable tail gas treater for Claus units in the U.S., providing high overall recoveries and process reliability. The North Dakota plant joins more than 30 other units operating in Canada, Greece, China and throughout Europe.

Davis, G.W.

1985-02-25T23:59:59.000Z

58

Power plants with topping gas turbines and coal gasification planning of new plants and upgrading of existing plants  

Science Conference Proceedings (OSTI)

This paper reports on existing and new power plants improved environmentally and economically by integrating gas turbines in the plant process. The rate of additional firing has an influence on the overall plant efficiency. The influence of the additional firing of natural gas-fired power plants is compared to that of power plants with integrated coal gasification. The differences are explained. The result of the examination lead to recommendations for the design of new plants and for upgrading of existing plants. The advantages of topping gas turbines are shown by examples of new power plants and upgraded plants.

Schoedel, J.; Mertens, K. (ABB Kraftwerke AG, Mannheim (DE))

1990-01-01T23:59:59.000Z

59

Natural gas conversion process  

Science Conference Proceedings (OSTI)

The experimental apparatus was dismantled and transferred to a laboratory space provided by Lawrence Berkeley Laboratory (LBL) which is already equipped with a high-ventilation fume hood. This will enable us to make tests at higher gas flow rates in a safe environment. Three papers presented at the ACS meeting in San Francisco (Symposium on Natural Gas Upgrading II) April 5--10, 1992 show that the goal of direct catalytic conversion of Methane into heavier Hydrocarbons in a reducing atmosphere is actively pursued in three other different laboratories. There are similarities in their general concept with our own approach, but the temperature range of the experiments reported in these recent papers is much lower and this leads to uneconomic conversion rates. This illustrates the advantages of Methane activation by a Hydrogen plasma to reach commercial conversion rates. A preliminary process flow diagram was established for the Integrated Process, which was outlined in the previous Quarterly Report. The flow diagram also includes all the required auxiliary facilities for product separation and recycle of the unconverted feed as well as for the preparation and compression of the Syngas by-product.

Not Available

1992-01-01T23:59:59.000Z

60

Natural Gas Processed  

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

Gross Withdrawals From Gas Wells Gross Withdrawals From Oil Wells Gross Withdrawals From Shale Gas Wells Gross Withdrawals From Coalbed Wells Repressuring Nonhydrocarbon Gases...

Note: This page contains sample records for the topic "gas processing plants" 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

Evaluation of gasification and gas cleanup processes for use in molten carbonate fuel cell power plants. Final report. [Contains lists and evaluations of coal gasification and fuel gas desulfurization processes  

DOE Green Energy (OSTI)

This report satisfies the requirements for DOE Contract AC21-81MC16220 to: List coal gasifiers and gas cleanup systems suitable for supplying fuel to molten carbonate fuel cells (MCFC) in industrial and utility power plants; extensively characterize those coal gas cleanup systems rejected by DOE's MCFC contractors for their power plant systems by virtue of the resources required for those systems to be commercially developed; develop an analytical model to predict MCFC tolerance for particulates on the anode (fuel gas) side of the MCFC; develop an analytical model to predict MCFC anode side tolerance for chemical species, including sulfides, halogens, and trace heavy metals; choose from the candidate gasifier/cleanup systems those most suitable for MCFC-based power plants; choose a reference wet cleanup system; provide parametric analyses of the coal gasifiers and gas cleanup systems when integrated into a power plant incorporating MCFC units with suitable gas expansion turbines, steam turbines, heat exchangers, and heat recovery steam generators, using the Westinghouse proprietary AHEAD computer model; provide efficiency, investment, cost of electricity, operability, and environmental effect rankings of the system; and provide a final report incorporating the results of all of the above tasks. Section 7 of this final report provides general conclusions.

Jablonski, G.; Hamm, J.R.; Alvin, M.A.; Wenglarz, R.A.; Patel, P.

1982-01-01T23:59:59.000Z

62

Optimization system for operation of gas cogeneration power plant  

Science Conference Proceedings (OSTI)

The paper presents a distributed control system for the realization of cogenerative supply of electricity and heat and, in given case, for their combination with waste heat recovery, particularly in combined (gas-steam) cycle industrial power plants. ... Keywords: cogenerative gas power plant, control of distributed parameter systems, optimization, process control

Ion Miciu

2008-09-01T23:59:59.000Z

63

Microsoft Word - RBL-RUL_Gas-Plant  

Office of Legacy Management (LM)

Page 1 Project Rulison Monitoring Results For Separated Water at a Natural Gas Plant, Parachute, Colorado U.S. Department of Energy Office of Legacy Management Grand Junction,...

64

,"Natural Gas Plant Liquids Proved Reserves"  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Natural Gas Plant Liquids Proved Reserves",49,"Annual",2011,"6301979" ,"Release Date:","81...

65

,"Natural Gas Plant Liquids Proved Reserves"  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Natural Gas Plant Liquids Proved Reserves",49,"Annual",2011,"6301979" ,"Release...

66

,"Texas Natural Gas Plant Fuel Consumption (MMcf)"  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas Natural Gas Plant Fuel Consumption (MMcf)",1,"Annual",2011 ,"Release Date:","1031...

67

Proceedings: EPRI Manufactured Gas Plants 2003 Forum  

SciTech Connect

The EPRI Manufactured Gas Plants 2003 Forum covered a range of topics related to remediation and management of former manufactured gas plant (MGP) sites, with emphasis on technological advances and current issues associated with site cleanup. In specific, the forum covered MGP coal-tar delineation, soil and groundwater remediation technologies, improvements in air monitoring, and ecological risk characterization/risk management tools.

None

2004-02-01T23:59:59.000Z

68

Improving steam turbine-gas turbine plants  

SciTech Connect

Leningrad Polytechnic Institute investigated the main characteristics of combined plants according to their structure, determined by very important parameters. The following parameters were selected: utilization factor (ratio of heat added to the steam-water working medium from the heat of the exhaust gases to the entire amount of heat added to the steam-water working medium) and fuel consumption factor (ratio of heat from fuel added to the steam-water working medium to the entire consumption of heat in the combined plant). It is concluded that steam turbine-gas turbine plants working at comparatively low gas temperatures (about 800/sup 0/C) must be constructed as plants of maximum capacity, i.e., with large steam flows. Gas turbine-steam turbine plants with high-temperature gas turbines operating at a high utilization factor (approaching binary plants) ensure a qualitative rise in efficiency and have high flexibility characteristics. They are the most promising power plants. A long-term plan for development of combined plants on the basis of standard steam turbine and gas turbine equipment, the production of which is planned in the USSR and in Comecon countries, is required. This plan must be closely connected with solution of the problem of using coals for gas turbine plants.

Kirillov, I.I.; Arsen' ev, L.V.; Khodak, E.A.; Romakhova, G.A.

1979-01-01T23:59:59.000Z

69

EIA - Natural Gas Pipeline Network - Transportation Process & Flow  

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

Process and Flow Process and Flow About U.S. Natural Gas Pipelines - Transporting Natural Gas based on data through 2007/2008 with selected updates Transportation Process and Flow Overview | Gathering System | Processing Plant | Transmission Grid | Market Centers/Hubs | Underground Storage | Peak Shaving Overview Transporting natural gas from the wellhead to the final customer involves several physical transfers of custody and multiple processing steps. A natural gas pipeline system begins at the natural gas producing well or field. Once the gas leaves the producing well, a pipeline gathering system directs the flow either to a natural gas processing plant or directly to the mainline transmission grid, depending upon the initial quality of the wellhead product.

70

Process for the desulfurization of flue gas  

SciTech Connect

A process for the removal of sulfur oxides from gases is described that is comprised of the steps of contacting the gas with a cerium oxide sorbent at conditions whereby the sulfur oxides present in the gas are sorbed by the cerium oxide sorbent and regenerate the cerium oxide sorbent by contacting it with a reducing atmosphere at conditions whereby the sorbent is substantially converted to a sulfur-free state. The gas may be an exhaust gas, e.g., from an automobile or a flue gas. This invention is especially preferred for treating flue gas. In this preferred embodiment, the flue gas may be contacted with the cerium oxide sorbent at a temperature of from 300/sup 0/ to 800/sup 0/C, to form cerium sulfate and/or sulfite and the sorbent is regenerated by contacting with a reducing gas, for example, hydrogen in admixture with steam or other inert gases at a temperature of from 500/sup 0/ to 800/sup 0/C to convert the cerium sulfate or sulfite to cerium oxide. During the regeneration step, the desorbed species is initially sulfur dioxide. However, when about 50% of the sulfur is removed from the sorbent, the desorbed species becomes H/sub 2/S. Thus, the instant invention provides SO/sub 2/ and H/sub 2/S in admixture with the excess reducing gas, which can be fed conveniently to the Claus plant for conversion into elemental sulfur.

Longo, J.M.

1977-01-04T23:59:59.000Z

71

Direct coal-fired gas turbines for combined cycle plants  

SciTech Connect

The combustion/emissions control island of the CFTCC plant produces cleaned coal combustion gases for expansion in the gas turbine. The gases are cleaned to protect the turbine from flow-path degeneration due to coal contaminants and to reduce environmental emissions to comparable or lower levels than alternate clean coal power plant tedmologies. An advantage of the CFTCC system over other clean coal technologies using gas turbines results from the CFTCC system having been designed as an adaptation to coal of a natural gas-fired combined cycle plant. Gas turbines are built for compactness and simplicity. The RQL combustor is designed using gas turbine combustion technology rather than process plant reactor technology used in other pressurized coal systems. The result is simpler and more compact combustion equipment than for alternate technologies. The natural effect is lower cost and improved reliability. In addition to new power generation plants, CFTCC technology will provide relatively compact and gas turbine compatible coal combustion/emissions control islands that can adapt existing natural gas-fired combined cycle plants to coal when gas prices rise to the point where conversion is economically attractive. Because of the simplicity, compactness, and compatibility of the RQL combustion/emission control island compared to other coal technologies, it could be a primary candidate for such conversions.

Rothrock, J.; Wenglarz, R.; Hart, P.; Mongia, H.

1993-11-01T23:59:59.000Z

72

Implementation of on-line control in chemical process plants  

Science Conference Proceedings (OSTI)

A range of identification, estimation and control algorithms has been implemented and tested on a chemical process plant/process control computer system which is typical of installations in the process industries. The plants studied are a gas-separating ... Keywords: Adaptive control, Kalman filters, chemical industry, computer control, fluid composition control, multivariable control systems, nonlinear systems, optimal control, parameter estimation, stochastic control

L. S. Kershenbaum; T. R. Fortescue

1981-11-01T23:59:59.000Z

73

Process gas solidification system  

DOE Patents (OSTI)

It has been the practice to (a) withdraw hot, liquid UF.sub.6 from various systems, (b) direct the UF.sub.6 into storage cylinders, and (c) transport the filled cylinders to another area where the UF.sub.6 is permitted to solidify by natural cooling. However, some hazard attends the movement of cylinders containing liquid UF.sub.6, which is dense, toxic, and corrosive. As illustrated in terms of one of its applications, the invention is directed to withdrawing hot liquid UF.sub.6 from a system including (a) a compressor for increasing the pressure and temperature of a stream of gaseous UF.sub.6 to above its triple point and (b) a condenser for liquefying the compressed gas. A network containing block valves and at least first and second portable storage cylinders is connected between the outlet of the condenser and the suction inlet of the compressor. After an increment of liquid UF.sub.6 from the condenser has been admitted to the first cylinder, the cylinder is connected to the suction of the compressor to flash off UF.sub.6 from the cylinder, thus gradually solidifying UF.sub.6 therein. While the first cylinder is being cooled in this manner, an increment of liquid UF.sub.6 from the condenser is transferred into the second cylinder. UF.sub.6 then is flashed from the second cylinder while another increment of liquid UF.sub.6 is being fed to the first. The operations are repeated until both cylinders are filled with solid UF.sub.6, after which they can be moved safely. As compared with the previous technique, this procedure is safer, faster, and more economical. The method also provides the additional advantage of removing volatile impurities from the UF.sub.6 while it is being cooled.

Fort, William G. S. (Oak Ridge, TN); Lee, Jr., William W. (Oak Ridge, TN)

1978-01-01T23:59:59.000Z

74

New type gas-injection plant readied  

SciTech Connect

A unique gas-injection plant is about to go on stream in Venezuela's Lake Maracaibo. The $10-million installation, designed for unattended operation, is a joint venture of Phillips Petroleum Co., as operator for itself, and Cia. Shell de Venezuela. The plant, housed on a 120 by 130-ft platform, will be the first in the world to use gas turbines to drive reciprocating compressors. The 130 MMscfd facility will use 2 General Electric 15,000-hp gas turbines with gear reducers to drive a pair of 4-stage Cooper- Bessemer LM-8 compressors. No previous attempt has ever been made to drive this type of unit by gas turbines. Phillips says the gas turbines were selected because of inherent flexibility reliability as prime movers, and lack of vibration--an important advantage in offshore gas plants.

Franco, A.

1967-07-17T23:59:59.000Z

75

Gas turbine-steam power plant  

SciTech Connect

The pressure vessel of the gas turbine-steam power plant is provided with a recuperator and a heat exchanger in order to reduce the temperature of the hot flue gas before separating out gas-entrained particles. The dust separator is connected to the recuperator on a secondary side so that the hot gas can be reheated for delivery to the gas turbine. By cooling the flue gas before entering the separator, use can be made of electrostatic dust filters or cloth filters.

Aguet, E.

1984-07-31T23:59:59.000Z

76

Energy Saving in Ammonia Plant by Using Gas Turbine  

E-Print Network (OSTI)

An ammonia plant, in which the IHI-SULZER Type 57 Gas Turbine is integrated in order to achieve energy saving, has started successful operation. Tile exhaust gas of the gas turbine has thermal energy of relatively high temperature, therefore, if the thermal energy of this gas is utilized effectively, the gas turbine could be superior to effectively, the gas turbine could be superior to other thermal engines in view of total energy effectiveness. As a typical example of the above use of the gas turbine, its application in the ammonia plant has now been realized. In addition to the use of the gas turbine as the driver for the process air compressor which was driven by the steam turbine, its exhaust gas is introduced to the ammonia reformer. It leads to the saving of the reformer fuel, and subsequently the energy saving of the reformer section in the plant of about 20% has been achieved. This paper describes the outline of the project, energy saving effectiveness and investigation for the application of the gas turbine in the ammonia plant.

Uji, S.; Ikeda, M.

1981-01-01T23:59:59.000Z

77

Illinois Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Natural Gas Processed (Million Cubic Feet) Natural Gas Processed (Million Cubic Feet) Illinois Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 483,902 483,336 478,291 1970's 429,691 341,750 376,310 358,142 342,046 322,393 305,441 275,060 327,451 1980's 150,214 152,645 166,568 156,791 153,419 146,463 106,547 757 509 1990's 607 951 942 809 685 727 578 500 468 358 2000's 271 233 299 306 328 280 242 235 233 164 2010's 5,393 15,727 0 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Illinois Natural Gas Plant Processing

78

Florida Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Natural Gas Processed (Million Cubic Feet) Natural Gas Processed (Million Cubic Feet) Florida Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 0 0 0 1970's 0 0 0 375,090 409,248 765,597 854,064 886,147 859,996 1980's 279,690 272,239 270,004 265,840 247,870 218,288 228,721 226,028 260,627 1990's 258,984 222,893 226,254 207,975 10,265 9,061 8,514 8,364 8,174 8,439 2000's 7,844 7,186 6,063 5,771 4,805 3,584 3,972 2,422 300 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 1/7/2014 Next Release Date: 1/31/2014 Referring Pages: Natural Gas Processed Florida Natural Gas Plant Processing

79

Optimization models of gas recovery and gas condensate processing  

Science Conference Proceedings (OSTI)

We present a complex of mathematical models that formalize gas recovery and processing. Optimization problems for gas recovery and gas condensate processing are stated and corresponding solution algorithms are suggested. These mathematical models provide ...

M. Kh. Prilutskii; V. E. Kostyukov

2012-05-01T23:59:59.000Z

80

Utah Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

93,836 195,701 202,380 412,639 454,832 490,233 1967-2011 Total Liquids Extracted (Thousand Barrels) 2,418 2,241 2,643 6,527 7,648 10,805 1983-2011 Extraction Loss (Million Cubic...

Note: This page contains sample records for the topic "gas processing plants" 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

California Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

223,580 206,239 195,272 198,213 204,327 180,648 1967-2011 Total Liquids Extracted (Thousand Barrels) 11,267 11,388 11,179 11,042 10,400 9,831 1983-2011 Extraction Loss (Million...

82

Ohio Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

2,397 1,456 1981-2007 Total Liquids Extracted (Thousand Barrels) 5 8 1983-2007 Extraction Loss (Million Cubic Feet) 5 9 0 0 0 0 1981...

83

Michigan Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

33,213 29,436 30,008 23,819 22,405 21,518 1967-2011 Total Liquids Extracted (Thousand Barrels) 2,335 2,547 2,840 2,409 2,207 2,132 1983-2011 Extraction Loss (Million Cubic Feet)...

84

Colorado Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

751,036 888,705 1,029,641 1,233,260 1,434,003 1,507,467 1967-2011 Total Liquids Extracted (Thousand Barrels) 26,111 27,447 37,804 47,705 57,924 63,075 1983-2011 Extraction Loss...

85

Illinois Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

242 235 233 164 5,393 15,727 1967-2011 Total Liquids Extracted (Thousand Barrels) 37 38 33 24 231 705 1983-2011 Extraction Loss (Million Cubic Feet) 47 48 42 31 345 1,043...

86

Arkansas Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

87

Colorado Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

88

Oklahoma Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

89

Alaska Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

90

Kansas Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

91

Kentucky Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

92

Florida Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

93

Montana Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

94

California Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

95

Michigan Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

96

Alabama Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

97

Nebraska Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

98

Mississippi Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

99

Louisiana Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

100

Pennsylvania Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

Note: This page contains sample records for the topic "gas processing plants" 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

Texas Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

102

Ohio Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

103

Tennessee Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

104

Illinois Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

105

Indiana Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

106

California Federal Offshore Natural Gas Plant Liquids, Proved...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) California Federal Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

107

California State Offshore Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) California State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

108

California - Los Angeles Basin Onshore Natural Gas Plant Liquids...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) California - Los Angeles Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2...

109

California--Coastal Region Onshore Natural Gas Plant Liquids...  

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

Coastal Region Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) California--Coastal Region Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels)...

110

California - Coastal Region Onshore Natural Gas Plant Liquids...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) California - Coastal Region Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2...

111

Louisiana - South Onshore Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Louisiana - South Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

112

Gulf of Mexico Federal Offshore - Texas Natural Gas Plant Liquids...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Gulf of Mexico Federal Offshore - Texas Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1...

113

California--San Joaquin Basin Onshore Natural Gas Plant Liquids...  

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

San Joaquin Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) California--San Joaquin Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

114

Utah and Wyoming Natural Gas Plant Liquids, Proved Reserves ...  

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

and Wyoming Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Utah and Wyoming Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2...

115

California--Los Angeles Basin Onshore Natural Gas Plant Liquids...  

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

Los Angeles Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) California--Los Angeles Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

116

South Dakota Natural Gas Lease and Plant Fuel Consumption (Million...  

Gasoline and Diesel Fuel Update (EIA)

View History: Annual Download Data (XLS File) South Dakota Natural Gas Lease and Plant Fuel Consumption (Million Cubic Feet) South Dakota Natural Gas Lease and Plant Fuel...

117

Microsoft Word - RBL-RUL_Gas-Plant  

Office of Legacy Management (LM)

Page 1 Project Rio Blanco Monitoring Results For Separated Water at a Natural Gas Plant, Parachute, Colorado U.S. Department of Energy Office of Legacy Management Grand Junction,...

118

Optimize control of natural gas plants  

SciTech Connect

Multivariable constraint control (MCS) has a very beneficial and profitable impact on the operation of natural gas plants. The applications described operate completely within a distributed control system (DCS) or programmable logic controllers (PLCs). That makes MCS accessible to almost all gas plant operators. The technology's relative ease of use, low maintenance effort and software sensor,'' make it possible to operate these control applications without increasing technical support staff. MCS improves not only profitability but also regulatory compliance of gas plants. It has been applied to fractionation units, cryogenic units, amine treaters, sulfur recovery units and utilities. The application typically pay for the cost of software and engineering in less than one month. If a DCS is installed within such a project the advanced control applications can generate a payout in less than one year. In the case here (an application on the deethanizers of a 500 MMscfd gas plant) product revenue increased by over $2 million/yr.

Treiber, S.; Walker, J.; Tremblay, M. de (Treiber Controls Inc., Toronto, Ontario (Canada)); Delgadillo, R.L.; Velasquez, R.N.; Valarde, M.J.G. (PEMEX, Villahermosa (Mexico))

1994-04-01T23:59:59.000Z

119

Combustion gas turbine/steam generator plant  

SciTech Connect

A fired steam generator is described that is interconnected with a gas turbine/steam generator plant having at least one gas turbine group followed by an exhaust-gas steam generator. The exhaust-gas steam generator has a preheater and an evaporator. The inlet of the preheater is connected to a feedwater distribution line which also feeds a preheater in the fired steam generator. The outlet of the preheater is connected to the evaporator of the fired steam generator. The evaporator outlet of the exhaust-gas steam generator is connected to the input of a superheater in the fired steam generator.

Aguet, E.

1975-11-18T23:59:59.000Z

120

Industrial Fuel Gas Demonstration Plant Program. Annual progress report, January-December 1979  

SciTech Connect

The objective of the Industrial Fuel Gas Demonstration Plant Program is to demonstrate the feasibility of converting agglomerating and high sulfur coal to clean fuel gas and utilizing this gas in a commercial application. Specific objectives are to conduct process analysis, design, construction, testing, operation and evaluation of a plant based on the U-Gas process for converting coal to industrial fuel gas. Phase I of the MLGW Industrial Fuel Gas Demonstration Plant Program started in September, 1977. In the first quarter of 1978, a conceptual design of a commercial plant was started, together with environmental monitoring activities and technical support work at the U-Gas pilot plant. After a series of successful pilot plant runs during the October 1978-March 1979 period, design work on the Demonstration Plant commenced. With the exception of Task I - Design and Evaluation of Commercial Plant, the majority of all other efforts were completed in 1979. These tasks are listed.

None

1980-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

California - Los Angeles Basin Onshore Natural Gas Plant ...  

U.S. Energy Information Administration (EIA)

California - Los Angeles Basin Onshore Natural Gas Plant Liquids, Reserves New Field Discoveries (Million Barrels)

122

California - Los Angeles Basin Onshore Natural Gas Plant ...  

U.S. Energy Information Administration (EIA)

California - Los Angeles Basin Onshore Natural Gas Plant Liquids, Reserves Acquisitions (Million Barrels)

123

U.S. Gas Plant Production of Natural Gas Liquids and Liquid ...  

U.S. Energy Information Administration (EIA)

U.S. Gas Plant Production of Natural Gas Liquids and Liquid Refinery Gases (Thousand Barrels per Day)

124

LPG-recovery processes for baseload LNG plants examined  

SciTech Connect

With demand on the rise, LPG produced from a baseload LNG plant becomes more attractive as a revenue-earning product similar to LNG. Efficient use of gas expanders in baseload LNG plants for LPG production therefore becomes more important. Several process variations for LPG recovery in baseload LNG plants are reviewed here. Exergy analysis (based on the Second Law of Thermodynamics) is applied to three cases to compare energy efficiency resulting from integration with the main liquefaction process. The paper discusses extraction in a baseload plant, extraction requirements, process recovery parameters, extraction process variations, and exergy analysis.

Chiu, C.H. [Bechtel Corp., Houston, TX (United States)

1997-11-24T23:59:59.000Z

125

Montana Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Montana Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 60,500 59,058 57,793 1970's 59,193 57,105 61,757 56,960 146,907 156,203 0 0 0 1980's 11,825 13,169 15,093 16,349 19,793 16,212 14,177 15,230 15,475 1990's 14,629 14,864 12,697 11,010 10,418 9,413 10,141 8,859 8,715 5,211 2000's 5,495 5,691 6,030 6,263 6,720 10,057 12,685 13,646 13,137 12,415 2010's 12,391 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Montana Natural Gas Plant Processing

126

Utah Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Utah Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 0 0 0 1970's 0 0 0 0 0 0 0 0 0 1980's 68,211 95,670 93,934 98,598 99,233 241,904 274,470 286,592 286,929 1990's 334,067 333,591 319,017 348,010 368,585 308,174 265,546 249,930 242,070 211,514 2000's 169,553 166,505 136,843 161,275 193,093 187,524 193,836 195,701 202,380 412,639 2010's 454,832 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Utah Natural Gas Plant Processing

127

Alabama Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Alabama Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 57,208 1970's 0 0 0 0 0 0 25,517 31,610 32,806 1980's 38,572 41,914 38,810 42,181 45,662 48,382 49,341 52,511 55,939 1990's 58,136 76,739 126,910 132,222 136,195 118,688 112,868 114,411 107,334 309,492 2000's 372,136 285,953 290,164 237,377 263,426 255,157 287,278 257,443 253,028 248,232 2010's 242,444 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Alabama Natural Gas Plant Processing

128

Pennsylvania Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Pennsylvania Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 2,247 2,390 1,708 1970's 1,418 1,112 1,711 0 0 0 0 0 0 1980's 2,001 2,393 5,432 6,115 5,407 6,356 6,459 6,126 6,518 1990's 6,613 10,244 11,540 10,263 7,133 10,106 10,341 11,661 11,366 11,261 2000's 7,758 9,928 7,033 9,441 9,423 11,462 12,386 13,367 18,046 22,364 2010's 56,162 131,959 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Pennsylvania Natural Gas Plant Processing

129

Mississippi Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Mississippi Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 46,068 44,510 0 1970's 50,509 44,732 29,538 29,081 24,568 29,694 0 0 0 1980's 34,337 38,315 29,416 29,705 23,428 21,955 12,131 9,565 8,353 1990's 7,887 7,649 4,822 4,892 5,052 4,869 4,521 4,372 3,668 135,773 2000's 205,106 239,830 263,456 283,675 283,763 292,023 278,436 224,596 174,573 215,951 2010's 218,840 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed Mississippi Natural Gas Plant Processing

130

Constrained model predictive control implementation for a heavy-duty gas turbine power plant  

Science Conference Proceedings (OSTI)

In this paper, model predictive control (MPC) strategy is implemented to a GE9001E gas turbine power plant. A linear model is developed for the gas turbine using conventional mathematical models and ARX identification procedure. Also a process control ... Keywords: ARX, PID, gas turbine, identification, modeling, multivariable control, power plant, predictive control

Hadi Ghorbani; Ali Ghaffari; Mehdi Rahnama

2008-06-01T23:59:59.000Z

131

Office of Enforcement and Oversight's Office of Safety and Emergency Management Evaluations Activity Report for Observation of Waste Treatment and Immobilization Plant LAW Melter and Melter Off-gas Process System Hazards Analysis _Oct 21-31  

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

HSS Independent Activity Report - HSS Independent Activity Report - Rev. 0 Report Number: HIAR-WTP-2013-10-21 Site: Hanford Site Subject: Office of Enforcement and Oversight's Office of Safety and Emergency Management Evaluations Activity Report for Observation of Waste Treatment and Immobilization Plant Low Activity Waste Melter and Melter Off-gas Process System Hazards Analysis Activities Dates of Activity : 10/21/13 - 10/31/13 Report Preparer: James O. Low Activity Description/Purpose: The Office of Health, Safety and Security (HSS), Office of Safety and Emergency Management Evaluations (Independent Oversight) reviewed the Insight software hazard evaluation (HE) tables for hazard analysis (HA) generated to date for the Waste Treatment and Immobilization Plant (WTP) Low Activity Waste (LAW) Melter and Off-gas systems, observed a

132

Coke oven gas desulphurization by the Carl Still process  

SciTech Connect

The Steubenville East Coke Plant need a desulfurization process that would desulfurize an eventual 95 million standard cubic feet per day of coke oven gas from an inlet of 450 gr/DSCF to an outlet of 45 gr/DSCF of hydrogen sulfide. The Dravo/Still plant process was selected, due to the use of ammonia which was available in the gas, as the absorbing agent. It was also a proven process. Dravo/Still also was capable of building a sulfuric acid plant. The desulfurization efficiency of the plant has consistently provided an average final gas sulfur loading below the guaranteed 45 gr/DSCF. This removal efficiency has enabled production of an average of 4615 tons per day of 66/sup 0/Be acid. Also SO/sub 2/ to SO/sub 3/ conversion has averaged 98%. 3 figures. (DP)

Knight, R.E.

1981-01-01T23:59:59.000Z

133

Extensive expansion at Karsto gas plant under way  

SciTech Connect

By 2000, the gas and condensate plant at Karsto, Norway, will have been expanded extensively: gas-processing capacity will increase to 2.2 bscfd from current 775 MMscfd; and production capacity for LPG, naphtha, and condensate will reach approximately 10 million metric tons/year (mty). Prompting this expansion is the landing of Karsto in 2000 of a 42-in., rich-gas pipeline from Haltenbanken, offshore mid-Norway, and installation of the 42-in. Europipe II dry-gas pipeline from Karsto to Germany. In the same period, several spin-off projects adding value to the overall concept may be constructed. These could include a 350-mw power plant and ethane-shipment facilities. Total investment at Karsto in the next 3--4 years will reach approximately $1.1 billion (US). Civil work began in June 1997; the detail engineering contract was awarded in August 1997. The paper describes the project.

Svenes, S. [Den Norske Stats Oljeselskap AS, Haugesund (Norway)

1998-07-27T23:59:59.000Z

134

Heat Exchanger Design for Solar Gas-Turbine Power Plant.  

E-Print Network (OSTI)

?? The aim of this project is to select appropriate heat exchangers out of available gas-gas heat exchangers for used in a proposed power plant.… (more)

Yakah, Noah

2012-01-01T23:59:59.000Z

135

Solvent Extraction for Remediation of Manufactured Gas Plant Sites  

Science Conference Proceedings (OSTI)

EPRI has assessed the feasibility of using a solvent extraction process to remove coal tar from the subsurface or to treat contaminated soil excavated from manufactured gas plant (MGP) sites. The assessment indicates that in situ solvent extraction may recover a significant amount of tar from the subsurface within a reasonable timeframe, provided subsurface conditions are conducive to process implementation. This work will help utilities searching for cost-effective technologies to remediate MGP sites.

1993-02-18T23:59:59.000Z

136

Alabama (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Alabama (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

137

Louisiana (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Louisiana (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

138

Indiana Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Indiana Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

139

California (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) California (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

140

Natural gas treatment process using PTMSP membrane  

DOE Patents (OSTI)

A process is described for separating C{sub 3}+ hydrocarbons, particularly propane and butane, from natural gas. The process uses a poly(trimethylsilylpropyne) membrane. 6 figs.

Toy, L.G.; Pinnau, I.

1996-03-26T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Natural gas treatment process using PTMSP membrane  

DOE Patents (OSTI)

A process for separating C.sub.3 + hydrocarbons, particularly propane and butane, from natural gas. The process uses a poly(trimethylsilylpropyne) membrane.

Toy, Lora G. (San Francisco, CA); Pinnau, Ingo (Palo Alto, CA)

1996-01-01T23:59:59.000Z

142

Thief Process Removal of Mercury from Flue Gas  

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

Process for the Removal of Mercury from Flue Gas Process for the Removal of Mercury from Flue Gas Opportunity The Department of Energy's National Energy Technology Laboratory (NETL) is seeking licensing partners interested in implementing United States Patent Number 6,521,021 entitled "Thief Process for the Removal of Mercury from Flue Gas." Disclosed in this patent is a novel process in which partially combusted coal is removed from the combustion chamber of a power plant using a lance (called a "thief"). This partially combusted coal acts as a thermally activated adsorbent for mercury. When it is in- jected into the duct work of the power plant downstream from the exit port of the combustion chamber, mercury within the flue gas contacts and adsorbs onto the thermally activated sorbent. The sorbent-mercury

143

Louisiana - North Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Louisiana - North Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

144

Texas - RRC District 10 Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 10 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

145

Texas - RRC District 6 Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 6 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

146

New Mexico - East Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) New Mexico - East Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

147

New Mexico - West Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) New Mexico - West Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

148

Texas - RRC District 2 Onshore Natural Gas Plant Liquids, Proved...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 2 Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

149

Texas - RRC District 8 Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 8 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

150

Texas - RRC District 9 Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 9 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

151

Louisiana State Offshore Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Louisiana State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

152

Texas State Offshore Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

153

Texas - RRC District 1 Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 1 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

154

Texas - RRC District 5 Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 5 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

155

Water Extraction from Coal-Fired Power Plant Flue Gas  

Science Conference Proceedings (OSTI)

The overall objective of this program was to develop a liquid disiccant-based flue gas dehydration process technology to reduce water consumption in coal-fired power plants. The specific objective of the program was to generate sufficient subscale test data and conceptual commercial power plant evaluations to assess process feasibility and merits for commercialization. Currently, coal-fired power plants require access to water sources outside the power plant for several aspects of their operation in addition to steam cycle condensation and process cooling needs. At the present time, there is no practiced method of extracting the usually abundant water found in the power plant stack gas. This project demonstrated the feasibility and merits of a liquid desiccant-based process that can efficiently and economically remove water vapor from the flue gas of fossil fuel-fired power plants to be recycled for in-plant use or exported for clean water conservation. After an extensive literature review, a survey of the available physical and chemical property information on desiccants in conjunction with a weighting scheme developed for this application, three desiccants were selected and tested in a bench-scale system at the Energy and Environmental Research Center (EERC). System performance at the bench scale aided in determining which desiccant was best suited for further evaluation. The results of the bench-scale tests along with further review of the available property data for each of the desiccants resulted in the selection of calcium chloride as the desiccant for testing at the pilot-scale level. Two weeks of testing utilizing natural gas in Test Series I and coal in Test Series II for production of flue gas was conducted with the liquid desiccant dehumidification system (LDDS) designed and built for this study. In general, it was found that the LDDS operated well and could be placed in an automode in which the process would operate with no operator intervention or adjustment. Water produced from this process should require little processing for use, depending on the end application. Test Series II water quality was not as good as that obtained in Test Series I; however, this was believed to be due to a system upset that contaminated the product water system during Test Series II. The amount of water that can be recovered from flue gas with the LDDS is a function of several variables, including desiccant temperature, L/G in the absorber, flash drum pressure, liquid-gas contact method, and desiccant concentration. Corrosion will be an issue with the use of calcium chloride as expected but can be largely mitigated through proper material selection. Integration of the LDDS with either low-grade waste heat and or ground-source heating and cooling can affect the parasitic power draw the LDDS will have on a power plant. Depending on the amount of water to be removed from the flue gas, the system can be designed with no parasitic power draw on the power plant other than pumping loads. This can be accomplished in one scenario by taking advantage of the heat of absorption and the heat of vaporization to provide the necessary temperature changes in the desiccant with the flue gas and precipitates that may form and how to handle them. These questions must be addressed in subsequent testing before scale-up of the process can be confidently completed.

Bruce C. Folkedahl; Greg F. Weber; Michael E. Collings

2006-06-30T23:59:59.000Z

156

Signature Metabolites at Manufactured Gas Plant Sites  

Science Conference Proceedings (OSTI)

This report presents results of research to demonstrate the biodegradation component of natural attenuation at former manufactured gas plant (MGP) sites. Researchers developed a target compound list of signature metabolites, biochemical intermediates of mono- and polycyclic aromatic hydrocarbon (MAH and PAH) biodegradation. They identified and tested appropriate methods of chemical analysis for these metabolites in MGP groundwater and sediments. Emphasis was placed on identifying natural microbiological ...

2008-10-14T23:59:59.000Z

157

Analysis of Natural Gas Fuel Cell Plant Configurations  

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

Analysis of Natur Analysis of Natur al Gas Fuel Cell Plant Configur ations March 24, 2011 DOE/NETL-2011/1486 Analysis of Natur al Gas Fuel Cell Plant Configur ations Disclaimer This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference therein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement,

158

Demonstration plant engineering and design. Phase I. The pipeline gas demonstration plant. Volume 9. Plant Section 800: product gas compression and drying  

SciTech Connect

Contract No. EF-77-C-01-2542 between Conoco Inc. and the US Department of Energy provides for the design, construction, and operation of a demonstration plant capable of processing bituminous caking coals into clean pipeline quality gas. The project is currently in the design phase scheduled to be completed in June 1981. One of the major efforts of Phase I is the completion of the process design and the project engineering design of the Demonstration Plant. This design effort has been completed. A report of the design effort is being issued in 24 volumes. This is Volume 9 which reports the design of Plant Section 800 - Product Gas Compression and Drying. Plant Section 800 compresses, cools, and drys the SNG product to conditions and specifications required for pipeline use. A conventional triethylene glycol (TEG) gas drying unit is employed to reduce the moisture content of the SNG to less than 7 pounds per million standard cubic feet. The product SNG has a minimum pressure of 800 psig and a maximum temperature of 100/sup 0/F. This section also includes the product gas analysis, metering, and totalizing instruments. It is designed to remove 3144 pounds of water from 19 million SCFC of SNG product. Volume 9 contains the following design information: process operation; design basis; heat and material balance; stream compositions; utility, chemical and catalyst summary; major equipment and machinery list; major equipment and machinery requisitions; instrument list; instrument requisitions; line lists; process flow diagram; engineering flow diagrams; and section plot plan.

Not Available

1981-01-01T23:59:59.000Z

159

Gas purification facilities at Purex: Process study  

SciTech Connect

This report provides a summary of the results of a process study, requested by the Atomic Energy Commission an the recovery of krypton and xenon from irradiated uranium at the Hanford Purex Plant. This request was prompted by original Commission forecasts of the expanded requirements for Krypton-85 for commercial phosphorescent signal lights and markers and for xenon isotopes of low neutron cross-section for use in liquid xenon scintillation counters, in connection with D.M.A., government and university-sponsored work. It was requested that both Hanford and Savannah River submit order of magnitude cost estimates for recovery facilities at the respective sites for three separate design cases. The cost information developed, along with market survey information obtained-through the A. D. Little Company and Department of Defense market surveys, would serve as the basis for scheduling of the Hanford and Savannah River participation in the Commission`s overall fission rare gas recovery program.

Michels, L.R.; Gerhart, J.M.

1958-12-31T23:59:59.000Z

160

Process for purifying natural gas  

SciTech Connect

This patent describes a process for separating water and carbon dioxide from a feedstream comprising hydrocarbons, water and carbon dioxide. It includes passing the feedstream to a first adsorption zone containing a solid adsorbent having selectivity for water at a first zone adsorption temperature effective to adsorb water and a first zone adsorption pressure and withdrawing a first zone adsorption effluent stream having a reduced concentration of water relative to the feedstream; passing at least a portion of the first zone adsorption effluent stream to a second adsorption zone containing a solid adsorbent having selectivity for carbon dioxide at a second zone adsorption temperature effective to adsorb carbon dioxide and a second zone adsorption pressure, the second zone adsorption temperature being lower than the first zone adsorption temperature, and withdrawing a second zone adsorption effluent stream having a reduced concentration of carbon dioxide relative to the first effluent stream; passing a first purge gas through the first adsorption zone at a first zone regeneration temperature.

Markovs, J.; James, F.E.

1992-02-18T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Gas Turbines Increase the Energy Efficiency of Industrial Processes  

E-Print Network (OSTI)

It is a well known fact that the gas turbine in a combined cycle has a higher inherent Carnot efficiency than the steam cycle which has been more generally accepted by industry. Unlike steam turbines, gas turbines do not require large boiler feed water, condensate and cooling water facilities. The benefits of the high efficiency of combined cycle gas turbines can only be realized if the energy in the hot exhaust can be utilized. Data for several plants, in various stages of engineering, in which clean fuel gas for the gas turbine is produced by gasification of coal, are presented. Waste heat from the gasifier and the gas turbine exhaust is converted to high pressure steam for steam turbines. Gas turbines may find application in other industrial processes, namely in the production of ammonia, LNG, and olefins. These options are briefly discussed.

Banchik, I. N.; Bohannan, W. R.; Stork, K.; McGovern, L. J.

1981-01-01T23:59:59.000Z

162

Efficient gas stream cooling in Second-Generation PFBC plants  

SciTech Connect

The coal-fueled Advanced or Second-Generation Pressurized Fluidized Bed Combustor concept (APFBC) is an efficient combined cycle in which coal is carbonized (partially gasified) to fuel a gas turbine, gas turbine exhaust heats feedwater for the steam cycle, and carbonizer char is used to generate steam for a steam turbine while heating combustion air for the gas turbine. The system can be described as an energy cascade in which chemical energy in solid coal is converted to gaseous form and flows to the gas turbine followed by the steam turbine, where it is converted to electrical power. Likewise, chemical energy in the char flows to both turbines generating electrical power in parallel. The fuel gas and vitiated air (PFBC exhaust) streams must be cleaned of entrained particulates by high-temperature equipment representing significant extensions of current technology. The energy recovery in the APFBC cycle allows these streams to be cooled to lower temperatures without significantly reducing the efficiency of the plant. Cooling these streams would allow the use of lower-temperature gas cleanup equipment that more closely approaches commercially available equipment, reducing cost and technological risk, and providing an earlier path to commercialization. This paper describes the performance effects of cooling the two hottest APFBC process gas streams: carbonizer fuel gas and vitiated air. Each cooling variation is described in terms of energy utilization, cycle efficiency, and cost implications.

White, J.S.; Horazak, D.A. [Foster Wheeler Development Corp., Livingston, NJ (United States); Robertson, A. [Foster Wheeler Development Corp., Livingston, NJ (United States)

1994-07-01T23:59:59.000Z

163

Advanced Materials and Processes for Gas Turbines  

Science Conference Proceedings (OSTI)

Jul 1, 2003 ... Out of Print. Description These proceedings from the United Engineering Foundation's Advanced Materials and Processes for Gas Turbines ...

164

Demonstration plant engineering and design. Phase I: the pipeline gas demonstration plant. Volume 7. Plant Section 500 - shift/methanation  

Science Conference Proceedings (OSTI)

Contract No. EF-77-C-01-2542 between Conoco Inc. and the US Department of Energy provides for the design, construction, and operation of a demonstration plant capable of processing bituminous caking coals into clean pipeline quality gas. The project is currently in the design phase (Phase I). This phase is scheduled to be completed in June 1981. One of the major efforts of Phase I is the completion of the process design and the project engineering design of the Demonstration Plant. A report of the design effort is being issued in 24 volumes. This is Volume 7 which reports the design of Plant Section 500 - Shift/Methanation. The shift/methanation process is used to convert the purified synthesis gas from the Rectisol unit (Plant Section 400) into the desired high-Btu SNG product. This is accomplished in a series of fixed-bed adiabatic reactors. Water is added to the feed gas to the reactors to effect the requisite reactions. A nickel catalyst is used in the shift/methanation process, and the only reaction products are methane and carbon dioxide. The carbon dioxide is removed from the SNG in Plant Sectin 600 - CO/sub 2/ Removal. After carbon dioxide removal from the SNG, the SNG is returned to Plant Section 500 for final methanation. The product from the final methanation reactor is an SNG stream having a gross heating value of approximately 960 Btu per standard cubic foot. The shift/methanation unit at design conditions produces 19 Million SCFD of SNG from 60 Million SCFD of purified synthesis gas.

Not Available

1981-01-01T23:59:59.000Z

165

WATER REQUIREMENTS FOR A RADIOCHEMICAL PROCESSING PLANT  

SciTech Connect

A survey of the water requirements is presented for a hypothetical plant to process all the fuel from a 15,000Mwe nuclear economy. For each processing plant, specific requirements must be based on a detailed water survey which includes water quality, process requirements, and in-plant conservation plans. These considerations are discussed and the quantitative requirements are listed. (J.R.D.)

Harrington, F.E.

1962-05-28T23:59:59.000Z

166

Gas consumption shrinks in commercial laundry plant  

SciTech Connect

The submerged-exhaust water-heating system with heat-recovery economizer operates above 90% efficiency compared to the 60% efficiency of the plant's old system. The system will require 3,936 therms/week compared to 5,887 with the old generator. Bubbles from the submerged downcomer tube rise through the surrounding bath, transferring heat through the gas-liquid interface as they rise to the surface. Heat transfer to the liquid bath is immediate and efficiency is high.

1981-09-01T23:59:59.000Z

167

Pennsylvania Natural Gas Plant Liquids Production, Gaseous Equivalent  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Liquids Production, Gaseous Equivalent (Million Cubic Feet) Pennsylvania Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 121 116 93 1970's 79 55 70 71 75 68 61 45 64 49 1980's 41 29 40 55 61 145 234 318 272 254 1990's 300 395 604 513 513 582 603 734 732 879 2000's 586 691 566 647 634 700 794 859 1,008 1,295 2010's 4,578 8,931 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: NGPL Production, Gaseous Equivalent Pennsylvania Natural Gas Plant Processing

168

Multivariable model predictive control for a gas turbine power plant  

Science Conference Proceedings (OSTI)

In this brief, constrained multi variable model predictive control (MPC) strategy is investigated for a GE9001E gas turbine power plant. So the rotor speed and exhaust gas temperature are controlled manipulating the fuel command and compressor inlet ... Keywords: ARX, gas turbine, identification, modeling, multivariable control, power plant, predictive control

Hadi Ghorbani; Ali Ghaffari; Mehdi Rahnama

2008-05-01T23:59:59.000Z

169

Simulation and integration of liquefied natural gas (lng) processes  

E-Print Network (OSTI)

The global use of natural gas is growing quickly. This is primarily attributed to its favorable characteristics and to the environmental advantages it enjoys over other fossil fuels such as oil and coal. One of the key challenges in supplying natural gas is the form (phase) at which it should be delivered. Natural gas may be supplied to the consumers as a compressed gas through pipelines. Another common form is to be compressed, refrigerated and supplied as a liquid known as liquefied natural gas (LNG). When there is a considerable distance involved in transporting natural gas, LNG is becoming the preferred method of supply because of technical, economic, and political reasons. Thus, LNG is expected to play a major role in meeting the global energy demands. This work addresses the simulation and optimization of an LNG plant. First, the process flowsheet is constructed based on a common process configuration. Then, the key units are simulated using ASPEN Plus to determine the characteristics of the various pieces of equipment and streams in the plant. Next, process integration techniques are used to optimize the process. Particular emphasis is given to energy objectives through three activities. First, the synthesis and retrofitting of a heat-exchange network are considered to reduce heating and cooling utilities. Second, the turbo-expander system is analyzed to reduce the refrigeration consumption in the process. Third, the process cogeneration is introduced to optimize the combined heat and power of the plant. These activities are carried out using a combination of graphical, computeraided, and mathematical programming techniques. A case study on typical LNG facilities is solved to examine the benefits of simulation and integration of the process. The technical, economic, and environmental impact of the process modifications are also discussed.

Al-Sobhi, Saad Ali

2007-12-01T23:59:59.000Z

170

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

171

Process for treatment of residual gas  

SciTech Connect

A process is disclosed for the treatment of the residual gases which are produced when hydrogen sulfide is reduced, by combustion, to elementary sulfur by the Claus process. The residual gases are fed through a heated conduit and gas scrubber, wherein the temperature of those residual gases are maintained above the melting point of sulfur. A portion of the raw coke oven gas condensate is admitted to the gas scrubber to be returned to the coke oven battery main from the flushing liquid separator as flushing liquor. The residual gases are then conducted through the coke oven gas purification process equipment along with the raw coke oven gas where the residual gases are intermixed with the raw coke oven gas prior to tar separation.

Nolden, K.

1980-01-01T23:59:59.000Z

172

Exhaust gas clean up process  

DOE Patents (OSTI)

A method of cleaning an exhaust gas containing particulates, SO/sub 2/ and NO/sub x/ is described. The method involves prescrubbing with water to remove HCl and most of the particulates, scrubbing with an aqueous absorbent containing a metal chelate and dissolved sulfite salt to remove NO/sub x/ and SO/sub 2/, and regenerating the absorbent solution by controlled heating, electrodialysis and carbonate salt addition. The NO/sub x/ is removed as N/sub 2/ gas or nitrogen sulfonate ions and the oxides of sulfur are removed as a valuable sulfate salt. 4 figs.

Walker, R.J.

1988-06-16T23:59:59.000Z

173

Plutonium Processing Plant Deactivated | National Nuclear Security  

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

Processing Plant Deactivated | National Nuclear Security Processing Plant Deactivated | National Nuclear Security Administration Our Mission Managing the Stockpile Preventing Proliferation Powering the Nuclear Navy Emergency Response Recapitalizing Our Infrastructure Continuing Management Reform Countering Nuclear Terrorism About Us Our Programs Our History Who We Are Our Leadership Our Locations Budget Our Operations Media Room Congressional Testimony Fact Sheets Newsletters Press Releases Speeches Events Social Media Video Gallery Photo Gallery NNSA Archive Federal Employment Apply for Our Jobs Our Jobs Working at NNSA Blog Home > About Us > Our History > NNSA Timeline > Plutonium Processing Plant Deactivated Plutonium Processing Plant Deactivated June 20, 1997 Hanford, WA Plutonium Processing Plant Deactivated The Plutonium Uranium Extraction Facility (PUREX), the largest of the

174

Plutonium Processing Plant Deactivated | National Nuclear Security  

National Nuclear Security Administration (NNSA)

Processing Plant Deactivated | National Nuclear Security Processing Plant Deactivated | National Nuclear Security Administration Our Mission Managing the Stockpile Preventing Proliferation Powering the Nuclear Navy Emergency Response Recapitalizing Our Infrastructure Continuing Management Reform Countering Nuclear Terrorism About Us Our Programs Our History Who We Are Our Leadership Our Locations Budget Our Operations Media Room Congressional Testimony Fact Sheets Newsletters Press Releases Speeches Events Social Media Video Gallery Photo Gallery NNSA Archive Federal Employment Apply for Our Jobs Our Jobs Working at NNSA Blog Home > About Us > Our History > NNSA Timeline > Plutonium Processing Plant Deactivated Plutonium Processing Plant Deactivated June 20, 1997 Hanford, WA Plutonium Processing Plant Deactivated The Plutonium Uranium Extraction Facility (PUREX), the largest of the

175

California Natural Gas Lease and Plant Fuel Consumption (Million...  

Annual Energy Outlook 2012 (EIA)

and Plant Fuel Consumption (Million Cubic Feet) California Natural Gas Lease and Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

176

Ohio Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

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

Plant Fuel Consumption (Million Cubic Feet) Ohio Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

177

Alaska (with Total Offshore) Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Alaska (with Total Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

178

Louisiana--North Natural Gas Plant Liquids, Proved Reserves ...  

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

Plant Liquids, Proved Reserves (Million Barrels) Louisiana--North Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

179

Louisiana--South Onshore Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Louisiana--South Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

180

Lower 48 Federal Offshore Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Lower 48 Federal Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

Note: This page contains sample records for the topic "gas processing plants" 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

Federal Offshore--California Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Federal Offshore--California Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

182

New Mexico--West Natural Gas Plant Liquids, Proved Reserves ...  

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

Plant Liquids, Proved Reserves (Million Barrels) New Mexico--West Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

183

Federal Offshore--Texas Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Federal Offshore--Texas Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

184

New Mexico--East Natural Gas Plant Liquids, Proved Reserves ...  

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

Plant Liquids, Proved Reserves (Million Barrels) New Mexico--East Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

185

Lower 48 States Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Plant Liquids, Proved Reserves (Million Barrels) Lower 48 States Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

186

Texas (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

187

Miscellaneous States Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Miscellaneous States Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

188

Texas--State Offshore Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

189

Louisiana--State Offshore Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Louisiana--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

190

California--State Offshore Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) California--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

191

Idaho Natural Gas Lease and Plant Fuel Consumption (Million Cubic...  

Gasoline and Diesel Fuel Update (EIA)

Lease and Plant Fuel Consumption (Million Cubic Feet) Idaho Natural Gas Lease and Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

192

,"Utah and Wyoming Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Utah and Wyoming Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",20...

193

,"Utah Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Utah Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011 ,"Release...

194

,"Lower 48 Federal Offshore Natural Gas Plant Liquids, Proved...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Lower 48 Federal Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

195

Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1...

196

,"Louisiana--State Offshore Natural Gas Plant Liquids, Proved...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Louisiana--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

197

,"Alabama (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Alabama (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

198

Louisiana--State Offshore Natural Gas Plant Liquids, Reserves...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Louisiana--State Offshore Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

199

,"Mississippi (with State Offshore) Natural Gas Plant Liquids...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Mississippi (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

200

,"Louisiana (with State Offshore) Natural Gas Plant Liquids,...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Louisiana (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

Note: This page contains sample records for the topic "gas processing plants" 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

,"Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids, Proved Reserves (Million...

202

,"Alaska (with Total Offshore) Natural Gas Plant Liquids, Proved...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Alaska (with Total Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

203

,"Federal Offshore--California Natural Gas Plant Liquids, Proved...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Federal Offshore--California Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

204

Federal Offshore--California Natural Gas Plant Liquids, Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Federal Offshore--California Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

205

California (with State Offshore) Natural Gas Plant Liquids, Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) California (with State Offshore) Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2...

206

,"California--San Joaquin Basin Onshore Natural Gas Plant Liquids...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California--San Joaquin Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

207

,"California--State Offshore Natural Gas Plant Liquids, Proved...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million...

208

,"California--Coastal Region Onshore Natural Gas Plant Liquids...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California--Coastal Region Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

209

,"California--Los Angeles Basin Onshore Natural Gas Plant Liquids...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California--Los Angeles Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

210

,"California (with State Offshore) Natural Gas Plant Liquids...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","California (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million...

211

/Gas Plant Operators Monthly Petroleum Product Sales Report. As  

U.S. Energy Information Administration (EIA)

sales to refiners and gas plant operators represented on the list. When using this list, ... (CNG Transmission) Dominion Transmission . DCP Midstream Partners.

212

EIA-782A EXCLUSIONARY LIST INSTRUCTIONS /Gas Plant Operators ...  

U.S. Energy Information Administration (EIA)

sales to refiners and gas plant operators represented on the list. When using this list, ... CNG Transmission (Dominion Field Serv.) Coastal Markets Limited .

213

,"North Dakota Natural Gas Plant Liquids Production, Gaseous...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","North Dakota Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

214

,"Tennessee Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Tennessee Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet)",1,"Annual",2012...

215

Illinois Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Illinois Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

216

Table 18. Natural gas plant liquids proved reserves and production...  

Gasoline and Diesel Fuel Update (EIA)

: Natural gas plant liquids proved reserves and production, 2009 - 2011 (excludes Lease Condensate) million barrels Reserves Production State and Subdivision 2009 2010 2011 2009...

217

Miscellaneous States Natural Gas Plant Liquids, Reserves Based...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Miscellaneous States Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

218

Kentucky Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

219

,"U.S. Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Natural Gas Plant Liquids Production, Gaseous Equivalent (Bcf)",1,"Monthly","92013" ,"Release...

220

Michigan Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

Note: This page contains sample records for the topic "gas processing plants" 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

Oklahoma Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Oklahoma Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

222

Montana Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

Annual Energy Outlook 2012 (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

223

Tennessee Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Tennessee Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

224

Florida Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Florida Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

225

Ohio Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Ohio Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

226

Colorado Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

227

Wyoming Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Wyoming Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

228

Mississippi (with State Offshore) Natural Gas Plant Liquids,...  

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

Liquids, Proved Reserves (Million Barrels) Mississippi (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

229

Montana Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Montana Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

230

Nebraska Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Annual Energy Outlook 2012 (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Nebraska Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

231

Kansas Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

Gasoline and Diesel Fuel Update (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

232

Oklahoma Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

233

,"New Mexico Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","New Mexico Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

234

Utah Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Utah Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

235

Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids...  

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

Proved Reserves (Million Barrels) Federal Offshore--Louisiana and Alabama Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

236

Alaska Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Alaska Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

237

,"Arkansas Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Arkansas Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

238

West Virginia Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Liquids Production, Gaseous Equivalent (Million Cubic Feet) West Virginia Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2...

239

,"Colorado Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Colorado Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

240

Kansas Natural Gas Plant Liquids Production, Gaseous Equivalent...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Production, Gaseous Equivalent (Million Cubic Feet) Kansas Natural Gas Plant Liquids Production, Gaseous Equivalent (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

Note: This page contains sample records for the topic "gas processing plants" 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

,"Kentucky Natural Gas Plant Liquids Production, Gaseous Equivalent...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Kentucky Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

242

,"West Virginia Natural Gas Plant Liquids Production, Gaseous...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","West Virginia Natural Gas Plant Liquids Production, Gaseous Equivalent (MMcf)",1,"Annual",2012 ,"Release...

243

,"Michigan Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Michigan Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

244

,"U.S. Natural Gas Plant Fuel Consumption (MMcf)"  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Natural Gas Plant Fuel Consumption (MMcf)",1,"Annual",2011 ,"Release Date:","10312013"...

245

Optical Gas Sensors for Advanced Coal-Fired Power Plants  

Science Conference Proceedings (OSTI)

Presentation Title, Optical Gas Sensors for Advanced Coal-Fired Power Plants. Author(s), Paul Ohodnicki, Congjun Wang, Douglas Kauffman, Kristi Kauffman, ...

246

,"Colorado Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Colorado Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

247

,"New Mexico Natural Gas Plant Fuel Consumption (MMcf)"  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","New Mexico Natural Gas Plant Fuel Consumption (MMcf)",1,"Annual",2011 ,"Release Date:","1031...

248

,"New Mexico Natural Gas Lease and Plant Fuel Consumption (MMcf...  

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

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","New Mexico Natural Gas Lease and Plant Fuel Consumption (MMcf)",1,"Annual",1998 ,"Release...

249

Texas (with State Offshore) Natural Gas Plant Liquids, Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Texas (with State Offshore) Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

250

,"Texas (with State Offshore) Natural Gas Plant Liquids, Proved...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas (with State Offshore) Natural Gas Plant Liquids, Proved Reserves (Million...

251

,"Federal Offshore--Texas Natural Gas Plant Liquids, Proved Reserves...  

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

Of Series","Frequency","Latest Data for" ,"Data 1","Federal Offshore--Texas Natural Gas Plant Liquids, Proved Reserves (Million Barrels)",1,"Annual",2011...

252

,"Texas--State Offshore Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--State Offshore Natural Gas Plant Liquids, Proved Reserves (Million...

253

More Economical Sulfur Removal for Fuel Processing Plants  

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

enabled TDA to develop and commercialize its direct oxidation process-a simple, catalyst-based system for removing sulfur from natural gas and petroleum-that was convenient and economical enough for smaller fuel processing plants to use. TDA Research, Inc. (TDA) of Wheat Ridge, CO, formed in 1987, is a privately-held R&D company that brings products to market either by forming internal business

254

Desulphurization of coke oven gas by the Stretford Process  

SciTech Connect

The Stretford process is probably the most effective means available for removing hydrogen sulphide from gas streams. For streams which do not contain hydrogen cyanide or excessive oxygen it should be nearly ideal. However, the large volume of waste liquor generated by fixation of hydrogen cyanide has prevented its widespread adoption for coke oven gas treatment. Investigations of various proposals for treating the waste liquor indicate that the only practicable way of dealing with it is by reductive incineration. Although attempts to apply the Peabody-Holmes reductive incineration process have been disappointing, significant progress in overcoming some of its deficiencies has been made. The Zimpro wet oxidation process will provide a convenient method of treating the HCN scrubber effluent at No. 1 Plant. However, it will not treat the sodium based liquor from the Stretford plant. Its application to Stretford waste treatment is limited to situations where ammonium liquors and ammonium sulphate recovery facilities are available. Commissioning of this plant has been delayed while a defect in the air compressor supplied for the plant is being remedied. When the problem of liquid effluent disposal has been overcome, and if reagent chemicals continue to be available at reasonable prices, the Stretford process will be a good choice for coke oven gas desulphurization. 8 figures.

Plenderleith, J.

1981-01-01T23:59:59.000Z

255

Issues evaluation process at Rocky Flats Plant  

SciTech Connect

This report describes the issues evaluation process for Rocky Flats Plant as established in July 1990. The issues evaluation process was initiated February 27, 1990 with a Charter and Process Overview for short-term implementation. The purpose of the process was to determine the projects required for completion before the Phased Resumption of Plutonium Operations. To determine which projects were required, the issues evaluation process and emphasized risk mitigation, based on a ranking system. The purpose of this report is to document the early design of the issues evaluation process to record the methodologies used that continue as the basis for the ongoing Issues Management Program at Rocky Flats Plant.

Smith, L.C.

1992-04-16T23:59:59.000Z

256

Topsoe`s Wet gas Sulfuric Acid (WSA) process: An alternative technology for recovering refinery sulfur  

SciTech Connect

The Topsoe Wet gas Sulfuric Acid (WSA) process is a catalytic process which produces concentrated sulfuric acid from refinery streams containing sulfur compounds such as H{sub 2}S (Claus plant feed), Claus plant tail gas, SO{sub 2} (FCC off-gas, power plants), and spent sulfuric acid (alkylation acid). The WSA process recovers up to 99.97% of the sulfur value in the stream as concentrated sulfuric acid (93--98.5 wt%). No solid waste products or waste water is produced and no chemicals are consumed in the process. The simple process layout provides low capital cost and attractive operating economy. Twenty four commercial WSA plants have been licensed. The WSA process is explained in detail and comparisons with alternative sulfur management technology are presented. Environmental regulations applying to SO{sub x} abatement and sulfuric acid production plants are explained in the context of WSA plant operation.

Ward, J.W. [Haldor Topsoe, Inc., Houston, TX (United States)

1995-09-01T23:59:59.000Z

257

Cogeneration Economics for Process Plants  

E-Print Network (OSTI)

This paper presents the incentives for cogeneration, describing pertinent legislation and qualification requirements for cogeneration benefits, and indicates the performance and economic characteristics of combined cycle cogeneration applications. The Fuel Use Act (FUA) restricts the use of un-renewable or premium fuels (e.g., natural gas and oil) for high-load-factor or base-load power generation. The Public Utility Regulatory Policy Act (PURPA) encourages high-efficiency cogeneration by providing exemptions to the restrictions and requiring that utilities purchase cogenerated power at rates corresponding to the costs they "avoid" by not generating this power.

Ahner, D. J.

1985-05-01T23:59:59.000Z

258

Methanation process utilizing split cold gas recycle  

DOE Patents (OSTI)

In the methanation of feed gas comprising carbon monoxide and hydrogen in multiple stages, the feed gas, cold recycle gas and hot product gas is mixed in such proportions that the mixture is at a temperature sufficiently high to avoid carbonyl formation and to initiate the reaction and, so that upon complete reaction of the carbon monoxide and hydrogen, an excessive adiabatic temperature will not be reached. Catalyst damage by high or low temperatures is thereby avoided with a process that utilizes extraordinarily low recycle ratios and a minimum of investment in operating costs.

Tajbl, Daniel G. (Evanston, IL); Lee, Bernard S. (Lincolnwood, IL); Schora, Jr., Frank C. (Palatine, IL); Lam, Henry W. (Rye, NY)

1976-07-06T23:59:59.000Z

259

Plant Networks for Processing Recyclable Materials  

Science Conference Proceedings (OSTI)

We use a modified optimal market area model to examine how links between material recycling and other aspects of operations strategy can shape plant networks for the processing of recyclable materials. We characterize the complementarity of the recyclate ... Keywords: localization, material versatility, minimills, operations strategy, optimal market area, plant networks, recycling

Lieven Demeester, Mei Qi, Luk N. Van Wassenhove

2013-10-01T23:59:59.000Z

260

New generation enrichment monitoring technology for gas centrifuge enrichment plants  

SciTech Connect

The continuous enrichment monitor, developed and fielded in the 1990s by the International Atomic Energy Agency, provided a go-no-go capability to distinguish between UF{sub 6} containing low enriched (approximately 4% {sup 235}U) and highly enriched (above 20% {sup 235}U) uranium. This instrument used the 22-keV line from a {sup 109}Cd source as a transmission source to achieve a high sensitivity to the UF{sub 6} gas absorption. The 1.27-yr half-life required that the source be periodically replaced and the instrument recalibrated. The instrument's functionality and accuracy were limited by the fact that measured gas density and gas pressure were treated as confidential facility information. The modern safeguarding of a gas centrifuge enrichment plant producing low-enriched UF{sub 6} product aims toward a more quantitative flow and enrichment monitoring concept that sets new standards for accuracy stability, and confidence. An instrument must be accurate enough to detect the diversion of a significant quantity of material, have virtually zero false alarms, and protect the operator's proprietary process information. We discuss a new concept for advanced gas enrichment assay measurement technology. This design concept eliminates the need for the periodic replacement of a radioactive source as well as the need for maintenance by experts. Some initial experimental results will be presented.

Ianakiev, Kiril D [Los Alamos National Laboratory; Alexandrov, Boian, S. [Los Alamos National Laboratory; Boyer, Brian, D. [Los Alamos National Laboratory; Hill, Thomas, R. [Los Alamos National Laboratory; Macarthur, Duncan, W. [Los Alamos National Laboratory; Marks, Thomas [Los Alamos National Laboratory; Moss, Calvin, E. [Los Alamos National Laboratory; Sheppard, Gregory, A. [Los Alamos National Laboratory; Swinhoe, Martyn, T. [Los Alamos National Laboratory

2008-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Tankathon-A Process Plant Simulation  

E-Print Network (OSTI)

Tankathon is a simulation of a process plant in a computer generated environment. Interaction and control in three dimensional control systems are studied. The simulated "process" consists of seven tanks containing a "liquid" flowing from tanks to tanks. The goal of the "plant manager", the user, is to keep the tanks from draining or overflowing. The user can interact with valves in the pipes connecting the tanks in order to regulate the liquid flow and check the flow rate.

Kai-Mikael Jää-Aro

1992-01-01T23:59:59.000Z

262

Gas permeation carbon capture --- Process modeling and optimization  

SciTech Connect

A multi-staged gas permeation carbon capture process model was developed in Aspen Custom Modeler{reg_sign} (ACM) and optimized in the context of the retrofit of a 550 MW subcritical pulverized coal (PC) power plant. The gas permeation stages in the process are described by a custom multi-component, hollowfiber membrane model. Gas transport across the asymmetric membrane was modeled according to the solution-diffusion model for the selective skin layer and the assumption of negligible flux resistance by the porous support. Counter-current, one-dimensional plug flow was assumed with permeate pressure drop in the fiber lumen side due to capillary constrained flow. A modular optimization framework was used to minimize the levelized cost of electricity (LCOE) by optimizing a set of key process variables. The framework allows the external control of multiple simulation modules from different software packages from a common interface.

Morinelly, Juan; Miller, David

2011-01-01T23:59:59.000Z

263

UPGRADING NATURAL GAS VIA MEMBRANE SEPARATION PROCESSES  

SciTech Connect

The objective of the present study is to assess the potential usefulness of membrane separation processes for removing CO{sub 2} and H{sub 2}S from low-quality natural gas containing substantial amounts of both these ''acid'' gases, e.g., up to 40 mole-% CO{sub 2} and 10 mole-% H{sub 2}S. The membrane processes must be capable of upgrading the crude natural gas to pipeline specifications ({le} 2 mole-% CO{sub 2}, {le} 4 ppm H{sub 2}S). Moreover, these processes must also be economically competitive with the conventional separation techniques, such as gas absorption, utilized for this purpose by the gas industry.

S.A.Stern; P.A. Rice; J. Hao

2000-03-01T23:59:59.000Z

264

How Gas Turbine Power Plants Work | Department of Energy  

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

How Gas Turbine Power Plants Work How Gas Turbine Power Plants Work How Gas Turbine Power Plants Work The combustion (gas) turbines being installed in many of today's natural-gas-fueled power plants are complex machines, but they basically involve three main sections: The compressor, which draws air into the engine, pressurizes it, and feeds it to the combustion chamber at speeds of hundreds of miles per hour. The combustion system, typically made up of a ring of fuel injectors that inject a steady stream of fuel into combustion chambers where it mixes with the air. The mixture is burned at temperatures of more than 2000 degrees F. The combustion produces a high temperature, high pressure gas stream that enters and expands through the turbine section. The turbine is an intricate array of alternate stationary and

265

Assessment of Natural Gas Combined Cycle (NGCC) Plants with  

E-Print Network (OSTI)

Assessment of Natural Gas Combined Cycle (NGCC) Plants with CO2 Capture and Storage Mike Gravely.5 Million Annual Budget FY 10/11 · $62.5 million electric · $24 million natural gas · Program Research Areas:45 Bevilacqua-Knight, Inc's Role and Reference Documents Rich Myhre ­ Bevilacqua-Knight, Inc 3:05 Pacific Gas

266

U.S. Gas Plant Production of Natural Gas Liquids and Liquid ...  

U.S. Energy Information Administration (EIA)

U.S. Gas Plant Production of Natural Gas Liquids and Liquid Refinery Gases (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 ...

267

U.S. Gas Plant Production of Natural Gas Liquids and Liquid ...  

U.S. Energy Information Administration (EIA)

U.S. Gas Plant Production of Natural Gas Liquids and Liquid Refinery Gases (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; ...

268

Juice Processing Plant EPI | ENERGY STAR Buildings & Plants  

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

Juice Processing Plant EPI Juice Processing Plant EPI Secondary menu About us Press room Contact Us Portfolio Manager Login Facility owners and managers Existing buildings Commercial new construction Industrial energy management Small business Service providers Service and product providers Verify applications for ENERGY STAR certification Design commercial buildings Energy efficiency program administrators Commercial and industrial program sponsors Associations State and local governments Federal agencies Tools and resources Training In This Section Campaigns Commercial building design Communications resources Energy management guidance Financial resources Portfolio Manager Products and purchasing Recognition Research and reports Service and product provider (SPP) resources Success stories Target Finder

269

Field Test of Manufactured Gas Plant Remediation Technologies: Material Removal and Handling  

Science Conference Proceedings (OSTI)

Common manufactured gas plant (MGP) site structures are often sources of contamination and present a number of unique material removal and handling challenges. This report provides results from a field-scale study involving the excavation of the contents of a subgrade gas holder tank. Specifically discussed are the material handling activities needed to prepare MGP impacted soils and debris for remediation processes.

1996-02-02T23:59:59.000Z

270

Coal gasification power plant and process  

DOE Patents (OSTI)

In an integrated coal gasification power plant, a humidifier is provided for transferring as vapor, from the aqueous blowdown liquid into relatively dry air, both (I) at least a portion of the water contained in the aqueous liquid and (II) at least a portion of the volatile hydrocarbons therein. The resulting humidified air is advantageously employed as at least a portion of the hot air and water vapor included in the blast gas supplied via a boost compressor to the gasifier.

Woodmansee, Donald E. (Schenectady, NY)

1979-01-01T23:59:59.000Z

271

Gas turbine power plant with supersonic gas compressor - Energy ...  

A gas turbine engine. The engine is based on the use of a gas turbine driven rotor having a compression ramp traveling at a local supersonic inlet velocity (based on ...

272

Transport Membrane Condenser for Water and Energy Recovery from Power Plant Flue Gas  

Science Conference Proceedings (OSTI)

The new waste heat and water recovery technology based on a nanoporous ceramic membrane vapor separation mechanism has been developed for power plant flue gas application. The recovered water vapor and its latent heat from the flue gas can increase the power plant boiler efficiency and reduce water consumption. This report describes the development of the Transport Membrane Condenser (TMC) technology in details for power plant flue gas application. The two-stage TMC design can achieve maximum heat and water recovery based on practical power plant flue gas and cooling water stream conditions. And the report includes: Two-stage TMC water and heat recovery system design based on potential host power plant coal fired flue gas conditions; Membrane performance optimization process based on the flue gas conditions, heat sink conditions, and water and heat transport rate requirement; Pilot-Scale Unit design, fabrication and performance validation test results. Laboratory test results showed the TMC system can exact significant amount of vapor and heat from the flue gases. The recovered water has been tested and proved of good quality, and the impact of SO{sub 2} in the flue gas on the membrane has been evaluated. The TMC pilot-scale system has been field tested with a slip stream of flue gas in a power plant to prove its long term real world operation performance. A TMC scale-up design approach has been investigated and an economic analysis of applying the technology has been performed.

Dexin Wang

2012-03-31T23:59:59.000Z

273

EIA - Natural Gas Pipeline Network - Expansion Process Flow Diagram  

Annual Energy Outlook 2012 (EIA)

Natural Gas based on data through 20072008 with selected updates Development and Expansion Process For Natural Gas Pipeline Projects Figure showing the expansion process...

274

Olinda Landfill Gas Recovery Plant Biomass Facility | Open Energy  

Open Energy Info (EERE)

Olinda Landfill Gas Recovery Plant Biomass Facility Olinda Landfill Gas Recovery Plant Biomass Facility Jump to: navigation, search Name Olinda Landfill Gas Recovery Plant Biomass Facility Facility Olinda Landfill Gas Recovery Plant Sector Biomass Facility Type Landfill Gas Location Orange County, California Coordinates 33.7174708°, -117.8311428° Loading map... {"minzoom":false,"mappingservice":"googlemaps3","type":"ROADMAP","zoom":14,"types":["ROADMAP","SATELLITE","HYBRID","TERRAIN"],"geoservice":"google","maxzoom":false,"width":"600px","height":"350px","centre":false,"title":"","label":"","icon":"","visitedicon":"","lines":[],"polygons":[],"circles":[],"rectangles":[],"copycoords":false,"static":false,"wmsoverlay":"","layers":[],"controls":["pan","zoom","type","scale","streetview"],"zoomstyle":"DEFAULT","typestyle":"DEFAULT","autoinfowindows":false,"kml":[],"gkml":[],"fusiontables":[],"resizable":false,"tilt":0,"kmlrezoom":false,"poi":true,"imageoverlays":[],"markercluster":false,"searchmarkers":"","locations":[{"text":"","title":"","link":null,"lat":33.7174708,"lon":-117.8311428,"alt":0,"address":"","icon":"","group":"","inlineLabel":"","visitedicon":""}]}

275

California - San Joaquin Basin Onshore Natural Gas Plant Liquids, Proved  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Gas Plant Liquids, Proved Reserves (Million Barrels) California - San Joaquin Basin Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1970's 77 1980's 81 57 124 117 105 120 109 107 101 95 1990's 86 75 83 85 75 80 80 82 58 60 2000's 64 52 68 78 95 112 100 103 97 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 8/1/2013 Next Release Date: 8/1/2014 Referring Pages: Natural Gas Liquids Proved Reserves as of Dec. 31 CA, San Joaquin Basin Onshore Natural Gas Liquids Proved Reserves Natural Gas Liquids Proved Reserves as of Dec.

276

Investigations of biological processes in Austrian MBT plants  

SciTech Connect

Mechanical biological treatment (MBT) of municipal solid waste (MSW) has become an important technology in waste management during the last decade. The paper compiles investigations of mechanical biological processes in Austrian MBT plants. Samples from all plants representing different stages of degradation were included in this study. The range of the relevant parameters characterizing the materials and their behavior, e.g. total organic carbon, total nitrogen, respiration activity and gas generation sum, was determined. The evolution of total carbon and nitrogen containing compounds was compared and related to process operation. The respiration activity decreases in most of the plants by about 90% of the initial values whereas the ammonium release is still ongoing at the end of the biological treatment. If the biogenic waste fraction is not separated, it favors humification in MBT materials that is not observed to such extent in MSW. The amount of organic carbon is about 15% dry matter at the end of the biological treatment.

Tintner, J. [Institute of Waste Management, Department of Water, Atmosphere and Environment, University of Natural Resources and Applied Life Sciences, Muthgasse 107, 1190 Vienna (Austria); Smidt, E., E-mail: ena.smidt@boku.ac.a [Institute of Waste Management, Department of Water, Atmosphere and Environment, University of Natural Resources and Applied Life Sciences, Muthgasse 107, 1190 Vienna (Austria); Boehm, K.; Binner, E. [Institute of Waste Management, Department of Water, Atmosphere and Environment, University of Natural Resources and Applied Life Sciences, Muthgasse 107, 1190 Vienna (Austria)

2010-10-15T23:59:59.000Z

277

Gas Fired Power Plants: Investment Timing, Operating Flexibility and Abandonment  

E-Print Network (OSTI)

Many firms are considering investment in gas fired power plants. We consider a firm holding a license, i.e. an option, to build a gas fired power plant. The operating cash flows from the plant depend on the spark spread, defined as the difference between the unit price of electricity and cost of gas. The plant produces electricity when the spark spread exceeds emission costs, otherwise the plant is ramped down and held idle. The owner has also an option to abandon the plant and realize the salvage value of the equipment. We compute optimal entry and exit threshold values for the spark spread. Also the effects of emission costs on the value of installing CO2 capture technology are analyzed.

Stein-erik Fleten; Erkka Näsäkkälä

2003-01-01T23:59:59.000Z

278

U.S. Normal Butane-Butylene Stocks at Natural Gas Processing ...  

U.S. Energy Information Administration (EIA)

U.S. Normal Butane-Butylene Stocks at Natural Gas Processing Plants (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: ...

279

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

Science Conference Proceedings (OSTI)

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

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

2007-04-01T23:59:59.000Z

280

The Thief Process for Mercury Removal from Flue Gas  

E-Print Network (OSTI)

The Thief Process is a cost-effective variation to activated carbon injection (ACI) for removal of mercury from flue gas. In this scheme, partially combusted coal from the furnace of a pulverized coal power generation plant is extracted by a lance and then re-injected into the ductwork downstream of the air preheater. Recent results on a 500-lb/hr pilot-scale combustion facility show similar removals of mercury for both the Thief Process and ACI. The tests conducted to date at laboratory, bench, and pilot-scales demonstrate that the Thief sorbents exhibit capacities for mercury from flue gas streams that are comparable to those exhibited by commercially available activated carbons. Independent verification of the sorbent activity at a pilot-plant that uses a slipstream from a Wisconsin utility has been accomplished. A patent for the process was issued in February 2003 [1]. The Thief sorbents are cheaper than commerciallyavailable activated carbons; exhibit excellent capacities for mercury; and the overall process holds great potential for reducing the cost of mercury removal from flue gas [1-4].

Evan J. Granite; Mark C. Freeman; Richard A. Hargis; William J. O’dowd; Henry W. Pennline

2004-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants |  

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

DOE, RTI to Design and Build Gas Cleanup System for IGCC Power DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants July 13, 2009 - 1:00pm Addthis Washington, DC - The U.S. Department of Energy (DOE) announces a collaborative project with Research Triangle Institute (RTI) International to design, build, and test a warm gas cleanup system to remove multiple contaminants from coal-derived syngas. The 50-MWe system will include technologies to remove trace elements such as mercury and arsenic, capture the greenhouse gas carbon dioxide (CO2), and extract more than 99.9 percent of the sulfur from the syngas. A novel process to convert the extracted sulfur to a pure elemental sulfur product will also be tested. This project supports DOE's vision of coal power plants with near-zero

282

DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants |  

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

DOE, RTI to Design and Build Gas Cleanup System for IGCC Power DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants DOE, RTI to Design and Build Gas Cleanup System for IGCC Power Plants July 13, 2009 - 1:00pm Addthis Washington, DC - The U.S. Department of Energy (DOE) announces a collaborative project with Research Triangle Institute (RTI) International to design, build, and test a warm gas cleanup system to remove multiple contaminants from coal-derived syngas. The 50-MWe system will include technologies to remove trace elements such as mercury and arsenic, capture the greenhouse gas carbon dioxide (CO2), and extract more than 99.9 percent of the sulfur from the syngas. A novel process to convert the extracted sulfur to a pure elemental sulfur product will also be tested. This project supports DOE's vision of coal power plants with near-zero

283

Plant Process Computer Replacement to Support Distributed Process Control: Joint STPNOC-EPRI Distributed Plant Process Computer Syst em Project  

Science Conference Proceedings (OSTI)

Concerns exist that nuclear power plant process computer systems are becoming obsolete and do not have the infrastructure to support new processes such as digital process control upgrades. To address these concerns, a distributed plant process computer system was designed and implemented at the South Texas Project Nuclear Operating Company Units 1 and 2. Implementing this new system and its associated plant networks, if done correctly, will facilitate future control and information system upgrades that c...

2001-11-16T23:59:59.000Z

284

Utah Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Fuel Consumption (Million Cubic Feet) Utah Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

285

Utah and Wyoming Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Utah and Wyoming Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

286

Federal Offshore--Texas Natural Gas Plant Liquids, Reserves Based...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Federal Offshore--Texas Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

287

California Natural Gas Plant Fuel Consumption (Million Cubic...  

Annual Energy Outlook 2012 (EIA)

Fuel Consumption (Million Cubic Feet) California Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

288

U.S. Natural Gas Plant Liquids Reserves, Estimated Production...  

Gasoline and Diesel Fuel Update (EIA)

Liquids Reserves, Estimated Production (Million Barrels) U.S. Natural Gas Plant Liquids Reserves, Estimated Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

289

Florida Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

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

Liquids, Proved Reserves (Million Barrels) Florida Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

290

U.S. Natural Gas Plant Liquids, Reserves Revision Decreases ...  

Gasoline and Diesel Fuel Update (EIA)

Decreases (Million Barrels) U.S. Natural Gas Plant Liquids, Reserves Revision Decreases (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

291

Mississippi Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

Liquids, Proved Reserves (Million Barrels) Mississippi Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

292

California Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

Liquids, Proved Reserves (Million Barrels) California Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

293

New Mexico Natural Gas Plant Liquids, Reserves Based Production...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) New Mexico Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

294

Louisiana--North Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Louisiana--North Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

295

U.S. Natural Gas Plant Liquids, Reserves Acquisitions (Million...  

Gasoline and Diesel Fuel Update (EIA)

Acquisitions (Million Barrels) U.S. Natural Gas Plant Liquids, Reserves Acquisitions (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

296

U.S. Natural Gas Plant Liquids, Reserves Adjustments (Million...  

Annual Energy Outlook 2012 (EIA)

Adjustments (Million Barrels) U.S. Natural Gas Plant Liquids, Reserves Adjustments (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

297

North Dakota Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Liquids, Proved Reserves (Million Barrels) North Dakota Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

298

U.S. Natural Gas Plant Liquids, Reserves Extensions (Million...  

Annual Energy Outlook 2012 (EIA)

Extensions (Million Barrels) U.S. Natural Gas Plant Liquids, Reserves Extensions (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

299

Wyoming Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

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

Liquids, Proved Reserves (Million Barrels) Wyoming Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

300

Wyoming Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Wyoming Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

Note: This page contains sample records for the topic "gas processing plants" 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

Colorado Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Colorado Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

302

Alaska Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

Annual Energy Outlook 2012 (EIA)

Liquids, Proved Reserves (Million Barrels) Alaska Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

303

Utah Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

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

Liquids, Proved Reserves (Million Barrels) Utah Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

304

Louisiana Natural Gas Plant Liquids, Proved Reserves (Million...  

Gasoline and Diesel Fuel Update (EIA)

Liquids, Proved Reserves (Million Barrels) Louisiana Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

305

Kentucky Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Kentucky Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

306

Texas Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

Annual Energy Outlook 2012 (EIA)

Liquids, Proved Reserves (Million Barrels) Texas Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

307

Kansas Natural Gas Plant Liquids, Reserves Based Production ...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Kansas Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

308

New Mexico Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Liquids, Proved Reserves (Million Barrels) New Mexico Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

309

Alabama Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

Gasoline and Diesel Fuel Update (EIA)

Liquids, Proved Reserves (Million Barrels) Alabama Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

310

Arkansas Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Liquids, Proved Reserves (Million Barrels) Arkansas Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

311

Utah Natural Gas Plant Liquids, Reserves Based Production (Million...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Utah Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

312

Florida Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Florida Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

313

West Virginia Natural Gas Plant Liquids, Proved Reserves (Million...  

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

Liquids, Proved Reserves (Million Barrels) West Virginia Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7...

314

U.S. Natural Gas Plant Liquids, Reserves Revision Increases ...  

Annual Energy Outlook 2012 (EIA)

Increases (Million Barrels) U.S. Natural Gas Plant Liquids, Reserves Revision Increases (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

315

Montana Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) Montana Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

316

North Dakota Natural Gas Plant Liquids, Reserves Based Production...  

Annual Energy Outlook 2012 (EIA)

Reserves Based Production (Million Barrels) North Dakota Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

317

Oklahoma Natural Gas Plant Liquids, Reserves Based Production...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Oklahoma Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

318

Michigan Natural Gas Plant Liquids, Reserves Based Production...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Michigan Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

319

Arkansas Natural Gas Plant Liquids, Reserves Based Production...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Arkansas Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

320

Michigan Natural Gas Plant Fuel Consumption (Million Cubic Feet...  

Annual Energy Outlook 2012 (EIA)

Fuel Consumption (Million Cubic Feet) Michigan Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

Note: This page contains sample records for the topic "gas processing plants" 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

Oklahoma Natural Gas Plant Liquids, Proved Reserves (Million Barrels)  

U.S. Energy Information Administration (EIA)

Oklahoma Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1970's: 583:

322

East Coast (PADD 1) Gas Plant Production of Normal Butane ...  

U.S. Energy Information Administration (EIA)

East Coast (PADD 1) Gas Plant Production of Normal Butane-Butylene (Thousand Barrels per Day) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; ...

323

Colorado Natural Gas Plant Fuel Consumption (Million Cubic Feet...  

Gasoline and Diesel Fuel Update (EIA)

Fuel Consumption (Million Cubic Feet) Colorado Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

324

New Mexico Natural Gas Plant Fuel Consumption (Million Cubic...  

Annual Energy Outlook 2012 (EIA)

Fuel Consumption (Million Cubic Feet) New Mexico Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8...

325

Texas Natural Gas Plant Fuel Consumption (Million Cubic Feet...  

Gasoline and Diesel Fuel Update (EIA)

Fuel Consumption (Million Cubic Feet) Texas Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

326

Texas--State Offshore Natural Gas Plant Liquids, Reserves Based...  

Gasoline and Diesel Fuel Update (EIA)

Reserves Based Production (Million Barrels) Texas--State Offshore Natural Gas Plant Liquids, Reserves Based Production (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

327

Proceedings: Decommissioning - Plant Reconfiguration and Engineering Processes Workshop  

Science Conference Proceedings (OSTI)

EPRI's Plant Reconfiguration and Engineering Processes Workshop -- the seventh in a series -- will help utility personnel evaluate technologies for decommissioning nuclear power plants. This workshop focused on specific aspects of plant reconfiguration and engineering processes as they relate to nuclear plant decommissioning. The information presented will help utilities assess approaches to restructuring of plant engineering processes and reconfiguration management to meet individual decommissioning pro...

2001-01-09T23:59:59.000Z

328

Combined gas turbine and steam turbine power plant  

SciTech Connect

A description is given of a power plant arrangement having a gas turbine, a heat recovery steam generator, a steam turbine and means for controlling steam flow from the heat recovery steam generator to the steam turbine. Steam conditions are maintained generally constant and variations in power plant loading are carried by the steam turbine while operating the gas turbine at a generally constant fuel flow.

Baker, J.M.; Clark, G.W.; Harper, D.M.; Tomlinson, L.O.

1978-04-04T23:59:59.000Z

329

Gas Turbine Plant Modeling for Dynamic Simulation.  

E-Print Network (OSTI)

?? Gas turbines have become effective in industrial applications for electric and thermal energy production partly due to their quick response to load variations. A… (more)

Endale Turie, Samson

2012-01-01T23:59:59.000Z

330

Plant Fuel Consumption of Natural Gas (Summary)  

U.S. Energy Information Administration (EIA)

... electric power price data are for regulated electric ... Gas volumes delivered for vehicle fuel are included in the State monthly totals from January 2011 ...

331

1 2Using Auxiliary Gas Power for CCS Energy Needs in Retrofitted Coal Power Plants  

E-Print Network (OSTI)

Post-combustion capture retrofits are expected to a near-term option for mitigating CO2 emissions from existing coal-fired power plants. Much of the literature proposes using power from the existing coal plant and thermal integration of its supercritical steam cycle with the stripper reboiler to supply the energy needed for solvent regeneration and CO2 compression. This study finds that using an auxiliary natural gas turbine plant to meet the energetic demands of carbon capture and compression may make retrofits more attractive compared to using thermal integration in some circumstances. Natural gas auxiliary plants increase the power output of the base plant and reduce technological risk associated with CCS, but require favorable natural gas prices and regional electricity demand for excess electricity to make using an auxiliary plant more desirable. Three different auxiliary plant technologies were compared to integration for 90 % capture from an existing, 500 MW supercritical coal plant. CO2 capture and compression is simulated using Aspen Plus and a monoethylamine (MEA) absorption process. Thermoflow software is used to simulate three gas plant technologies. The three technologies assessed are the

Sarah Bashadi; Howard Herzog; Dava J. Newman; Sarah Bashadi

2010-01-01T23:59:59.000Z

332

An Evaluation of Gas Turbines for APFBC Power Plants  

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

EVALUATION OF GAS TURBINES FOR APFBC POWER PLANTS EVALUATION OF GAS TURBINES FOR APFBC POWER PLANTS Donald L. Bonk U.S. DOE National Energy Technology Laboratory Morgantown, West Virginia eMail: dbonk@netl.doe.gov phone: (304) 285-4889 Richard E. Weinstein, P.E. Parsons Infrastructure & Technology Group Inc. Reading, Pennsylvania eMail: richard.e.weinstein@parsons.com phone: (610) 855-2699 Abstract This paper describes a concept screening evaluation of gas turbines from several manufacturers that assessed the merits of their respective gas turbines for advanced circulating pressurized fluidized bed combustion combined cycle (APFBC) applications. The following gas turbines were evaluated for the modifications expected for APFBC service: 2 x Rolls-Royce Industrial Trent aeroderivative gas turbine configurations; a 3 x Pratt & Whitney Turbo Power FT8 Twin-

333

,"U.S. Natural Gas Plant Processing"  

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

,"Release Date:","12122013" ,"Next Release Date:","172014" ,"Excel File Name:","ngprodppdcunusm.xls" ,"Available from Web Page:","http:www.eia.govdnavng...

334

,"U.S. Natural Gas Plant Processing"  

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

,"Release Date:","12122013" ,"Next Release Date:","172014" ,"Excel File Name:","ngprodppdcunusa.xls" ,"Available from Web Page:","http:www.eia.govdnavng...

335

U.S. Natural Gas Plant Processing  

Gasoline and Diesel Fuel Update (EIA)

Period: Monthly Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area Feb-13 Mar-13...

336

U.S. Natural Gas Processing Plant  

Gasoline and Diesel Fuel Update (EIA)

Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History All Oils (Excluding Crude Oil) 5,419 6,722 6,801 5,826 6,210 6,249 1993-2013 Pentanes Plus 787 1,076 1,000 757 707 644...

337

U.S. Natural Gas Processing Plant  

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

647 837 1993-2012 PropanePropylene 864 1,575 1,329 1,371 1,505 1,944 1993-2012 Normal ButaneButylene 646 1,373 907 1,292 688 907 1993-2012 IsobutaneButylene 499 453 567 500 500...

338

New Mexico Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

339

North Dakota Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Annual Download Series...

340

U.S. Natural Gas Plant Processing  

Annual Energy Outlook 2012 (EIA)

Michigan Mississippi Montana Nebraska New Mexico North Dakota Ohio Oklahoma Pennsylvania South Dakota Tennessee Texas Utah West Virginia Wyoming Period: Monthly Annual Download...

Note: This page contains sample records for the topic "gas processing plants" 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

An expert system prototype for designing natural gas cogeneration plants  

Science Conference Proceedings (OSTI)

Cogeneration plants are units that simultaneously produce electricity and useful heat from the same fuel. In such plants different components (prime movers, pumps, steam generators, etc.) are combined in order to meet electricity and useful heat loads ... Keywords: Cogeneration, Engineering design, Expert systems, Natural gas

José Alexandre Matelli; Edson Bazzo; Jonny Carlos da Silva

2009-05-01T23:59:59.000Z

342

Simulated coal gas MCFC power plant system verification  

DOE Green Energy (OSTI)

The following tasks are included in this project: Commercialization; Power plant development; Manufacturing facilities development; Test facility development; Stack research; and Advanced research and technology development. This report briefly describes the subtasks still to be completed: Power plant system test with reformed natural gas; Upgrading of existing, US government-owned, test facilities; and Advanced MCFC component research.

NONE

1998-02-01T23:59:59.000Z

343

Federal Offshore--Gulf of Mexico Natural Gas Extraction Loss...  

Annual Energy Outlook 2012 (EIA)

Pages: Extraction Loss of Natural Gas at Processing Plants (Summary) Federal Offshore Gulf of Mexico Natural Gas Plant Processing Extraction Loss of Natural Gas at...

344

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

345

Idaho Chemical Processing Plant product denitrator upgrade  

SciTech Connect

The uranium product denitrator at the Idaho Chemical Processing Plant has had serious operating problems since 1970, including inadequate contamintion control, fluidized bed caking, frequent bed heater failure, product overflow plugging, and poor feed control. These problems were minimized through selective redesign and upgrade of the process equipment as part of a process upgrade program completed in March 1981. Following startup and testing of the rebuilt product denitrator, 1044 kg of enriched uranium was processed in three weeks while demonstrating greater reliability, ease of operation, and improved contamination control. To maximize personnel safety in the future, the denitrator vessel should be made critically safe by geometry and process instrumentation isolated from the process for semi-remote operation.

Rindfleisch, J.A.; Durst, P.C.; Dahl, C.A.; Casterline, C.E.; Petig, A.V.

1982-05-01T23:59:59.000Z

346

Lease and Plant Fuel Consumption of Natural Gas (Summary)  

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

Repressuring Nonhydrocarbon Gases Removed Vented and Flared Marketed Production Natural Gas Processed Extraction Loss Dry Production Imports By Pipeline LNG Imports Exports...

347

North Dakota Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) North Dakota Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 42,828 41,318 37,818 1970's 36,830 33,252 32,131 0 0 0 0 0 0 1980's 50,900 57,608 71,745 77,524 81,008 72,678 86,329 67,867 59,841 1990's 62,042 59,228 50,462 51,713 55,150 49,861 47,942 51,657 52,777 52,191 2000's 54,738 58,536 59,894 58,479 60,261 63,240 65,575 69,653 76,762 87,977 2010's 91,539 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Processed North Dakota Natural Gas Plant Processing

348

Pinellas Plant facts. [Products, processes, laboratory facilities  

SciTech Connect

This plant was built in 1956 in response to a need for the manufacture of neutron generators, a principal component in nuclear weapons. The neutron generators consist of a miniaturized linear ion accelerator assembled with the pulsed electrical power supplies required for its operation. The ion accelerator, or neutron tube, requires ultra clean, high vacuum technology: hermetic seals between glass, ceramic, glass-ceramic, and metal materials: plus high voltage generation and measurement technology. The existence of these capabilities at the Pinellas Plant has led directly to the assignment of the lightning arrester connector, specialty capacitor, vacuum switch, and crystal resonator. Active and reserve batteries and the radioisotopically-powered thermoelectric generator draw on the materials measurement and controls technologies which are required to ensure neutron generator life. A product development and production capability in alumina ceramics, cermet (electrical) feedthroughs, and glass ceramics has become a specialty of the plant; the laboratories monitor the materials and processes used by the plant's commercial suppliers of ferroelectric ceramics. In addition to the manufacturing facility, a production development capability is maintained at the Pinellas Plant.

1986-09-01T23:59:59.000Z

349

Louisiana Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Natural Gas Processed (Million Cubic Feet) Natural Gas Processed (Million Cubic Feet) Louisiana Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 3,383,334 3,728,717 4,465,379 1970's 5,237,519 5,994,431 6,337,328 6,524,729 6,273,136 5,831,487 5,749,783 5,709,535 5,561,040 1980's 5,197,429 4,770,095 4,190,105 4,439,430 3,811,852 3,794,464 3,880,364 3,918,236 4,002,843 1990's 4,220,068 4,340,531 4,466,425 4,315,312 4,200,126 4,604,292 4,652,677 4,767,965 4,610,969 4,687,261 2000's 4,316,127 4,206,470 3,771,001 3,391,870 3,244,850 2,527,636 2,511,802 2,857,443 2,208,920 2,175,026 2010's 2,207,760 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data.

350

Biennial Assessment of the Fifth Power Plan Gas Turbine Power Plant Planning Assumptions  

E-Print Network (OSTI)

Biennial Assessment of the Fifth Power Plan Gas Turbine Power Plant Planning Assumptions October 17, 2006 Simple- and combined-cycle gas turbine power plants fuelled by natural gas are among the bulk-emission and efficient gas turbine technology made combined-cycle gas turbine power plants the "resource of choice

351

Proceedings: Distributed Digital Systems, Plant Process  

Science Conference Proceedings (OSTI)

A workshop on Distributed Digital Systems, Plant Process Computers, and Networks was held in Charlotte, North Carolina on August 16-18, 1994. The purpose of the workshop was to provide a forum for technology transfer, technical information exchange, and education. The workshop was attended by more than 100 representatives of electric utilities, equipment manufacturers, engineering service organizations, and government agencies. The workshop consisted of three days of presentations, exhibitions, a panel d...

1995-03-31T23:59:59.000Z

352

Process for selected gas oxide removal by radiofrequency catalysts  

DOE Patents (OSTI)

This process to remove gas oxides from flue gas utilizes adsorption on a char bed subsequently followed by radiofrequency catalysis enhancing such removal through selected reactions. Common gas oxides include SO.sub.2 and NO.sub.x.

Cha, Chang Y. (3807 Reynolds St., Laramie, WY 82070)

1993-01-01T23:59:59.000Z

353

Profitability Comparison Between Gas Turbines and Gas Engine in Biomass-Based Power Plants Using Binary Particle Swarm Optimization  

Science Conference Proceedings (OSTI)

This paper employs a binary discrete version of the classical Particle Swarm Optimization to compare the maximum net present value achieved by a gas turbines biomass plant and a gas engine biomass plant. The proposed algorithm determines the optimal ...

P. Reche López; M. Gómez González; N. Ruiz Reyes; F. Jurado

2007-06-01T23:59:59.000Z

354

Gas Centrifuge Enrichment Plant Safeguards System Modeling  

SciTech Connect

The U.S. Department of Energy (DOE) is interested in developing tools and methods for potential U.S. use in designing and evaluating safeguards systems used in enrichment facilities. This research focuses on analyzing the effectiveness of the safeguards in protecting against the range of safeguards concerns for enrichment plants, including diversion of attractive material and unauthorized modes of use. We developed an Extend simulation model for a generic medium-sized centrifuge enrichment plant. We modeled the material flow in normal operation, plant operational upset modes, and selected diversion scenarios, for selected safeguards systems. Simulation modeling is used to analyze both authorized and unauthorized use of a plant and the flow of safeguards information. Simulation tracks the movement of materials and isotopes, identifies the signatures of unauthorized use, tracks the flow and compilation of safeguards data, and evaluates the effectiveness of the safeguards system in detecting misuse signatures. The simulation model developed could be of use to the International Atomic Energy Agency IAEA, enabling the IAEA to observe and draw conclusions that uranium enrichment facilities are being used only within authorized limits for peaceful uses of nuclear energy. It will evaluate improved approaches to nonproliferation concerns, facilitating deployment of enhanced and cost-effective safeguards systems for an important part of the nuclear power fuel cycle.

Elayat, H A; O'Connell, W J; Boyer, B D

2006-06-05T23:59:59.000Z

355

Idaho Chemical Processing Plant safety document ICPP hazardous chemical evaluation  

Science Conference Proceedings (OSTI)

This report presents the results of a hazardous chemical evaluation performed for the Idaho Chemical Processing Plant (ICPP). ICPP tracks chemicals on a computerized database, Haz Track, that contains roughly 2000 individual chemicals. The database contains information about each chemical, such as its form (solid, liquid, or gas); quantity, either in weight or volume; and its location. The Haz Track database was used as the primary starting point for the chemical evaluation presented in this report. The chemical data and results presented here are not intended to provide limits, but to provide a starting point for nonradiological hazards analysis.

Harwood, B.J.

1993-01-01T23:59:59.000Z

356

New Measures to Safeguard Gas Centrifuge Enrichment Plants  

SciTech Connect

As Gas Centrifuge Enrichment Plants (GCEPs) increase in separative work unit (SWU) capacity, the current International Atomic Energy Agency (IAEA) model safeguards approach needs to be strengthened. New measures to increase the effectiveness of the safeguards approach are being investigated that will be mutually beneficial to the facility operators and the IAEA. One of the key concepts being studied for application at future GCEPs is embracing joint use equipment for process monitoring of load cells at feed and withdrawal (F/W) stations. A mock F/W system was built at Oak Ridge National Laboratory (ORNL) to generate and collect F/W data from an analogous system. The ORNL system has been used to collect data representing several realistic normal process and off-normal (including diversion) scenarios. Emphasis is placed on the novelty of the analysis of data from the sensors as well as the ability to build information out of raw data, which facilitates a more effective and efficient verification process. This paper will provide a progress report on recent accomplishments and next steps.

Whitaker, Jr., James [ORNL; Garner, James R [ORNL; Whitaker, Michael [ORNL; Lockwood, Dunbar [U.S. Department of Energy, NNSA; Gilligan, Kimberly V [ORNL; Younkin, James R [ORNL; Hooper, David A [ORNL; Henkel, James J [ORNL; Krichinsky, Alan M [ORNL

2011-01-01T23:59:59.000Z

357

Evaluation of the NeuStream-S™ Flue Gas Desulfurization Process  

Science Conference Proceedings (OSTI)

Harris Group Inc. (HGI) of Denver, Colorado, was contracted by the Electric Power Research Institute (EPRI) to monitor, evaluate, and prepare this report on a dual-alkali flue gas desulfurization (FGD) process developed by Neumann Systems Group, Inc. (NSG). The process is being demonstrated in a nominal 20-MW demonstration plant, treating a slip stream of flue gas from the Colorado Springs Utilities 142-MW Drake Unit 7. HGI evaluated performance, operability, and readiness for scale-up of the process. Co...

2011-05-31T23:59:59.000Z

358

Development of advanced hot-gas desulfurization processes  

SciTech Connect

Advanced integrated gasification combined cycle (IGCC) power plants nearing completion, such as Sierra-Pacific, employ a circulating fluidized-bed (transport) reactor hot-gas desulfurization (HGD) process that uses 70-180 {micro}m average particle size (aps) zinc-based mixed-metal oxide sorbent for removing H{sub 2}S from coal gas down to less than 20 ppmv. The sorbent undergoes cycles of absorption (sulfidation) and air regeneration. The key barrier issues associated with a fluidized-bed HGD process are chemical degradation, physical attrition, high regeneration light-off (initiation) temperature, and high cost of the sorbent. Another inherent complication in all air-regeneration-based HGD processes is the disposal of the problematic dilute SO{sub 2} containing regeneration tail-gas. Direct Sulfur Recovery Process (DSRP), a leading first generation technology, efficiently reduces this SO{sub 2} to desirable elemental sulfur, but requires the use of 1-3 % of the coal gas, thus resulting in an energy penalty to the plant. Advanced second-generation processes are under development that can reduce this energy penalty by modifying the sorbent so that it could be directly regenerated to elemental sulfur. The objective of this research is to support the near and long term DOE efforts to commercialize the IGCC-HGD process technology. Specifically we aim to develop: optimized low-cost sorbent materials with 70-80 {micro}m average aps meeting all Sierra specs; attrition resistant sorbents with 170 {micro}m aps that allow greater flexibility in the choice of the type of fluidized-bed reactor e.g. they allow increased throughput in a bubbling-bed reactor; and modified fluidizable sorbent materials that can be regenerated to produce elemental sulfur directly with minimal or no use of coal gas. The effort during the reporting period has been devoted to testing the FHR-32 sorbent. FHR-32 sorbent was tested for 50 cycles of sulfidation in a laboratory scale reactor.

Jothimurugesan, K.

2000-04-17T23:59:59.000Z

359

Second-Generation Pressurized Fluidized Bed Combustion: Small gas turbine induustrial plant study  

SciTech Connect

Second-Generation Pressurized Fluidized Bed Combustion (PFBC) plants provide a coal-fired, high-efficiency, combined-cycle system for the generation of electricity and steam. The plants use lime-based sorbents in PFB combustors to meet environmental air standards without back-end gas desulfurization equipment. The second-generation system is an improvement over earlier PFBC concepts because it can achieve gas temperatures of 2100[degrees]F and higher for improved cycle efficiency while maintaining the fluidized beds at 1600[degrees]F for enhanced sulfur capture and minimum alkali release. Second-generation PFBC systems are capable of supplying the electric and steam process needs of industrial plants. The basic second-generation system can be applied in different ways to meet a variety of process steam and electrical requirements. To evaluate the potential of these systems in the industrial market, conceptual designs have been developed for six second-generation PFBC plants. These plants cover a range of electrical outputs from 6.3 to 41.5 MWe and steam flows from 46,067 to 442,337 lb/h. Capital and operating costs have been estimated for these six plants and for equivalent (in size) conventional, coal-fired atmospheric fluidized bed combustion cogeneration plants. Economic analyses were conducted to compare the cost of steam for both the second-generation plants and the conventional plants.

Shenker, J.; Garland, R.; Horazak, D.; Seifert, F.; Wenglarz, R.

1992-07-01T23:59:59.000Z

360

Second-Generation Pressurized Fluidized Bed Combustion: Small gas turbine industrial plant study  

SciTech Connect

Second-Generation Pressurized Fluidized Bed Combustion (PFBC) plants provide a coal-fired, high-efficiency, combined-cycle system for the generation of electricity and steam. The plants use lime-based sorbents in PFB combustors to meet environmental air standards without back-end gas desulfurization equipment. The second-generation system is an improvement over earlier PFBC concepts because it can achieve gas temperatures of 2100{degrees}F and higher for improved cycle efficiency while maintaining the fluidized beds at 1600{degrees}F for enhanced sulfur capture and minimum alkali release. Second-generation PFBC systems are capable of supplying the electric and steam process needs of industrial plants. The basic second-generation system can be applied in different ways to meet a variety of process steam and electrical requirements. To evaluate the potential of these systems in the industrial market, conceptual designs have been developed for six second-generation PFBC plants. These plants cover a range of electrical outputs from 6.3 to 41.5 MWe and steam flows from 46,067 to 442,337 lb/h. Capital and operating costs have been estimated for these six plants and for equivalent (in size) conventional, coal-fired atmospheric fluidized bed combustion cogeneration plants. Economic analyses were conducted to compare the cost of steam for both the second-generation plants and the conventional plants.

Shenker, J.; Garland, R.; Horazak, D.; Seifert, F.; Wenglarz, R.

1992-07-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Natural Gas Plant Field Production: Natural Gas Liquids  

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

Product: Natural Gas Liquids Pentanes Plus Liquefied Petroleum Gases Ethane Propane Normal Butane Isobutane Period-Unit: Monthly-Thousand Barrels Monthly-Thousand Barrels per Day Annual-Thousand Barrels Annual-Thousand Barrels per Day Product: Natural Gas Liquids Pentanes Plus Liquefied Petroleum Gases Ethane Propane Normal Butane Isobutane Period-Unit: Monthly-Thousand Barrels Monthly-Thousand Barrels per Day Annual-Thousand Barrels Annual-Thousand Barrels per Day Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Product Area Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History U.S. 74,056 76,732 74,938 79,040 82,376 81,196 1981-2013 PADD 1 1,525 1,439 2,394 2,918 2,821 2,687 1981-2013 East Coast 1993-2008 Appalachian No. 1 1,525 1,439 2,394 2,918 2,821 2,687 1993-2013 PADD 2 12,892 13,208 13,331 13,524 15,204 15,230 1981-2013 Ind., Ill. and Ky. 1,975 1,690 2,171 1,877 2,630 2,746 1993-2013

362

Natural Gas Plant Stocks of Natural Gas Liquids  

Gasoline and Diesel Fuel Update (EIA)

Product: Natural Gas Liquids Pentanes Plus Liquefied Petroleum Gases Ethane Propane Normal Butane Isobutane Period: Monthly Annual Product: Natural Gas Liquids Pentanes Plus Liquefied Petroleum Gases Ethane Propane Normal Butane Isobutane Period: Monthly Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Product Area Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History U.S. 5,419 6,722 6,801 5,826 6,210 6,249 1993-2013 PADD 1 122 121 115 189 246 248 1993-2013 East Coast 1993-2010 Appalachian No. 1 122 121 115 189 246 248 1993-2013 PADD 2 959 891 880 1,129 1,104 1,041 1993-2013 Ind., Ill. and Ky. 311 300 298 308 262 260 1993-2013 Minn., Wis., N. Dak., S. Dak. 56 64 58 60 51 64 1993-2013 Okla., Kans., Mo. 592 527 524 761 791 717 1993-2013 PADD 3 3,810 5,007 5,032 3,817 4,246 4,272 1993-2013

363

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During precommissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with their Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's Engineering group has found a new site for the project at a Duke Energy gas processing plant in Milfay, Oklahoma.

Dr. Andre Da Costa

2003-04-10T23:59:59.000Z

364

U.S., Canada continue dominance of world`s gas processing  

Science Conference Proceedings (OSTI)

Gas plants in the US and Canada continued to lead the rest of the world in processing capacity, throughput, and NGL production in 1996. The consolidation of gas-processing assets that has been rolling through US companies in recent years continued to limit growth in new capacity. Canadian liquids producers, on the other hand, will likely benefit from increased gas production and export sales to the US when a clutch of pipeline expansions in the next 18--30 months eases the capacity constraints on gas movements southward. And, markets and suppliers around the world continue to become more closely dependent on each other, stimulating new capacity and production. US capacity stood at slightly more than 678 bcfd as of January 1, 1997; throughput for 1996 averaged 48.8 bcfd; and NGL production exceeded 76,000 gpd. Canadian gas-processing capacity last year approached 40 bcfd. Gas-processing throughput there averaged more than 30.8 bcfd; NGL production fell to slightly more than 42,000 gpd. Oil and Gas Journal`s most recent exclusive, plant-by-plant, worldwide gas-processing survey and its international survey of petroleum-derived sulfur recovery reflect these trends. This report supplements operator-supplied capacity and production data for Alberta with figures from the (1) Alberta Energy and Utilities Board (AEUB), formerly the Energy Resources Conservation Board (ERBC), (2) British Columbia Ministry of Employment and Investment`s Engineering and Operations Branch, and (3) Saskatchewan Ministry of Energy and Mines.

True, W.R.

1997-06-02T23:59:59.000Z

365

Process for making substitute natural gas  

SciTech Connect

A process, having high thermal efficiency, is provided for the production of substitute natural gas from fossil fuels such as crude oil, by non-catalytic hydrogenation. High thermal efficiency is obtained by using cryogenic systems for separating hydrogen from (A) the product of the hydrogenation reaction and (B) from products produced by partial oxidation in the production of hydrogen required for the hydrogenation reactions. Other products from the partial oxidation reaction may be used either as fuel or as feedstocks for catalytic steam reforming to produce SNG.

Conway, H.L.; Hargis, J.A.; Stroud, H.J.

1980-06-24T23:59:59.000Z

366

Plant Process Computer Upgrade Guidelines, Volume 1: Replacement Guidelines  

Science Conference Proceedings (OSTI)

The gradual obsolescence of the original plant process computers at nuclear power plants decreases their effectiveness in supporting plant operation and maintenance. This project, based on the practical experience of utility personnel, presents guidelines on plant process computer replacement planning and implementation.

1993-01-01T23:59:59.000Z

367

A Wood-Fired Gas Turbine Plant  

E-Print Network (OSTI)

This paper covers the research and development of a wood-fired gas turbine unit that is used for generating electricity. The system uses one large cyclonic combustor and a cyclone cleaning system in series to provide hot gases to drive an Allison T-56 aircraft engine (the industrial version is the 501-k). A Westinghouse 3,000-kW generator is used on the prototype facility with a Philadelphia gear system reducing the 14,000-rpm turbine output speed to the 3,600-rpm generator operating speed. Fuel is fed into the combustor by a rotary valve system. The swirling effect of the cyclone combustor ensures that residence time is adequate to completely burn all solid particles in the combustor ahead of the cyclone filter. Burning of particles on the metal walls of the cyclone filter could cause overheating and deterioration of the walls. This wood-fired gas turbine unit could provide a low cost source of power for areas where conventional methods are now prohibitive and provide a means for recovering energy from a source that now poses disposal problems.

Powell, S. H.; Hamrick, J. T.

1986-06-01T23:59:59.000Z

368

Adaptation of a commercially available 200 kW natural gas fuel cell power plant for operation on a hydrogen rich gas stream  

DOE Green Energy (OSTI)

International Fuel Cells (IFC) has designed a hydrogen fueled fuel cell power plant based on a modification of its standard natural gas fueled PC25{trademark} C fuel cell power plant. The natural gas fueled PC25 C is a 200 kW, fuel cell power plant that is commercially available. The program to accomplish the fuel change involved deleting the natural gas processing elements, designing a new fuel pretreatment subsystem, modifying the water and thermal management subsystem, developing a hydrogen burner to combust unconsumed hydrogen, and modifying the control system. Additionally, the required modifications to the manufacturing and assembly procedures necessary to allow the hydrogen fueled power plant to be manufactured in conjunction with the on-going production of the standard PC25 C power plants were identified. This work establishes the design and manufacturing plan for the 200 kW hydrogen fueled PC25 power plant.

Maston, V.A.

1997-12-01T23:59:59.000Z

369

Natural gas conversion process. Sixth quarterly report  

Science Conference Proceedings (OSTI)

The experimental apparatus was dismantled and transferred to a laboratory space provided by Lawrence Berkeley Laboratory (LBL) which is already equipped with a high-ventilation fume hood. This will enable us to make tests at higher gas flow rates in a safe environment. Three papers presented at the ACS meeting in San Francisco (Symposium on Natural Gas Upgrading II) April 5--10, 1992 show that the goal of direct catalytic conversion of Methane into heavier Hydrocarbons in a reducing atmosphere is actively pursued in three other different laboratories. There are similarities in their general concept with our own approach, but the temperature range of the experiments reported in these recent papers is much lower and this leads to uneconomic conversion rates. This illustrates the advantages of Methane activation by a Hydrogen plasma to reach commercial conversion rates. A preliminary process flow diagram was established for the Integrated Process, which was outlined in the previous Quarterly Report. The flow diagram also includes all the required auxiliary facilities for product separation and recycle of the unconverted feed as well as for the preparation and compression of the Syngas by-product.

Not Available

1992-12-01T23:59:59.000Z

370

Controllability analysis and decentralized control of a wet limestone flue gas desulfurization plant  

Science Conference Proceedings (OSTI)

Presently, decentralized feedback control is the only control strategy used in wet limestone flue gas desulfurization (WLFGD) plants. Proper tuning of this control strategy is becoming an important issue in WLFGD plants because more stringent SO{sub 2} regulations have come into force recently. Controllability analysis is a highly valuable tool for proper design of control systems, but it has not been applied to WLFGD plants so far. In this paper a decentralized control strategy is designed and applied to a WLFGD pilot plant taking into account the conclusions of a controllability analysis. The results reveal that good SO{sub 2} control in WLFGD plants can be achieved mainly because the main disturbance of the process is well-aligned with the plant and interactions between control loops are beneficial to SO{sub 2} control.

Perales, A.L.V.; Ortiz, F.J.G.; Ollero, P.; Gil, F.M. [University of Seville, Seville (Spain)

2008-12-15T23:59:59.000Z

371

Pennsylvania Natural Gas Lease and Plant Fuel Consumption (Million Cubic  

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

and Plant Fuel Consumption (Million Cubic Feet) and Plant Fuel Consumption (Million Cubic Feet) Pennsylvania Natural Gas Lease and Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 2,270 1,530 1,924 1970's 2,251 2,419 2,847 2,725 1,649 1,760 3,043 3,210 2,134 2,889 1980's 1,320 1,580 3,278 3,543 5,236 4,575 4,715 5,799 4,983 4,767 1990's 6,031 3,502 3,381 4,145 3,252 3,069 3,299 2,275 1,706 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Lease and Plant Fuel Consumption Pennsylvania Natural Gas Consumption by End Use Lease and Plant

372

Mississippi Natural Gas Lease and Plant Fuel Consumption (Million Cubic  

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

and Plant Fuel Consumption (Million Cubic Feet) and Plant Fuel Consumption (Million Cubic Feet) Mississippi Natural Gas Lease and Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 8,582 9,158 8,521 1970's 7,893 5,840 9,153 6,152 5,357 7,894 4,836 4,979 5,421 8,645 1980's 4,428 4,028 7,236 6,632 7,202 6,296 6,562 8,091 7,100 5,021 1990's 7,257 4,585 4,945 4,829 3,632 3,507 3,584 3,652 3,710 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Lease and Plant Fuel Consumption Mississippi Natural Gas Consumption by End Use Lease and Plant

373

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1-MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technologies group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The system has been installed in the field and initial startup activities have been completed. The system has not yet produced the flow rate required for continuous stable operation. NTE, the company hosting this test site/pilot plant, will drill additional wells to increase the inlet flow rate. The system is expected to be in full continuous operation by May 2004.

Kaaeid Lokhandwala

2004-04-30T23:59:59.000Z

374

,"Natural Gas Plant Field Production: Natural Gas Liquids "  

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

Field Production: Natural Gas Liquids " Field Production: Natural Gas Liquids " ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Natural Gas Plant Field Production: Natural Gas Liquids ",16,"Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_gp_a_epl0_fpf_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_gp_a_epl0_fpf_mbbl_m.htm" ,"Source:","Energy Information Administration"

375

H[sub 2]S in EOR--1: Gas processing for CO[sub 2] EOR involves sulfur removal  

SciTech Connect

A design study for a new West Texas gas processing plant for a CO[sub 2] EOR project provides for installation of H[sub 2]S removal processes to be delayed for 3 years after completion of the plant. During this delay, a more precise produced gas composition will be obtained so that the process equipment for removing H[sub 2]S can be properly selected and sized to handle the gas stream that at the peak will reach about 30 MMscfd. The new plant's processing components include inlet separation, sulfur removal and recovery, compression, dehydration, and NGL recovery. The new plant will be capable of processing CO[sub 2]-contaminated associated gas, recovering valuable propane-plus NGLs,a nd producing a miscible CO[sub 2] for reinjection. The first in a series of two articles details the process and configuration options. The concluding part will discuss in greater detail the sulfur recovery alternatives.

Johnson, J.E. (Pritchard Corp., Overland Park, KS (United States)); Tzap, S.J.; Kelley, R.E. (Raytheon Engineers and Constructors, Denver, CO (United States)); Laczko, L.P. (OXY USA Inc., Midland, TX (United States))

1993-11-15T23:59:59.000Z

376

CO2 capture processes in power plants - Le captage du CO2 dans les centrales thermiques  

E-Print Network (OSTI)

This review is devoted to assess and compare various processes aiming at recover CO2 from power plants fed with natural gas (NGCC) and pulverized coal (PC). These processes are post combustion CO2 capture using chemical solvents, natural gas reforming for pre-combustion capture and oxy-fuel combustion with cryogenic recovery of CO2. These processes were evaluated to give some clues for choosing the best option for each type of power plant. The comparison of these various concepts suggests that, in the short and medium term, chemical absorption is the most interesting process for NGCC power plants. For CP power plants, oxy-combustion can be a very interesting option, as well as post-combustion capture by chemical solvents.

Chakib Bouallou

2010-08-12T23:59:59.000Z

377

CO2 capture processes in power plants - Le captage du CO2 dans les centrales thermiques  

E-Print Network (OSTI)

This review is devoted to assess and compare various processes aiming at recover CO2 from power plants fed with natural gas (NGCC) and pulverized coal (PC). These processes are post combustion CO2 capture using chemical solvents, natural gas reforming for pre-combustion capture and oxy-fuel combustion with cryogenic recovery of CO2. These processes were evaluated to give some clues for choosing the best option for each type of power plant. The comparison of these various concepts suggests that, in the short and medium term, chemical absorption is the most interesting process for NGCC power plants. For CP power plants, oxy-combustion can be a very interesting option, as well as post-combustion capture by chemical solvents.

Bouallou, Chakib

2010-01-01T23:59:59.000Z

378

TECHNICAL AND OPERATING SUPPORT FOR PILOT DEMONSTRATION OF MORPHYSORB ACID GAS REMOVAL PROCESS  

SciTech Connect

Over the past 14 years, the Gas Technology Institute and jointly with Uhde since 1997 developing Morphysorb{reg_sign} a new physical solvent-based acid gas removal process. Based on extensive laboratory, bench, pilot-plant scale experiments and computer simulations, DEGT Gas Transmission Company, Canada (DEGT) has chosen the process for use at its Kwoen processing facility near Chetwynd, British Columbia, Canada as the first commercial application for the Morphysorb process. DOE co-funded the development of the Morphysorb process in various stages of development. DOE funded the production of this report to ensure that the results of the work would be readily available to potential users of the process in the United States. The Kwoen Plant is designed to process 300 MMscfd of raw natural gas at 1,080-psia pressure. The sour natural gas contains 20 to 25 percent H{sub 2}S and CO{sub 2}. The plant reduces the acid gas content by about 50% and injects the removed H{sub 2}S and CO{sub 2} into an injection well. The Kwoen plant has been operating since August 2002. Morphysorb{reg_sign} is a physical solvent-based process used for the bulk removal of CO{sub 2} and/or H{sub 2}S from natural gas and other gaseous streams. The solvent consists of N-Formyl morpholine and other morpholine derivatives. This process is particularly effective for high-pressure and high acid-gas applications and offers substantial savings in investment and operating cost compared to competitive physical solvent-based processes. GTI and DEGT first entered into an agreement in 2002 to test the Morphysorb process at their Kwoen Gas Treating Plant in northern BC. The process is operating successfully without any solvent related problems and has between DEGTC and GTI. As of December 2003, about 90 Bcf of sour gas was processed. Of this about 8 Bcf of acid gas containing mainly H{sub 2}S and CO{sub 2} was injected back into the depleted reservoir and 82 Bcf sent for further processing at DEGTC's Pine River Plant. This report discusses the operational performance at Kwoen plant during the performance test as well as the solvent performance since the plant started up. The Morphysorb performance is assessed by Duke Energy according to five metrics: acid gas pickup, recycle gas flow, total hydrocarbon loss in acid gas stream, Morphysorb solvent losses and foaming related problems. Plant data over a period of one year show that the Morphysorb solvent has performed extremely well in four out of five of these categories. The fifth metric, Morphysorb solvent loss, is being evaluated over a longer-term period in order to accurately assess it. However, the preliminary indications based on makeup solvent used to date are that solvent losses will also be within expectations. The analysis of the solvent samples indicates that the solvent is very stable and did not show any sign of degradation. The operability of the solvent is good and no foaming related problems have been encountered. According to plant operators the Morphysorb unit runs smoothly and requires no special attention.

Nagaraju Palla; Dennis Leppin

2004-02-01T23:59:59.000Z

379

Colorado Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Colorado Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 112,440 96,397 85,171 1970's 82,736 97,420 104,116 110,662 118,686 136,090 175,624 171,233 167,959 1980's 201,637 220,108 173,894 181,150 191,625 163,614 180,290 178,048 196,682 1990's 208,069 234,851 256,019 307,250 353,855 345,441 493,963 374,728 425,083 444,978 2000's 494,581 497,385 534,295 555,544 703,804 730,948 751,036 888,705 1,029,641 1,233,260 2010's 1,434,003 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014

380

Oklahoma Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Oklahoma Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 1,038,103 1,122,692 1,167,150 1970's 1,183,273 1,123,614 1,116,872 1,175,548 1,092,487 1,033,003 1,072,992 1,057,326 1,069,293 1980's 1,063,256 1,112,740 1,023,057 1,118,403 1,137,463 1,103,062 1,127,780 1,301,673 1,145,688 1990's 1,102,301 1,100,812 1,071,426 1,082,452 1,092,734 1,015,965 1,054,123 1,014,008 947,177 892,396 2000's 963,464 957,665 854,220 804,029 839,366 865,411 908,055 964,709 1,047,643 1,112,510 2010's 1,110,236 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data.

Note: This page contains sample records for the topic "gas processing plants" 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

Michigan Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Michigan Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 171,531 156,996 143,802 1970's 139,571 141,784 94,738 37,384 45,106 79,154 151,318 172,578 199,347 1980's 155,984 151,560 137,364 148,076 151,393 142,255 137,687 125,183 123,578 1990's 134,550 170,574 186,144 201,985 196,000 179,678 117,119 86,564 83,052 67,514 2000's 58,482 50,734 47,292 41,619 37,977 34,545 33,213 29,436 30,008 23,819 2010's 22,405 21,518 21,243 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014

382

Arkansas Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Arkansas Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 93,452 88,011 56,190 1970's 37,816 31,387 17,946 26,135 19,784 17,918 20,370 18,630 18,480 1980's 29,003 31,530 33,753 34,572 258,648 174,872 197,781 213,558 228,157 1990's 272,278 224,625 156,573 198,074 218,710 100,720 219,477 185,244 198,148 179,524 2000's 207,045 207,352 12,635 13,725 10,139 16,756 13,702 11,532 6,531 2,352 2010's 9,599 5,611 6,872 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014

383

California Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) California Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 505,063 476,596 455,692 1970's 444,700 431,605 386,664 359,841 252,402 213,079 216,667 206,981 204,693 1980's 169,812 261,725 263,475 276,209 281,389 263,823 276,969 270,191 254,286 1990's 263,667 246,335 243,692 246,283 228,346 226,548 240,566 243,054 235,558 259,518 2000's 260,049 258,271 249,671 238,743 236,465 226,230 223,580 206,239 195,272 198,213 2010's 204,327 180,648 169,203 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 1/7/2014

384

Wyoming Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Wyoming Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 261,478 259,227 269,921 1970's 276,926 292,434 298,439 303,519 263,684 215,104 251,846 262,801 255,760 1980's 366,530 393,027 432,313 579,479 624,619 506,241 512,579 560,603 591,472 1990's 635,922 681,266 728,113 750,853 821,689 895,129 845,253 863,052 870,518 902,889 2000's 993,702 988,595 1,083,860 1,101,425 1,249,309 1,278,087 1,288,124 1,399,570 1,278,439 1,507,142 2010's 1,642,190 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 1/7/2014

385

Texas Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Texas Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 7,018,237 7,239,621 7,613,234 1970's 7,808,476 7,938,550 8,139,408 7,683,830 7,194,453 6,509,132 6,253,159 6,030,131 5,621,419 1980's 4,563,931 4,507,771 4,258,852 4,377,799 4,164,382 4,199,501 3,997,226 3,813,727 3,842,395 1990's 3,860,388 4,874,718 4,231,145 4,301,504 4,160,551 4,132,491 4,180,062 4,171,967 4,073,739 3,903,351 2000's 4,096,535 3,876,399 3,861,114 3,658,929 3,748,670 3,781,565 3,990,862 4,187,358 4,431,574 4,478,331 2010's 4,534,403 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data.

386

Alaska Natural Gas Processed (Million Cubic Feet)  

Gasoline and Diesel Fuel Update (EIA)

Processed (Million Cubic Feet) Processed (Million Cubic Feet) Alaska Natural Gas Processed (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1960's 0 1970's 0 0 0 0 0 0 149,865 151,669 147,954 1980's 111,512 115,394 42,115 62,144 66,062 58,732 134,945 76,805 75,703 1990's 1,571,438 1,873,279 2,121,838 2,295,499 2,667,254 2,980,557 2,987,364 2,964,734 2,966,461 2,950,502 2000's 3,123,599 2,984,807 2,997,824 2,447,017 2,680,859 3,089,229 2,665,742 2,965,956 2,901,760 2,830,034 2010's 2,731,803 2,721,396 2,788,997 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 1/7/2014 Next Release Date: 1/31/2014

387

New Concepts in Hardware and Processes to Conserve Oil and Gas in Industrial Processes  

E-Print Network (OSTI)

A broad program to identify and evaluate new types of hardware and processes to conserve oil and gas in chemical plants and petroleum refineries has been completed. During the course of this program, which was sponsored by the Office of Industrial Programs of the U.S. Department of Energy, Argonne interacted with 130 industrial companies to help define and evaluate appropriate areas of technology. The initial step was to assemble a master list of technologies that promised to conserve oil and gas. These technologies were then screened on the basis of quantity of energy saved, capital and operating costs, industry attitude, market potential, and special barriers to implementation such as environmental issues and other special types of problems. One approach used to determine industry attitudes on technologies was to poll several key energy-conservation groups. These included the Gulf Coast Energy Society, Golden Triangle Energy Society, CMA Energy Committee, and the Energy Conservation Committee of the American Petroleum Institute. This paper will summarize some of the results of this program in terms of the following areas of technology: Energy-efficient methods of separation ; Alternative fuels and feed stocks ; Recovery of low-level heat; Advanced Concepts Although the above technologies were identified and evaluated in terms of their application specifically to chemical plants and petroleum refineries, they have the potential of conserving oil and gas across a broad spectrum of industrial processes.

Humphrey, J. L.

1982-01-01T23:59:59.000Z

388

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology Group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group first found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produced about 1 MMscfd of gas containing 24% nitrogen. The membrane unit was built to bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid was built by ABB. NTE ordered the required compressor and MTR made the membrane modules for a December 2004 delivery. However, the gas supply was not steady enough for field testing, and MTR/ABB have now located other sites for field testing and commercial development.

Kaaeid Lokhandwala

2005-12-22T23:59:59.000Z

389

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR is now working with the company's Randall Gas Technology Group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group first found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produced about 1 MMscfd of gas containing 24% nitrogen. The membrane unit was built to bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid was built by ABB. NTE ordered the required compressor and MTR made the membrane modules for a December 2004 delivery. However, the gas supply was not steady enough for field testing, and MTR/ABB have now located other sites for field testing and commercial development.

Kaaeid Lokhandwala

2005-12-15T23:59:59.000Z

390

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd nitrogen removal/gas treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project field test at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. The membrane skid is scheduled to be completed by December 29. Our target is to have the unit installed and optimized by mid-January.

Kaaeid Lokhandwala

2005-02-28T23:59:59.000Z

391

Consider trigeneration techniques for process plants  

SciTech Connect

Trigeneration has, until recently, been used exclusively for air conditioning systems with small or moderate capacities. However, with more recent chiller packages providing larger capacities, and with modern cogeneration applications, trigeneration is now open to a wider range of process applications. It can provide tremendous hydrocarbon processing industry opportunities for more economical use of energy. Cogeneration is the most widely used technique for producing heat and power. If refrigeration is also produced form the same energy source, then the cogeneration simply becomes trigeneration. The technique is not new, it is commonly used in district heating and cooling schemes. However, trigeneration is being used more in the oil and gas, and petrochemical industries as three products--heat, power and refrigeration--are frequently needed in many modern processes. Moreover, this technique provides a wide scope for technical advances. The paper discusses the equipment needed as driver, waste heat recovery, refrigeration equipment, thermodynamics, capacity size limits, different trigeneration configurations, economics, and design enhancements to improve operating economy.

Dharmadhikari, S. [Ingerop, Paris (France)

1997-07-01T23:59:59.000Z

392

TECHNICAL AND OPERATING SUPPORT FOR PILOT DEMONSTRATION OF MORPHYSORB ACID GAS REMOVAL PROCESS  

Science Conference Proceedings (OSTI)

GTI and Krupp Uhde have been jointly developing advanced technology for removing high concentrations of acid gas from high-pressure natural gas for over a decade. This technology, the Morphysorb{reg_sign} process, based on N-formyl and N-acetyl morpholine mixtures, has now been tested in a large-scale facility and this paper presents preliminary results from acceptance testing at that facility. Earlier publications have discussed the bench-scale and pilot plant work that led up to this important milestone. The site was Duke Energy's new Kwoen sour gas upgrader near Chetwynd B.C., Canada. This facility has a nameplate capacity of 300 MMscfd of sour natural gas. The objective of the Morphysorb process at this site was to remove 33 MMscfd of acid gas (H{sub 2}S and CO{sub 2}) for reinjection downhole. This represents about half the acid gas present in the feed to the plant. In so doing, proportionately more of the plant ''sales'' gas, which is sent for final processing at the nearby Pine River plant, can be sent down the line without coming up against the sulfur removal capacity limits of Pine River plant, than could with other solvents that were evaluated. Other benefits include less loss of methane downhole with the rejected acid gas and lower circulation and recycle compression horsepower than with competitive solvents. On the downside, the process is expected to have higher solvent vaporization losses than competitive solvents, but this is a comparatively minor drawback when weighed against the value of the benefits. These benefits (and drawbacks) were developed into quantitative ''acceptance'' criteria, which will determine if the solvent will continue to be used at the site and for award of monetary bonuses to the process developer (GTI).

Nagaraju Palla; Dennis Leppin

2003-09-30T23:59:59.000Z

393

TECHNICAL AND OPERATING SUPPORT FOR PILOT DEMONSTRATION OF MORPHYSORB ACID GAS REMOVAL PROCESS  

Science Conference Proceedings (OSTI)

GTI and Krupp Uhde have been jointly developing advanced technology for removing high concentrations of acid gas from high-pressure natural gas for over a decade. This technology, the Morphysorb{reg_sign} process, based on N-formyl and N-acetyl morpholine mixtures, has now been tested in a large-scale facility and this paper presents preliminary results from acceptance testing at that facility. Earlier publications have discussed the bench-scale and pilot plant work that led up to this important milestone. The site was Duke Energy's new Kwoen sour gas upgrader near Chetwynd B.C., Canada. This facility has a nameplate capacity of 300 MMscfd of sour natural gas. The objective of the Morphysorb process at this site was to remove 33 MMscfd of acid gas (H{sub 2}S and CO{sub 2}) for reinjection downhole. This represents about half the acid gas present in the feed to the plant. In so doing, proportionately more of the plant ''sales'' gas, which is sent for final processing at the nearby Pine River plant, can be sent down the line without coming up against the sulfur removal capacity limits of Pine River plant, than could with other solvents that were evaluated. Other benefits include less loss of methane downhole with the rejected acid gas and lower circulation and recycle compression horsepower than with competitive solvents. On the downside, the process is expected to have higher solvent vaporization losses than competitive solvents, but this is a comparatively minor drawback when weighed against the value of the benefits. These benefits (and drawbacks) were developed into quantitative ''acceptance'' criteria, which will determine if the solvent will continue to be used at the site and for award of monetary bonuses to the process developer (GTI).

Nagaraju Palla; Dennis Leppin

2003-06-30T23:59:59.000Z

394

HTGR-GT closed-cycle gas turbine: a plant concept with inherent cogeneration (power plus heat production) capability  

SciTech Connect

The high-grade sensible heat rejection characteristic of the high-temperature gas-cooled reactor-gas turbine (HTGR-GT) plant is ideally suited to cogeneration. Cogeneration in this nuclear closed-cycle plant could include (1) bottoming Rankine cycle, (2) hot water or process steam production, (3) desalination, and (4) urban and industrial district heating. This paper discusses the HTGR-GT plant thermodynamic cycles, design features, and potential applications for the cogeneration operation modes. This paper concludes that the HTGR-GT plant, which can potentially approach a 50% overall efficiency in a combined cycle mode, can significantly aid national energy goals, particularly resource conservation.

McDonald, C.F.

1980-04-01T23:59:59.000Z

395

Oklahoma Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

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

Fuel Consumption (Million Cubic Feet) Fuel Consumption (Million Cubic Feet) Oklahoma Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 29,750 31,237 31,121 29,705 35,751 40,508 38,392 1990's 39,249 42,166 39,700 39,211 35,432 34,900 35,236 30,370 26,034 25,055 2000's 25,934 28,266 25,525 26,276 27,818 27,380 28,435 28,213 27,161 24,089 2010's 23,238 24,938 27,809 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Plant Fuel Consumption Oklahoma Natural Gas Consumption by End Use Plant Fuel Consumption of Natural Gas (Summary)

396

Alaska Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

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

Fuel Consumption (Million Cubic Feet) Fuel Consumption (Million Cubic Feet) Alaska Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 1,225 1,736 1,807 1,582 4,278 2,390 2,537 1990's 27,720 36,088 36,741 35,503 37,347 39,116 40,334 40,706 39,601 41,149 2000's 42,519 42,243 44,008 44,762 44,016 43,386 38,938 41,197 40,286 39,447 2010's 37,316 35,339 37,397 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Plant Fuel Consumption Alaska Natural Gas Consumption by End Use Plant Fuel Consumption of Natural Gas (Summary)

397

Louisiana Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

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

Fuel Consumption (Million Cubic Feet) Fuel Consumption (Million Cubic Feet) Louisiana Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 121,848 123,993 104,292 102,185 123,008 121,936 134,132 1990's 82,828 83,733 86,623 74,925 66,600 75,845 69,235 71,155 63,368 68,393 2000's 69,174 63,137 63,031 56,018 55,970 45,837 46,205 51,499 42,957 39,002 2010's 40,814 42,633 42,123 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Plant Fuel Consumption Louisiana Natural Gas Consumption by End Use Plant Fuel Consumption of Natural Gas (Summary)

398

Wyoming Natural Gas Plant Fuel Consumption (Million Cubic Feet)  

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

Fuel Consumption (Million Cubic Feet) Fuel Consumption (Million Cubic Feet) Wyoming Natural Gas Plant Fuel Consumption (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1980's 12,572 16,185 17,090 13,633 16,249 17,446 19,820 1990's 12,182 14,154 13,217 13,051 13,939 14,896 15,409 15,597 16,524 19,272 2000's 20,602 20,991 25,767 28,829 24,053 24,408 23,868 25,276 23,574 25,282 2010's 27,104 28,582 29,157 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 12/12/2013 Next Release Date: 1/7/2014 Referring Pages: Natural Gas Plant Fuel Consumption Wyoming Natural Gas Consumption by End Use Plant Fuel Consumption of Natural Gas (Summary)

399

Troubleshooting natural gas processing: Wellhead to transmission  

Science Conference Proceedings (OSTI)

This book describes practical, day-to-day problems of natural gas handling. This book combines field experience with technical principles on natural gas production treating and transmission. This volume is dominated by illustrative case histories and rules of thumb. The book also provides a checklist of distillation problems which is a summary of causes and cures of the problems encountered in the fractionation of propane, butane and natural gasoline. A glossary of terms used in natural gas transmission is another good part of this book. The author has avoided complex mechanical details in favor of simple line drawings. Among the topics discussed are; wellhead pressure and gas flow, vapor-liquid separation at the wellhead, wellhead compression, corrosion in gathering systems, gas sweetening using amines, sulfur recovery, dehydration, centrifugal gas compression, reciprocal gas compression, hydrates, gas cooling and condensate recovery.

Lieberman, N.

1987-01-01T23:59:59.000Z

400

Role of gas and steam turbines to reduce industrial plant energy costs  

SciTech Connect

Data are given to help industry select the economic fuel and economic mix of steam and gas turbines for energy-conservation measures and costs. Utilities and industrials can no longer rely on a firm supply of natural gas to fuel their boilers and turbines. The effect various liquid fuels have on gas turbine maintenance and availability is summarized. Process heat requirements per unit of power, process steam pressure, and the type of fuel will be factors in evaluating the proper mix of steam and gas turbines. The plant requirements for heat, and the availability of a reliable source of electric power will influence the amount of power (hp and kW) that can be economically generated by the industrial. (auth)

Wilson, W.B.; Hefner, W.J.

1973-11-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Texas - RRC District 7B Natural Gas Plant Liquids, Proved Reserves...  

Gasoline and Diesel Fuel Update (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 7B Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

402

U.S. Federal Offshore Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) U.S. Federal Offshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

403

Texas - RRC District 7C Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 7C Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

404

Texas - RRC District 8A Natural Gas Plant Liquids, Proved Reserves...  

Annual Energy Outlook 2012 (EIA)

Gas Plant Liquids, Proved Reserves (Million Barrels) Texas - RRC District 8A Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

405

Defining the needs for gas centrifuge enrichment plants advanced safeguards  

Science Conference Proceedings (OSTI)

Current safeguards approaches used by the International Atomic Energy Agency (IAEA) at gas centrifuge enrichment plants (GCEPs) need enhancement in order to verify declared low-enriched (LEU) production, detect undeclared LEU production and detect highly enriched uranium (HEU) production with adequate detection probability using nondestructive assay (NDA) techniques. At present inspectors use attended systems, systems needing the presence of an inspector for operation, during inspections to verify the mass and {sup 235}U enrichment of declared UF{sub 6} containers used in the process of enrichment at GCEPs. In verifying declared LEU production, the inspectors also take samples for off-site destructive assay (DA) which provide accurate data, with 0.1% to 0.5% measurement uncertainty, on the enrichment of the UF{sub 6} feed, tails, and product. However, taking samples of UF{sub 6} for off-site analysis is a much more labor and resource intensive exercise for the operator and inspector. Furthermore, the operator must ship the samples off-site to the IAEA laboratory which delays the timeliness of results and interruptions to the continuity of knowledge (CofK) of the samples during their storage and transit. This paper contains an analysis of possible improvements in unattended and attended NDA systems such as process monitoring and possible on-site analysis of DA samples that could reduce the uncertainty of the inspector's measurements and provide more effective and efficient IAEA GCEPs safeguards. We also introduce examples advanced safeguards systems that could be assembled for unattended operation.

Boyer, Brian David [Los Alamos National Laboratory; Erpenbeck, Heather H [Los Alamos National Laboratory; Miller, Karen A [Los Alamos National Laboratory; Swinhoe, Martyn T [Los Alamos National Laboratory; Ianakiev, Kiril [Los Alamos National Laboratory; Marlowe, Johnna B [Los Alamos National Laboratory

2010-01-01T23:59:59.000Z

406

Techno-socio-economic study of bio-gas plants  

Science Conference Proceedings (OSTI)

This study covers technological, social and economic aspects of the biogas program in Chitawan, Nepal. Many interesting facts are revealed which may be useful for future planning of Nepalese biogas programs. Concerning the social aspects, only big farmers (having more than 4 bighas of land and more than 10 domestic animals) were found to have biogas plants. No farmer who had a biogas plant was illiterate. As for the technical aspects of the total gas ovens used in the area, 66% were of BTI design. Most of the ovens were of 0.45-m/sup 3/ capacity. The life of BTI ovens was found to be shorter than the life of ovens of other companies. BTI ovens are not useful when farmers have to use a big pot for cooking. All farmers of the area were found to be convinced of the utility of the biogas plant. With regard to the economic aspects of using biogas plants, farmers were able to save 53% of the total expenditure which they had been spending for fuel. Wood consumption was reduced to 50% by using biogas. The internal rate of return of a 2.8-m/sup 3/ biogas plant was found to be 14% assuming that the plant would last for 20 years. Most of the farmers in the area did not have biogas plants. The main reason given was that there were not enough capital and cattle to begin such an operation.

Not Available

1981-01-01T23:59:59.000Z

407

Weekly U.S. Refiner, Blender, and Gas Plant Net Production of ...  

U.S. Energy Information Administration (EIA)

Weekly U.S. Refiner, Blender, and Gas Plant Net Production of Propane and Propylene (Thousand Barrels per Day)

408

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. The membrane skid is scheduled to be completed by December 29. Our target is to have the unit installed and optimized by mid-January.

Kaaeid Lokhandwala

2004-09-01T23:59:59.000Z

409

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. The membrane skid is scheduled to be completed by December 29. Our target is to have the unit installed and optimized by mid-January.

Kaaeid Lokhandwala

2004-11-15T23:59:59.000Z

410

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During precommissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. The membrane skid is scheduled to be completed by December 29. The target is to have the unit installed and optimized by mid-January.

Andre Da Costa

2003-11-24T23:59:59.000Z

411

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPERATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. System fabrication was completed in January 2004 and the membrane inserts were loaded. Additional pressure testing and verification will be completed prior to shipment, which is expected in early February 2004.

Kaaeid Lokhandwala

2004-01-30T23:59:59.000Z

412

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group has found a new site for the project at a North Texas Exploration (NTE) gas processing plant. The plant produces about 1 MMscfd of gas containing 24% nitrogen. The membrane unit will bring this gas to 4% nitrogen for delivery to the pipeline. The membrane skid is being built by ABB. NTE has ordered the required compressor and MTR is making the membrane modules. System fabrication was completed in January 2004 and the membrane inserts were loaded. Additional pressure testing and verification will be completed prior to shipment, which is expected in early February 2004.

Kaaeid Lokhandwala

2003-12-31T23:59:59.000Z

413

Treatment of gas from an in situ conversion process  

SciTech Connect

A method of producing methane is described. The method includes providing formation fluid from a subsurface in situ conversion process. The formation fluid is separated to produce a liquid stream and a first gas stream. The first gas stream includes olefins. At least the olefins in the first gas stream are contacted with a hydrogen source in the presence of one or more catalysts and steam to produce a second gas stream. The second gas stream is contacted with a hydrogen source in the presence of one or more additional catalysts to produce a third gas stream. The third gas stream includes methane.

Diaz, Zaida (Katy, TX); Del Paggio, Alan Anthony (Spring, TX); Nair, Vijay (Katy, TX); Roes, Augustinus Wilhelmus Maria (Houston, TX)

2011-12-06T23:59:59.000Z

414

Sediment Capping Resource Guide for Manufactured Gas Plant Sites  

Science Conference Proceedings (OSTI)

This report describes tools and techniques applicable to design and implementation of sediment capping remedies at former manufactured gas plant (MGP) sites. It includes a number of practical case studies describing cap designs and cap construction experience. The report is intended as a sediment capping resource guide to be used with EPRI's 2007 Handbook of Remedial Alternatives for MGP Sites with Contaminated Sediments (EPRI report 1012592).

2008-11-18T23:59:59.000Z

415

Groundwater Closure Strategy for Former Manufactured Gas Plant Sites  

Science Conference Proceedings (OSTI)

Utilities responsible for Manufactured Gas Plant (MGP) remediation must navigate numerous challenges in order to attain regulatory closure. Typically, the first strategic focus is on source remediation: to locate, treat or remove MGP residuals that constitute ongoing sources of impacts to receptors (e.g., direct contact, soil vapor, or groundwater). Often the last compliance piece that must fall into place is compliance with regulatory criteria for groundwater. The state-specific regulatory closure ...

2012-12-12T23:59:59.000Z

416

Renewable LNG: Update on the World's Largest Landfill Gas to LNG Plant  

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

LNG LNG Update on the world's largest landfill gas to LNG plant Mike McGowan Head of Government Affairs Linde NA, Inc. June 12, 2012 $18.3 billion global sales A leading gases and engineering company Linde North America Profile $2.3 billion in gases sales revenue in North America in 2011 5,000 employees throughout the U.S., Canada and the Caribbean Supplier of compressed and cryogenic gases and technology Atmospheric gases - oxygen, nitrogen, argon Helium LNG and LPG Hydrogen Rare gases Plant engineering and supply LNG Petrochemicals Natural gas processing Atmospheric gases 3 Linde's alternative fuels portfolio Green hydrogen production - Magog, Quebec Renewable liquefied natural gas production - Altamont, CA Biogas fueling, LNG import terminal - Sweden

417

The advanced PFB process: Pilot plant results and design studies  

SciTech Connect

The plant being developed is a hybrid of two technologies; it incorporates the partial gasification of coal in a vessel called the carbonizer and the combustion of the resultant char residue in a circulating pressurized fluidized bed combustor (CPFBC). In this plant, coal is fed to a pressurized carbonizer that produces a low-Btu fuel gas and char. After passing through a cyclone and a ceramic barrier filter to remove gas-entrained particulates, the fuel gas is burned in a topping combustor to produce the energy required to drive a gas turbine. The gas turbine drives a generator and a compressor that feeds air to the carbonizer, a CPFBC, and a fluidized bed heat exchanger (FBHE). The carbonizer char is burned in the CPFBC with high excess air. The vitiated air from the CPFBC supports combustion of the fuel gas in the gas turbine topping combustor. Steam generated in a heat-recovery steam generator (HRSG) downstream of the gas turbine and in the FBHE associated with the CPFBC drives the steam turbine generator that furnishes the balance of electric power delivered by the plant. The low-Btu gas is produced in the carbonizer by pyrolysis/mild devolatilization of coal in a fluidized bed reactor. Because this unit operates at temperatures much lower than gasifiers currently under development, it also produces a char residue. Left untreated, the fuel gas will contain hydrogen sulfide and sulfur-containing tar/light oil vapors; therefore, lime-based sorbents are injected into the carbonizer to catalytically enhance tar cracking and to capture sulfur as calcium sulfide. Sulfur is captured in situ, and the raw fuel gas is fired hot. Thus the expensive, complex, fuel gas heat exchangers and the chemical or sulfur-capturing bed cleanup systems that are part of the coal gasification combined-cycle plants now being developed are eliminated.

Robertson, A. [Foster Wheeler Development Corp., Livingston, NJ (United States); Domeracki, W. [Westinghouse Power Generation Business Group, Orlando, FL (United States); Horazak, D. [Gilbert/Commonwealth, Green Hills, PA (United States); Newby, R. [Westinghouse Science and Technology Center, Pittsburgh, PA (United States); Rehmat, A. [Institute of Gas Technology, Chicago IL (United States)

1993-11-01T23:59:59.000Z

418

Fuel gas main replacement at Acme Steel's coke plant  

SciTech Connect

ACME Steel's Chicago coke plant consists of two 4-meter, 50-oven Wilputte underjet coke-oven batteries. These batteries were constructed in 1956--1957. The use of blast furnace gas was discontinued in the late 1960's. In 1977--1978, the oven walls in both batteries were reconstructed. Reconstruction of the underfire system was limited to rebuilding the coke-oven gas reversing cocks and meter in orifices. By the early 1980's, the 24-in. diameter underfire fuel gas mains of both batteries developed leaks at the Dresser expansion joints. These leaks were a result of pipe loss due to corrosion. Leaks also developed along the bottoms and sides of both mains. A method is described that permitted pushing temperatures to be maintained during replacement of underfire fuel gas mains. Each of Acme's two, 50-oven, 4-metric Wilputte coke-oven, gas-fired batteries were heated by converting 10-in. diameter decarbonizing air mains into temporary fuel gas mains. Replacement was made one battery at a time, with the temporary 10-in. mains in service for five to eight weeks.

Trevino, O. (Acme Steel Co., Chicago, IL (United States). Chicago Coke Plant)

1994-09-01T23:59:59.000Z

419

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

420

Method for processing coke oven gas  

SciTech Connect

Coke oven gas is subjected, immediately after the discharge thereof from coke ovens, and without any preliminary cooling operation or any purification operation other than desulfurization, to a catalytic cracking operation to form a hot cracked gas which is rich in hydrogen and carbon monoxide. The catalytic cracking reaction is carried out in the presence of a hydrogen-containing and/or CO2-containing gas, with a steam reforming catalyst.

Flockenhaus, C.; Meckel, J.F.; Wagener, D.

1980-11-25T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Gas turbine electric plant construction cost and annual production expenses. First annual publication, 1972  

SciTech Connect

By the end of 1972, gas turbine power plants owned and operated by U.S. utilities had a capacity of 27,918 MW. Data from the 1972 annual reports filed with the Federal Power Commission by utility systems are presented which show the plant cost, generating expenses, capacity and generation, and plant and equipment characteristics of 299 gas turbine plants. (LCL)

1972-01-01T23:59:59.000Z

422

pH Adjustment of Power Plant Cooling Water with Flue Gas/Fly Ash  

to fossil fuel burning power plants to control mineral precipitation in cooling water. Flue gas, which is 10% CO2, could be diverted into a plant’s cooling water

423

Sales and Use Tax Exemption for Gas Processing Facilities  

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

In North Dakota, materials purchased for building or expending gas processing facilities are exempt from sales and use taxes. Building materials, equipment, and other tangible property are eligible...

424

Process Optimization of Cast Alloy 718 for Water Cooled Gas ...  

Science Conference Proceedings (OSTI)

FOR WATER COOLED GAS TURBINE APPLICATION. G.K. Bouse+ and P.W. Schilke*. Gene@ Electric Company+ Materials and Processes Laboratory, and.

425

File:BOEMRE oil.gas.plant.platform.sta.brbra.map.4.2010.pdf | Open Energy  

Open Energy Info (EERE)

oil.gas.plant.platform.sta.brbra.map.4.2010.pdf oil.gas.plant.platform.sta.brbra.map.4.2010.pdf Jump to: navigation, search File File history File usage Federal Leases in Pacific Ocean, near Santa Barbara Channel Size of this preview: 463 × 599 pixels. Other resolution: 464 × 600 pixels. Full resolution ‎(1,275 × 1,650 pixels, file size: 234 KB, MIME type: application/pdf) Description Federal Leases in Pacific Ocean, near Santa Barbara Channel Sources Bureau of Ocean Energy Management, Regulation and Enforcement (BOEMRE) Related Technologies Oil, Natural Gas Creation Date 2010-04 Extent Santa Barbara Channel Countries United States UN Region Northern America States California Locations of oil and separation and treatment plants, oil separation, gas processing, and treatment plants, oil spill response vessels, platforms,

426

GRR/Section 7-CA-b - State Plant Commissioning Process, Small Power Plant  

Open Energy Info (EERE)

7-CA-b - State Plant Commissioning Process, Small Power Plant 7-CA-b - State Plant Commissioning Process, Small Power Plant Exception < GRR Jump to: navigation, search GRR-logo.png GEOTHERMAL REGULATORY ROADMAP Roadmap Home Roadmap Help List of Sections Section 7-CA-b - State Plant Commissioning Process, Small Power Plant Exception 07CABPlantCommissioningProcessSmallPowerPlantExemption.pdf Click to View Fullscreen Contact Agencies California Energy Commission Regulations & Policies California Code of Regulations, Title 20 - Public Utilities and Energy Triggers None specified Click "Edit With Form" above to add content 07CABPlantCommissioningProcessSmallPowerPlantExemption.pdf Error creating thumbnail: Page number not in range. Error creating thumbnail: Page number not in range. Error creating thumbnail: Page number not in range.

427

Hot gas cleanup and gas turbine aspects of an advanced PFBC power plant  

SciTech Connect

The overall objective of the second-generation PFBC development program is to advance this concept to a commercial status. Three major objectives of the current Phase 2 program activities are to: Separately test key components of the second-generation PFBC power plant at sub-scale to ascertain their performance characteristics, Revise the commercial plant performance and economic predictions where necessary, Prepare for a 1.6 MWe equivalent Phase 3 integrated subsystem test of the key components. The key components of the plant, with respect to development risk, are the carbonizer, the circulating PFBC unit, the ceramic barrier filter, and the topping combustor. This paper reports on the development and testing of one key component -- the ceramic barrier filter for the carbonizer fuel gas. The objective of the Phase 2 carbonizer ceramic barrier filter testing has been to confirm filter performance and operability in the carbonizer fuel gas environment.

Robertson, A. (Foster Wheeler Development Corp., Livingston, NJ (United States)); Newby, R.A.; Alvin, M.A.; Bachovchin, D.M.; Bruck, G.J.; Smeltzer, E.E. (Westinghouse Electric Corp., Pittsburgh, PA (United States). Science and Technology Center)

1992-01-01T23:59:59.000Z

428

Economic assessment of advanced flue gas desulfurization processes. Final report  

Science Conference Proceedings (OSTI)

This report presents the results of a project sponsored by the Morgantown Energy Technology Center (METC). The purpose of the study was to perform an economic and market assessment of advanced flue gas desulfurization (FGD) processes for application to coal-fired electric utility plants. The time period considered in the study is 1981 through 1990, and costs are reported in 1980 dollars. The task was divided into the following four subtasks: (1) determine the factors affecting FGD cost evaluations; (2) select FGD processes to be cost-analyzed; (3) define the future electric utility FGD system market; and (4) perform cost analyses for the selected FGD processes. The study was initiated in September 1979, and separate reports were prepared for the first two subtasks. The results of the latter two subtasks appear only in this final reprot, since the end-date of those subtasks coincided with the end-date of the overall task. The Subtask 1 report, Criteria and Methods for Performing FGD Cost Evaluations, was completed in October 1980. A slightly modified and condensed version of that report appears as appendix B to this report. The Subtask 2 report, FGD Candidate Process Selection, was completed in January 1981, and the principal outputs of that subtask appear in Appendices C and D to this report.

Bierman, G. R.; May, E. H.; Mirabelli, R. E.; Pow, C. N.; Scardino, C.; Wan, E. I.

1981-09-01T23:59:59.000Z

429

Process for selected gas oxide removal by radiofrequency catalysts  

DOE Patents (OSTI)

This process to remove gas oxides from flue gas utilizes adsorption on a char bed subsequently followed by radiofrequency catalysis enhancing such removal through selected reactions. Common gas oxides include SO[sub 2] and NO[sub x]. 1 figure.

Cha, C.Y.

1993-09-21T23:59:59.000Z

430

Natural Gas Liquefaction Process for Small-scale LNG Project  

Science Conference Proceedings (OSTI)

In the field of natural gas liquefaction, the small-scale natural gas liquefier has been attracting more and more attentions home and abroad, thanks to its small volume, mobile transportation, easy start-up and shut-down, as well as skid-mounted package. ... Keywords: Natural gas, Small-scale, LNG, Liquefaction process

Cao Wensheng

2012-03-01T23:59:59.000Z

431

Advanced design nuclear power plants: Competitive, economical electricity. An analysis of the cost of electricity from coal, gas and nuclear power plants  

SciTech Connect

This report presents an updated analysis of the projected cost of electricity from new baseload power plants beginning operation around the year 2000. Included in the study are: (1) advanced-design, standardized nuclear power plants; (2) low emissions coal-fired power plants; (3) gasified coal-fired power plants; and (4) natural gas-fired power plants. This analysis shows that electricity from advanced-design, standardized nuclear power plants will be economically competitive with all other baseload electric generating system alternatives. This does not mean that any one source of electric power is always preferable to another. Rather, what this analysis indicates is that, as utilities and others begin planning for future baseload power plants, advanced-design nuclear plants should be considered an economically viable option to be included in their detailed studies of alternatives. Even with aggressive and successful conservation, efficiency and demand-side management programs, some new baseload electric supply will be needed during the 1990s and into the future. The baseload generating plants required in the 1990s are currently being designed and constructed. For those required shortly after 2000, the planning and alternatives assessment process must start now. It takes up to ten years to plan, design, license and construct a new coal-fired or nuclear fueled baseload electric generating plant and about six years for a natural gas-fired plant. This study indicates that for 600-megawatt blocks of capacity, advanced-design nuclear plants could supply electricity at an average of 4.5 cents per kilowatt-hour versus 4.8 cents per kilowatt-hour for an advanced pulverized-coal plant, 5.0 cents per kilowatt-hour for a gasified-coal combined cycle plant, and 4.3 cents per kilowatt-hour for a gas-fired combined cycle combustion turbine plant.

1992-06-01T23:59:59.000Z

432

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR is working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group found a new site for the project at a North Texas Exploration (NTE) gas processing plant, which met with limited success. MTR then located an alternative testing opportunity and signed a contract with Towne Exploration in the third quarter of 2006, for a demonstration plant in Rio Vista, CA, to be run through May 2007. The demonstration for Towne has already resulted in the sale of two commercial skids to the company; the units will be delivered in mid-2007. Total sales of nitrogen/natural gas membrane separation units from the partnership with ABB are now approaching $4.0 million.

Kaaeid Lokhandwala

2007-03-31T23:59:59.000Z

433

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR is working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group found a new site for the project at a North Texas Exploration (NTE) gas processing plant, and we continue, but have as yet been unsuccessful in our attempts, to negotiate with Atmos Energy for a final test of the original project demonstration unit. In the meantime, MTR has located an alternative testing opportunity and signed a contract with Towne Exploration for a demonstration plant in Rio Vista, CA, to be run through May 2007. Several commercial sales have resulted from the partnership with ABB, and total sales of nitrogen/natural gas membrane separation units are now approaching $2.6 million.

Kaaeid Lokhandwala

2006-09-30T23:59:59.000Z

434

Conceptual Process Plant Utility Schemes with Hybrid Energy System  

Science Conference Proceedings (OSTI)

Use of Alternative energy Production from sun and wind power with storage can become an integral part of a process plant utility. This will facilitate reduced ...

435

State-of-the-art gas turbine and steam turbine power plant  

SciTech Connect

A state-of-the-art power plant in which the heat from solid or low quality fuels is utilized to heat indirectly a motive stream composition of a mixture of steam and gases to drive a gas turbine. The thermal energy from the burning of the solid or low quality fuels is also utilized to generate steam which powers a steam turbine. Excess steam may be generated to be utilized as process steam.

Willyoung, D. M.; Anand, A. K.

1985-03-12T23:59:59.000Z

436

Evaluation of Biosparging for Management of Groundwater at the Manufactured Gas Plant in Baraboo, Wisconsin  

Science Conference Proceedings (OSTI)

This report presents the results of field and modeling studies of the fate and transport of a plume of organic constituents in an aquifer underlying a manufactured gas plant (MGP) site and documents the effectiveness of biosparging technology for remediation of groundwater. Because a significant fraction of naphthalene and other contaminants are only slowly released to the aqueous phase, processes such as biodegradation or pump-and-treat that address constituents in the aqueous phase require exceedingly ...

2001-01-30T23:59:59.000Z

437

Evaluation of In-Situ Solidification/Stabilization For Redevelopment of Manufactured Gas Plant Impacted Sites  

Science Conference Proceedings (OSTI)

Process byproducts produced at manufactured gas plants (MGP) pose concerns from an environmental standpoint. One treatment for the management of a broad range of contaminated media and wastes is solidification/stabilization (S/S). The U.S. Environmental Protection Agency (EPA) considers S/S an established treatment technology and it continues as a cornerstone treatment technology for the management of site remediation. The Electric Power Research Institute (EPRI) has been sponsoring research on the ...

2013-05-09T23:59:59.000Z

438

Thief process for the removal of mercury from flue gas  

DOE Patents (OSTI)

A system and method for removing mercury from the flue gas of a coal-fired power plant is described. Mercury removal is by adsorption onto a thermally activated sorbent produced in-situ at the power plant. To obtain the thermally activated sorbent, a lance (thief) is inserted into a location within the combustion zone of the combustion chamber and extracts a mixture of semi-combusted coal and gas. The semi-combusted coal has adsorptive properties suitable for the removal of elemental and oxidized mercury. The mixture of semi-combusted coal and gas is separated into a stream of gas and semi-combusted coal that has been converted to a stream of thermally activated sorbent. The separated stream of gas is recycled to the combustion chamber. The thermally activated sorbent is injected into the duct work of the power plant at a location downstream from the exit port of the combustion chamber. Mercury within the flue gas contacts and adsorbs onto the thermally activated sorbent. The sorbent-mercury combination is removed from the plant by a particulate collection system.

Pennline, Henry W. (Bethel Park, PA); Granite, Evan J. (Wexford, PA); Freeman, Mark C. (South Park Township, PA); Hargis, Richard A. (Canonsburg, PA); O' Dowd, William J. (Charleroi, PA)

2003-02-18T23:59:59.000Z

439

The NO{sub x} Abatement Program at the Idaho Chemical Processing Plant  

SciTech Connect

A No{sub x} abatement program was implemented at the Idaho Chemical Processing Plant (ICPP) to reduce No{sub x}, emissions from the New Waste Calcining Facility (NWCF). Extensive research and development work has indicated that the selective catalytic reduction (SCR) process is the most promising technology for treating the NWCF off-gas. Laboratory-scale and pilot-plant tests were performed to determine the compatibility of the SCR process with actual NWCF off-gas, and to optimize operating parameters and develop a flow scheme for a full-scale No{sub x}, abatement facility. An advanced conceptual design for the No{sub x}. abatement project, incorporating pilot-plant findings and recommendations, has been completed. Title design by an architectural engineering firm, for the full-scale No{sub x}, abatement facility, is scheduled to begin this year. Construction is scheduled for 1994--1997. The facility is planned to be operational in 1998.

McCray, J.A.; Boardman, R.D.

1992-03-20T23:59:59.000Z

440

Cornell's conversion of a coal fired heating plant to natural Gas -BACKGROUND: In December 2009, the Combined Heat and Power Plant  

E-Print Network (OSTI)

Cornell's conversion of a coal fired heating plant to natural Gas University began operating with natural gas, instead of the coal-fired generators of the coal that had been stockpiled, the Plant is running completely on natural gas

Keinan, Alon

Note: This page contains sample records for the topic "gas processing plants" 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 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

442

Off-site regeneration of gas-plant molecular sieves  

SciTech Connect

The use of regenerated molecular sieve, significantly reduces the operating costs associated with adsorption, dehydration, and processing gas-treating equipment. Laboratory analysis have proven an effective tool in predicting the regenerability of sieve and the expected effectiveness of the regeneration. 2 figures, 1 table.

Moses, J.R. (Catalyst Recovery Canada, Ltd., Calgary, Alberta); Auger, L.E.

1983-03-01T23:59:59.000Z

443

Evaluation of high-efficiency gas-liquid contactors for natural gas processing. Second semiannual technical progress report, April 1, 1993--September 30, 1993  

SciTech Connect

The objective of this proposed program is to evaluate the potential of rotating gas-liquid contactors for natural gas processing by expanding the currently available database. This expansion will focus on application of this technology to environments representative of those typically encountered in natural gas processing plants. Operational and reliability concerns will be addressed while generating pertinent engineering data relating to the mass-transfer process. Work to be performed this reporting period are: complete all negotiations and processing of agreements; complete assembly, modifications, shakedown, and conduct fluid dynamic studies using the plastic rotary contactor unit; confirmation of project test matrix; and locate, and transport an amine plant and dehydration plant. Accomplishment for this period are presented.

Not Available

1993-12-01T23:59:59.000Z

444

Risk-Informed Process Hierarchy for Fossil Plant Maintenance Application  

Science Conference Proceedings (OSTI)

This report describes the functions, capabilities, and features of risk-informed maintenance processes for fossil power plants. This research is the basis on which to develop a software module in an enterprise asset management system (EAMS). Some power plants already use one of the processes described in this report. Additional capabilities are described to enhance that process. New processes are described that address additional applications for risk-informed maintenance.

2008-12-23T23:59:59.000Z

445

Comparison of intergrated coal gasification combined cycle power plants with current and advanced gas turbines  

Science Conference Proceedings (OSTI)

Two recent conceptual design studies examined ''grass roots'' integrated gasification-combined cycle (IGCC) plants for the Albany Station site of Niagara Mohawk Power Corporation. One of these studies was based on the Texaco Gasifier and the other was developed around the British Gas Co.-Lurgi slagging gasifier. Both gasifiers were operated in the ''oxygen-blown'' mode, producing medium Btu fuel gas. The studies also evaluated plant performance with both current and advanced gas turbines. Coalto-busbar efficiencies of approximately 35 percent were calculated for Texaco IGCC plants using current technology gas turbines. Efficiencies of approximately 39 percent were obtained for the same plant when using advanced technology gas turbines.

Banda, B.M.; Evans, T.F.; McCone, A.I.; Westisik, J.H.

1984-08-01T23:59:59.000Z

446

Process for recovering condensible components from a gas stream  

SciTech Connect

A method is described for adsorbing the condensible components out of the inlet gas stream in one of a number of stationary adsorption beds, while simultaneously cooling one or more of the other adsorption beds with the residue gas stream from the adsorbing bed. At the same time, one or more other adsorption beds are heated by a regeneration gas stream in a closed cycle, thereby stripping and vaporizing the condensible components. A special main gas-flow pattern is utilized at the beginning of each cycle to prevent condensible components, remaining in the bed or beds just heated, from being lost, with the gas stream leaving the process. (6 claims)

McMinn, R.E.; Loomer, J.A.; Sellars, A.I.

1970-09-08T23:59:59.000Z

447

Material Consolidation, Rendering, and Disposal Studies of Gas Holders at Former Manufactured Gas Plant Sites  

Science Conference Proceedings (OSTI)

This report presents results of full-scale field implementation studies conducted in conjunction with an evaluation of EPRI-sponsored bench-scale mixing tests. The study was designed to complement bench-scale mixing studies that correlated those results to full-scale remedial actions at former manufactured gas plant (MGP) sites. The field implementation study included a review of potentially applicable remedial approaches, site characterization, bench-scale treatability tests, and results of site remedia...

2001-12-13T23:59:59.000Z

448

Final environmental information volume for the coke oven gas cleaning project at the Bethlehem Steel Corporation Sparrows Point Plant  

Science Conference Proceedings (OSTI)

Bethelehem Steel Corporation (BSC) is planning to conduct a demonstration project involving an integrated system that can be retrofitted into coke oven gas handling systems to address a variety of environmental and operational factors in a more cost-effective manner. Successful application of this technology to existing US coke plants could: (1) reduce emissions of sulfur dioxide, cyanide, and volatile organic compounds (including benzene) (2) reduce the cost and handling of processing feed chemicals, (3) disposal costs of nuisance by-products and (4) increase reliability and reduce operation/maintenance requirements for coke oven gas desulfurization systems. The proposed system will remove sulfur from the coke oven gas in the form of hydrogen sulfide using the ammonia indigenous to the gas as the primary reactive chemical. Ammonia and hydrogen cyanide are also removed in this process. The hydrogen sulfide removed from the coke oven gas in routed to a modified Claus plant for conversion to a saleable sulfur by-product. Ammonia and hydrogen cyanide will be catalytically converted to hydrogen, nitrogen, carbon dioxide, and carbon monoxide. The tail gas from the sulfur recovery unit is recycled to the coke oven gas stream, upstream of the new gas cleaning system. The proposed demonstration project will be installed at the existing coke oven facilities at BSC's Sparrows Point Plant. This volume describes the proposed actions and the resulting environmental impacts. 21 refs., 19 figs., 9 tabs.

Not Available

1990-04-24T23:59:59.000Z

449

Comparative Assessment of Coal-and Natural Gas-fired Power Plants under a  

E-Print Network (OSTI)

Comparative Assessment of Coal- and Natural Gas-fired Power Plants under a CO2 Emission Performance standard (EPS) for pulverized coal (PC) and natural gas combined cycle (NGCC) power plants; · Evaluate · Coal-fired Power Plant: Supercritical pulverized coal (SC PC) Illinois #6 Coal Capacity Factor 75

450

Low Quality Natural Gas Sulfur Removal and Recovery CNG Claus Sulfur Recovery Process  

Science Conference Proceedings (OSTI)

Increased use of natural gas (methane) in the domestic energy market will force the development of large non-producing gas reserves now considered to be low quality. Large reserves of low quality natural gas (LQNG) contaminated with hydrogen sulfide (H{sub 2}S), carbon dioxide (CO{sub 2}) and nitrogen (N) are available but not suitable for treatment using current conventional gas treating methods due to economic and environmental constraints. A group of three technologies have been integrated to allow for processing of these LQNG reserves; the Controlled Freeze Zone (CFZ) process for hydrocarbon / acid gas separation; the Triple Point Crystallizer (TPC) process for H{sub 2}S / C0{sub 2} separation and the CNG Claus process for recovery of elemental sulfur from H{sub 2}S. The combined CFZ/TPC/CNG Claus group of processes is one program aimed at developing an alternative gas treating technology which is both economically and environmentally suitable for developing these low quality natural gas reserves. The CFZ/TPC/CNG Claus process is capable of treating low quality natural gas containing >10% C0{sub 2} and measurable levels of H{sub 2}S and N{sub 2} to pipeline specifications. The integrated CFZ / CNG Claus Process or the stand-alone CNG Claus Process has a number of attractive features for treating LQNG. The processes are capable of treating raw gas with a variety of trace contaminant components. The processes can also accommodate large changes in raw gas composition and flow rates. The combined processes are capable of achieving virtually undetectable levels of H{sub 2}S and significantly less than 2% CO in the product methane. The separation processes operate at pressure and deliver a high pressure (ca. 100 psia) acid gas (H{sub 2}S) stream for processing in the CNG Claus unit. This allows for substantial reductions in plant vessel size as compared to conventional Claus / Tail gas treating technologies. A close integration of the components of the CNG Claus process also allow for use of the methane/H{sub 2}S separation unit as a Claus tail gas treating unit by recycling the CNG Claus tail gas stream. This allows for virtually 100 percent sulfur recovery efficiency (virtually zero SO{sub 2} emissions) by recycling the sulfur laden tail gas to extinction. The use of the tail gas recycle scheme also deemphasizes the conventional requirement in Claus units to have high unit conversion efficiency and thereby make the operation much less affected by process upsets and feed gas composition changes. The development of these technologies has been ongoing for many years and both the CFZ and the TPC processes have been demonstrated at large pilot plant scales. On the other hand, prior to this project, the CNG Claus process had not been proven at any scale. Therefore, the primary objective of this portion of the program was to design, build and operate a pilot scale CNG Claus unit and demonstrate the required fundamental reaction chemistry and also demonstrate the viability of a reasonably sized working unit.

Klint, V.W.; Dale, P.R.; Stephenson, C.

1997-10-01T23:59:59.000Z

451

Computer-Aided Design Reveals Potential of Gas Turbine Cogeneration in Chemical and Petrochemical Plants  

E-Print Network (OSTI)

Gas turbine cogeneration cycles provide a simple and economical solution to the problems created by rising fuel and electricity costs. These cycles can be designed to accommodate a wide range of electrical, steam, and process heating demands. The optimum cycle is typically based on an analysis of the plant's electrical / steam / process heating requirements, an evaluation of the potential for selling to or permit wheeling by utilities of electrical power under PURPA guidelines, and application of pertinent investment decision criteria. The study that identifies the best solution to the problem must contain sufficient detail to support a plan of action by management. This paper addresses how computer-aided design techniques support the effort necessary to fully evaluate several alternative cycle designs in a short time frame. It includes examples for a new power unit as well as for cycles which require modifications to existing process and steam generating equipment in a medium-sized chemical plant.

Nanny, M. D.; Koeroghlian, M. M.; Baker, W. J.

1984-01-01T23:59:59.000Z

452

Adsorption process producing chronologically constant amount of a residual gas  

SciTech Connect

An adsorption process is disclosed for purifying or fractionating a gaseous feed mixture comprises an adsorption phase, at least one expansion phase, a purging phase and at least one pressure buildup phase. The expansion phase(S) and the purging phase produce residual process gas fractions. The sum total of volume, and/or mass streams of the residual process gas fractions comprises a residual gas stream which is maintained chronologically substantially constant by controlling the volume and/or gas streams of the gas entering the purging phase and maintaining the gas leaving the expansion phase(S) at a substantially constant value, dependent on the desired mass and/or volume quantity of the residual gas stream. The length of the purging phase and of the expansion phase(S) is adjusted accordingly so that the relationship of the length of time of the purging phase to the length of time of the expansion phase(S) is substantially the same as the relationship of the volume and/or mass of the gas fractions obtained during the purging to those obtained during the expansion phase(S), respectively. The control of the purging and of the expansion phase(S) can also be varied in response to a flow rate of a feed gas entering the process.

Benkmann, C.

1982-02-16T23:59:59.000Z

453

Field Demonstration of a Membrane Process to Separate Nitrogen from Natural Gas  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During pre-commissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Since that time, Membrane Technology and Research, Inc. (MTR) has signed a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with the company's Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry. Randall's engineering group found a new site for the project at a North Texas Exploration (NTE) gas processing plant, and we are now negotiating with Atmos Energy for a final test of the project demonstration unit. Several commercial sales have also resulted from the partnership with ABB, and sales of nitrogen/natural gas membrane separation units now total $2.3 million.

Kaaeid Lokhandwala

2006-03-20T23:59:59.000Z

454

Cryogenic fractionator gas as stripping gas of fines slurry in a coking and gasification process  

DOE Patents (OSTI)

In an integrated coking and gasification process wherein a stream of fluidized solids is passed from a fluidized bed coking zone to a second fluidized bed and wherein entrained solid fines are recovered by a scrubbing process and wherein the resulting solids-liquid slurry is stripped with a stripping gas to remove acidic gases, at least a portion of the stripping gas comprises a gas comprising hydrogen, nitrogen and methane separated from the coker products.

DeGeorge, Charles W. (Chester, NJ)

1981-01-01T23:59:59.000Z

455

Hydrogen Gas Production from Nuclear Power Plant in Relation to Hydrogen Fuel Cell Technologies Nowadays  

Science Conference Proceedings (OSTI)

Recently, world has been confused by issues of energy resourcing, including fossil fuel use, global warming, and sustainable energy generation. Hydrogen may become the choice for future fuel of combustion engine. Hydrogen is an environmentally clean source of energy to end-users, particularly in transportation applications because without release of pollutants at the point of end use. Hydrogen may be produced from water using the process of electrolysis. One of the GEN-IV reactors nuclear projects (HTGRs, HTR, VHTR) is also can produce hydrogen from the process. In the present study, hydrogen gas production from nuclear power plant is reviewed in relation to commercialization of hydrogen fuel cell technologies nowadays.

Yusibani, Elin [Research Center for Hydrogen Industrial Use and Storage, AIST (Japan); Department of Physics, Universitas Syiah Kuala (Indonesia); Kamil, Insan; Suud, Zaki [Department of Physics, Institut Teknologi Bandung (Indonesia)

2010-06-22T23:59:59.000Z

456

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

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

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

457

Oil and Gas Environmental Review and Approval Processes (New Brunswick,  

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

Oil and Gas Environmental Review and Approval Processes (New Oil and Gas Environmental Review and Approval Processes (New Brunswick, Canada) Oil and Gas Environmental Review and Approval Processes (New Brunswick, Canada) < Back Eligibility Commercial Developer Fuel Distributor Industrial Investor-Owned Utility Municipal/Public Utility Utility Program Info State New Jersey Program Type Environmental Regulations Provider New Brunswick Natural Resources Oil and natural gas companies engaged in exploration, development and production in New Brunswick will be required by the Department of Environment to undergo a Phased Environmental Impact Assessment (EIA) process. The process will identify potential environmental impacts at the early stages before a project is implemented so that negative environmental impacts can be avoided.

458

Humidification Processes in Gas Turbine Cycles.  

E-Print Network (OSTI)

??The global climate change caused by emissions of greenhouse gases from combustion processes has been recognized as a continuously growing problem and much research focuses… (more)

Thern, Marcus

2005-01-01T23:59:59.000Z

459

Optimum Heat Power Cycles for Process Industrial Plants  

E-Print Network (OSTI)

Electric power cogeneration is compared with direct mechanical drives emphasizing the technical aspects having the greatest impact on energy economics. Both steam and gas turbine applications are discussed and practical methods of developing existing systems for maximum effectiveness are explained. Specific plant cases are cited as examples of major dollar savings opportunities.

Waterland, A. F.

1982-01-01T23:59:59.000Z

460

Novel cost allocation framework for natural gas processes: methodology and application to plan economic optimization  

E-Print Network (OSTI)

Natural gas plants can have multiple owners for raw natural gas streams and processing facilities as well as for multiple products. Therefore, a proper cost allocation method is necessary for taxation of the profits from natural gas and crude oil as well as for cost sharing among gas producers. However, cost allocation methods most often used in accounting, such as the sales value method and the physical units method, may produce unacceptable or even illogical results when applied to natural gas processes. Wright and Hall (1998) proposed a new approach called the design benefit method (DBM), based upon engineering principles, and Wright et al. (2001) illustrated the potential of the DBM for reliable cost allocation for natural gas processes by applying it to a natural gas process. In the present research, a rigorous modeling technique for the DBM has been developed based upon a Taylor series approximation. Also, we have investigated a cost allocation framework that determines the virtual flows, models the equipment, and evaluates cost allocation for applying the design benefit method to other scenarios, particularly those found in the petroleum and gas industries. By implementing these individual procedures on a computer, the proposed framework easily can be developed as a software package, and its application can be extended to large-scale processes. To implement the proposed cost allocation framework, we have investigated an optimization methodology specifically geared toward economic optimization problems encountered in natural gas plants. Optimization framework can provide co-producers who share raw natural gas streams and processing plants not only with optimal operating conditions but also with valuable information that can help evaluate their contracts. This information can be a reasonable source for deciding new contracts for co-producers. For the optimization framework, we have developed a genetic-quadratic search algorithm (GQSA) consisting of a general genetic algorithm and a quadratic search that is a suitable technique for solving optimization problems including process flowsheet optimization. The GQSA inherits the advantages of both genetic algorithms and quadratic search techniques, and it can find the global optimum with high probability for discontinuous as well as non-convex optimization problems much faster than general genetic algorithms.

Jang, Won-Hyouk

2005-05-01T23:59:59.000Z

Note: This page contains sample records for the topic "gas processing plants" 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

Process of producing combustible gas and for carbonizing coal  

SciTech Connect

This patent describes a process of producing combustible gas by supporting a column of fuel in a shaft furnace, intermittently blasting a combustion-supporting gas transversely through a mid portion of said column to produce a mid zone of sufficiently high temperature to decompose steam. The steam then circulated upwardly through said column between said blasting operations.

Doherty, H.L.

1922-08-15T23:59:59.000Z

462

Process for producing dimethyl ether form synthesis gas  

DOE Green Energy (OSTI)

This invention pertains to a Fischer Tropsch process for converting synthesis gas to an oxygenated hydrocarbon with particular emphasis on dimethyl ether. Synthesis gas comprising carbon monoxide and hydrogen are converted to dimethyl ether by carrying out the reaction in the presence of an alkali metal-manganese-iron carbonyl cluster incorporated onto a zirconia-alumina support.

Pierantozzi, Ronald (Macungie, PA)

1985-01-01T23:59:59.000Z

463

Process for producing dimethyl ether from synthesis gas  

DOE Patents (OSTI)

This invention pertains to a Fischer Tropsch process for converting synthesis gas to an oxygenated hydrocarbon with particular emphasis on dimethyl ether. Synthesis gas comprising carbon monoxide and hydrogen are converted to dimethyl ether by carrying out the reaction in the presence of an alkali metal-manganese-iron carbonyl cluster incorporated onto a zirconia-alumina support.

Pierantozzi, R.

1985-06-04T23:59:59.000Z

464

Sorbent Activation Process for Mercury Control: Field Testing at the Ameren Meredosia Power Plant  

Science Conference Proceedings (OSTI)

The Electric Power Research Institute (EPRI) and the Illinois State Geological Survey have developed and patented a technology for the on-site production of activated carbon (AC). The basic approach of the sorbent activation process (SAP) is to use coal from the plant site to form AC for direct injection into flue gas upstream of the particulate control device for mercury adsorption. The SAP process is designed to help significantly reduce the cost of AC for power plant mercury control. This report summa...

2009-12-03T23:59:59.000Z

465

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During precommissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Membrane Technology and Research, Inc. (MTR) has started to negotiate a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with their Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry.

Dr. Andre Da Costa

2003-04-10T23:59:59.000Z

466

FIELD DEMONSTRATION OF A MEMBRANE PROCESS TO SEPARATE NITROGEN FROM NATURAL GAS  

Science Conference Proceedings (OSTI)

The original proposal described the construction and operation of a 1 MMscfd treatment system to be operated at a Butcher Energy gas field in Ohio. The gas produced at this field contained 17% nitrogen. During precommissioning of the project, a series of well tests showed that the amount of gas in the field was significantly smaller than expected and that the nitrogen content of the wells was very high (25 to 30%). After evaluating the revised cost of the project, Butcher Energy decided that the plant would not be economical and withdrew from the project. Membrane Technology and Research, Inc. (MTR) continued to negotiate a marketing and sales partnership with ABB Lummus Global, a large multinational corporation. MTR will be working with their Randall Gas Technology group, a supplier of equipment and processing technology to the natural gas industry.

Dr. Andre Da Costa

2003-04-10T23:59:59.000Z

467

Effects of microbial processes on gas generation under expected WIPP repository conditions: Annual report through 1992  

Science Conference Proceedings (OSTI)

Microbial processes involved in gas generation from degradation of the organic constituents of transuranic waste under conditions expected at the Waste Isolation Pilot Plant (WIPP) repository are being investigated at Brookhaven National Laboratory. These laboratory studies are part of the Sandia National Laboratories -- WIPP Gas Generation Program. Gas generation due to microbial degradation of representative cellulosic waste was investigated in short-term ( 6 months) experiments by incubating representative paper (filter paper, paper towels, and tissue) in WIPP brine under initially aerobic (air) and anaerobic (nitrogen) conditions. Samples from the WIPP surficial environment and underground workings harbor gas-producing halophilic microorganisms, the activities of which were studied in short-term experiments. The microorganisms metabolized a variety of organic compounds including cellulose under aerobic, anaerobic, and denitrifying conditions. In long-term experiments, the effects of added nutrients (trace amounts of ammonium nitrate, phosphate, and yeast extract), no nutrients, and nutrients plus excess nitrate on gas production from cellulose degradation.

Francis, A.J.; Gillow, J.B.

1993-09-01T23:59:59.000Z

468

Small-Scale, Biomass-Fired Gas Turbine Plants Suitable for Distributed and Mobile Power Generation  

Science Conference Proceedings (OSTI)

This study evaluated the cost-effectiveness of small-scale, biomass-fired gas turbine plants that use an indirectly-fired gas turbine cycle. Such plants were originally thought to have several advantages for distributed generation, including portability. However, detailed analysis of two designs revealed several problems that would have to be resolved to make the plants feasible and also determined that a steam turbine cycle with the same net output was more economic than the gas turbine cycle. The incre...

2007-01-19T23:59:59.000Z

469

Investigation of Flue Gas Desulfurization Chemical Process Problems  

Science Conference Proceedings (OSTI)

An understanding of flue gas desulfurization process chemistry is crucial in troubleshooting problems in operating FGD systems. This report discusses a variety of problems and solutions associated with process chemistry for 25 different wet FGD systems, including lime/limestone and double alkali processes. Among the problems addressed are SO2 removal, mist eliminator scaling, poor solids dewatering, and water management.

1990-09-10T23:59:59.000Z

470

Permeation: A new competitive process for offshore gas dehydration  

SciTech Connect

Usual process for gas dehydration implement absorption (glycol chemical process) or adsorption (molecular sieves). The new dehydration process as described in this paper will be a strong competitor with these usual processes, especially for offshore applications, due to its simplicity and space and weight saving. This new membrane based process is discussed along major constraints of the application, suitable characteristics of the adapted permeation membranes and gain versus conventional gylcol in offshore application.

Fournie, F.; Agostini, J.P.

1984-05-01T23:59:59.000Z

471

Portfolio-Based Planning Process for Greenhouse Gas Mitigation | Department  

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

Portfolio-Based Planning Process for Greenhouse Gas Mitigation Portfolio-Based Planning Process for Greenhouse Gas Mitigation Portfolio-Based Planning Process for Greenhouse Gas Mitigation October 7, 2013 - 10:10am Addthis The portfolio-based planning process for greenhouse gas (GHG) mitigation offers an approach to: Evaluating the GHG reduction potential at the site, program, and agency level Identifying strategies for reducing those emissions Prioritizing activities to achieve both GHG reduction and cost objectives. Portfolio-based management for GHG mitigation helps agencies move from "peanut-butter-spreading" obligations for meeting GHG reduction targets evenly across all agency operating units to strategic planning of GHG reduction activities based on each operating unit's potential and cost to reduce emissions. The result of this prioritization will lay the foundation

472

Texas--RRC District 4 Onshore Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 4 Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

473

Texas--RRC District 5 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 5 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

474

Texas--RRC District 2 Onshore Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 2 Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

475

Texas--RRC District 1 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 1 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

476

Texas--RRC District 3 Onshore Natural Gas Plant Liquids, Proved...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 3 Onshore Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3...

477

Texas--RRC District 8A Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 8A Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

478

Texas--RRC District 7B Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 7B Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

479

Texas--RRC District 7C Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 7C Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

480

Texas--RRC District 6 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 6 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

Note: This page contains sample records for the topic "gas processing plants" 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

Texas--RRC District 10 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 10 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

482

Texas--RRC District 9 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 9 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

483

Texas--RRC District 8 Natural Gas Plant Liquids, Proved Reserves...  

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

Plant Liquids, Proved Reserves (Million Barrels) Texas--RRC District 8 Natural Gas Plant Liquids, Proved Reserves (Million Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5...

484

Title: Net Energy Ratio and Greenhouse Gas Analysis of a Biogas Power Plant  

E-Print Network (OSTI)

of a Biogas Power Plant Author: W. Bauer Author Affiliation: Department and greenhouse gas analysis for a 1.45 MW (0.71 MW electrical) biogas power plant

Bauer, Wolfgang

485

PERFORMANCE OF THE TBP PROCESS FOR ALUMINUM FUELS IDAHO CHEMICAL PROCESSING PLANT, 1955-1956  

SciTech Connect

Observations of the performance of the Idaho Chemical Processing Plant as modified for continuous dissolution and TBP lst cycle extraction, as to process chemistry and process engineering are reported for the initial plantscale full-irradiation-level operating run. As-operated flowsheets, the results of plant scale tests of the continuous dissolver, and fission prcduct decontamination data are emphasized. (auth)

Rohde, K.L.

1958-01-30T23:59:59.000Z

486

U.S. Natural Gas Plant Liquids, Proved Reserves (Million Barrels...  

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

W Withheld to avoid disclosure of individual company data. Release Date: 812013 Next Release Date: 812014 Referring Pages: Natural Gas Plant Liquids Proved Reserves...

487

Co-Removal of Mercury from Coal-Fired Power Plant Flue Gas with...  

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

combustion conditions, and air pollution control devices upstream of a power plant FGD system have an impact on the types and concentration of flue gas mercury at the...

488

Second law analysis of a natural gas-fired steam boiler and cogeneration plant.  

E-Print Network (OSTI)

??A second law thermodynamic analysis of a natural gas-fired steam boiler and cogeneration plant at Rice University was conducted. The analysis included many components of… (more)

Conklin, Eric D

2010-01-01T23:59:59.000Z

489

,"Texas--RRC District 1 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 1 Natural Gas Plant Liquids, Proved Reserves (Million...

490

,"Texas--RRC District 8 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 8 Natural Gas Plant Liquids, Proved Reserves (Million...

491

,"Texas--RRC District 5 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 5 Natural Gas Plant Liquids, Proved Reserves (Million...

492

,"Texas--RRC District 6 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 6 Natural Gas Plant Liquids, Proved Reserves (Million...

493

,"Texas--RRC District 7B Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 7B Natural Gas Plant Liquids, Proved Reserves (Million...

494

,"Texas--RRC District 2 Onshore Natural Gas Plant Liquids, Proved...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 2 Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

495

,"Texas--RRC District 9 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 9 Natural Gas Plant Liquids, Proved Reserves (Million...

496

,"Texas--RRC District 8A Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 8A Natural Gas Plant Liquids, Proved Reserves (Million...

497

,"Texas--RRC District 3 Onshore Natural Gas Plant Liquids, Proved...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 3 Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

498

,"Texas--RRC District 4 Onshore Natural Gas Plant Liquids, Proved...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 4 Onshore Natural Gas Plant Liquids, Proved Reserves (Million...

499

,"Texas--RRC District 7C Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 7C Natural Gas Plant Liquids, Proved Reserves (Million...

500

,"Texas--RRC District 10 Natural Gas Plant Liquids, Proved Reserves...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Texas--RRC District 10 Natural Gas Plant Liquids, Proved Reserves (Million...