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Note: This page contains sample records for the topic "liquefied refinery gases" 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

Refinery Yield of Liquefied Refinery Gases  

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

Refinery Yield Refinery Yield (Percent) Product: Liquefied Refinery Gases Finished Motor Gasoline Finished Aviation Gasoline Kerosene-Type Jet Fuel Kerosene Distillate Fuel Oil Residual Fuel Oil Naphtha for Petrochemical Feedstock Use Other Oils for Petrochemical Feedstock Use Special Naphthas Lubricants Waxes Petroleum Coke Asphalt and Road Oil Still Gas Miscellaneous Products Processing Gain(-) or Loss(+) 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. 5.3 5.4 5.2 5.2 5.1 3.9 1993-2013 PADD 1 4.4 5.1 4.9 4.9 4.6 2.1 1993-2013 East Coast 4.4 5.3 5.1 5.1 4.9 2.2 1993-2013

2

Extraction of uranium from spent fuels using liquefied gases  

SciTech Connect (OSTI)

For reprocessing of spent nuclear fuels, a novel method to extract actinides from spent fuel using highly compressed gases, nitrogen dioxide and carbon dioxide was proposed. As a fundamental study, the nitrate conversion with liquefied nitrogen dioxide and the nitrate extraction with supercritical carbon dioxide were demonstrated by using uranium dioxide powder, uranyl nitrate and tri-n-butylphosphate complex in the present study. (authors)

Sawada, Kayo; Hirabayashi, Daisuke; Enokida, Youichi [EcoTopia Science Institute, Nagoya University, Furo-cho, Chikusa-ku, Nagoya, 464-8603 (Japan)

2007-07-01T23:59:59.000Z

3

Factors affecting the recovery of petroleum in projects involving the injection of liquefied petroleum gases (LPG)  

E-Print Network [OSTI]

FACTORS AFFECTING THE RECOVERY OF PETROLEUM IN PROJECTS INVOLVING THE INJECTION OF LIQUEFIED PETROLEUM GASES (LPG) A Thesis By GERRY A. GRAHAM Submitted to the Graduate School of the Agricultural and Mechanical College of Texas in partial... fulfillment of the requirements for the degree of MASTER OF SCIENCE August, 1961 Major Subject: Petroleum Engineering GERRY A. GRAHAM FACTORS AFFECTING THE RECOVERY OF PETROLEUM IN PROJECTS INVOLVING THE INJECTION OF LIQUEFIED PETROLEUM GASES (LPG) A...

Graham, Gerry A

2012-06-07T23:59:59.000Z

4

U.S. Refinery and Blender Net Production  

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

18,146 17,882 18,452 18,673 18,564 19,106 1983-2013 Liquefied Refinery Gases 630 623 659 619 630 623 1984-2013 EthaneEthylene 18 19 20 20 18 7 1985-2013 Ethane 13 14 14 14 13 7...

5

Refinery & Blenders Net Input of Crude Oil  

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

Input Input Product: Total Crude Oil & Petroleum Products Crude Oil Natural Gas Plant Liquids and Liquefied Refinery Gases Pentanes Plus Liquefied Petroleum Gases Ethane Normal Butane Isobutane Other Liquids Hydrogen/Oxygenates/Renewables/Other Hydrocarbons Hydrogen Oxygenates (excl. Fuel Ethanol) Methyl Tertiary Butyl Ether (MTBE) All Other Oxygenates Renewable Fuels (incl. Fuel Ethanol) Fuel Ethanol Renewable Diesel Fuel Other Renewable Fuels Other Hydrocarbons Unfinished Oils (net) Unfinished Oils, Naphthas and Lighter Unfinished Oils, Kerosene and Light Gas Oils Unfinished Oils, Heavy Gas Oils Residuum Motor Gasoline Blending Components (MGBC) (net) MGBC - Reformulated MGBC - Reformulated - RBOB MGBC - Reformulated, RBOB for Blending w/ Alcohol MGBC - Reformulated, RBOB for Blending w/ Ether MGBC - Reformulated, GTAB MGBC - Conventional MGBC - CBOB MGBC - Conventional, GTAB MGBC - Other Conventional Aviation Gasoline Blending Components (net) Period-Unit: Monthly-Thousand Barrels Monthly-Thousand Barrels per Day Annual-Thousand Barrels Annual-Thousand Barrels per Day

6

U.S. Refinery & Blender Net Input  

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

Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History Total 526,996 566,851 559,032 581,600 578,456 543,388 1981-2013 Crude Oil 445,937 474,296 474,991 497,241 489,887 468,825 1981-2013 Natural Gas Plant Liquids and Liquefied Refinery Gases 12,805 11,759 12,769 13,227 13,760 16,794 1981-2013 Pentanes Plus 4,949 4,341 4,752 4,734 5,331 5,666 1981-2013 Liquefied Petroleum Gases 7,856 7,418 8,017 8,493 8,429 11,128 1981-2013 Ethane 1981-1992 Normal Butane 2,668 1,880 1,998 2,014 2,083 4,711 1981-2013 Isobutane 5,188 5,538 6,019 6,479 6,346 6,417 1981-2013 Other Liquids 68,254 80,796 71,272 71,132 74,809 57,769 1981-2013 Hydrogen/Oxygenates/Renewables/ Other Hydrocarbons 32,667 34,665 34,097 35,446 36,356 33,881 1981-2013

7

U.S. Refinery & Blender Net Input  

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

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History Total 6,204,500 6,277,893 6,169,893 6,345,372 6,422,710 6,406,693 1981-2012 Crude Oil 5,532,097 5,361,287 5,232,656 5,374,094 5,404,347 5,489,516 1981-2012 Natural Gas Plant Liquids and Liquefied Refinery Gases 184,383 177,559 177,194 161,479 178,884 186,270 1981-2012 Pentanes Plus 64,603 55,497 59,100 56,686 63,385 63,596 1981-2012 Liquefied Petroleum Gases 119,780 122,062 118,094 104,793 115,499 122,674 1981-2012 Ethane 1981-1992 Normal Butane 48,292 50,024 48,509 43,802 47,571 52,246 1981-2012 Isobutane 71,488 72,038 69,585 60,991 67,928 70,428 1981-2012 Other Liquids 488,020 739,047 760,043 809,799 839,479 730,907 1981-2012 Hydrogen/Oxygenates/Renewables/ Other Hydrocarbons

8

U.S. Refinery Yield  

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

Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History Liquefied Refinery Gases 5.3 5.4 5.2 5.2 5.1 3.9 1993-2013 Finished Motor Gasoline 44.4 44.1 44.4 43.9 43.9 44.9 1993-2013 Finished Aviation Gasoline 0.1 0.1 0.1 0.1 0.1 0.1 1993-2013 Kerosene-Type Jet Fuel 10.0 9.1 9.3 9.4 9.8 9.6 1993-2013 Kerosene 0.0 0.1 0.1 0.1 0.0 0.0 1993-2013 Distillate Fuel Oil 28.4 29.4 28.7 29.2 29.3 29.7 1993-2013 Residual Fuel Oil 3.3 2.9 2.8 2.8 2.5 2.6 1993-2013 Naphtha for Petrochemical Feedstock Use 1.4 1.5 1.5 1.6 1.5 1.5 1993-2013 Other Oils for Petrochemical Feedstock Use 0.6 0.6 0.7 0.7 0.6 0.7 1993-2013 Special Naphthas 0.3 0.3 0.3 0.2 0.3 0.2 1993-2013 Lubricants 0.9 1.1 1.1 1.1 1.1 1.1 1993-2013 Waxes

9

U.S. Refinery Yield  

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

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History Liquefied Refinery Gases 4.1 4.1 4.1 4.3 4.0 4.1 1993-2012 Finished Motor Gasoline 45.5 44.2 46.1 45.7 44.9 45.0 1993-2012 Finished Aviation Gasoline 0.1 0.1 0.1 0.1 0.1 0.1 1993-2012 Kerosene-Type Jet Fuel 9.1 9.7 9.3 9.3 9.4 9.5 1993-2012 Kerosene 0.2 0.1 0.1 0.1 0.1 0.1 1993-2012 Distillate Fuel Oil 26.1 27.8 26.9 27.5 28.9 29.1 1993-2012 Residual Fuel Oil 4.2 4.0 4.0 3.8 3.4 3.2 1993-2012 Naphtha for Petrochemical Feedstock Use 1.3 1.0 1.3 1.4 1.3 1.3 1993-2012 Other Oils for Petrochemical Feedstock Use 1.3 1.2 0.8 0.8 0.7 0.6 1993-2012 Special Naphthas 0.3 0.3 0.2 0.2 0.2 0.3 1993-2012 Lubricants 1.1 1.1 1.0 1.1 1.1 1.0 1993-2012 Waxes 0.1 0.1 0.1 0.1 0.1 0.1 1993-2012

10

U.S. Refinery Net Production  

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

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History Total 5,383,494 5,119,100 4,676,865 4,568,301 4,484,600 4,395,128 2005-2012 Liquefied Refinery Gases 238,904 230,431 227,470 240,454 225,992 230,413 2005-2012 Ethane/Ethylene 7,323 6,671 7,069 7,228 7,148 6,597 2005-2012 Ethane 5,145 4,608 5,229 5,200 5,105 4,835 2005-2012 Ethylene 2,178 2,063 1,840 2,028 2,043 1,762 2005-2012 Propane/Propylene 205,179 190,020 196,011 204,223 201,492 202,309 2005-2012 Propane 120,596 114,268 106,177 102,913 98,508 100,933 2005-2012 Propylene 84,583 75,752 89,834 101,310 102,984 101,376 2005-2012 Normal Butane/Butylene 24,285 30,887 24,148 30,281 17,449 20,580 2005-2012 Normal Butane 25,715 33,092 25,825 32,094 19,263 22,965 2005-2012

11

TABLE17.CHP:Corel VENTURA  

Gasoline and Diesel Fuel Update (EIA)

7. Refinery Net Production of Finished Petroleum Products by PAD and Refining Districts, January 1998 Liquefied Refinery Gases ... 576 -7...

12

Refinery Capacity Report  

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

Report --- Full report in PDF (1 MB) XLS --- Refinery Capacity Data by individual refinery as of January 1, 2006 Tables 1 Number and Capacity of Operable Petroleum...

13

Refinery & Blender Net Production of Total Finished Petroleum Products  

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

& Blender Net Production & Blender Net Production Product: Total Finished Petroleum Products Liquefied Refinery Gases Ethane/Ethylene Ethane Ethylene Propane/Propylene Propane Propylene Normal Butane/Butylene Normal Butane Butylene Isobutane/Isobutylene Isobutane Isobutylene Finished Motor Gasoline Reformulated Gasoline Reformulated Blended w/ Fuel Ethanol Reformulated Other Gasoline Conventional Gasoline Conventional Blended w/ Fuel Ethanol Conventional Blended w/ Fuel Ethanol, Ed55 and Lower Conventional Blended w/ Fuel Ethanol, Greater than Ed55 Conventional Other Finished Aviation Gasoline Kerosene-Type Jet Fuel Kerosene Distillate Fuel Oil Distillate F.O., 15 ppm Sulfur and under Distillate F.O., Greater than 15 ppm to 500 ppm Sulfur Distillate F.O., Greater than 500 ppm Sulfur Residual Fuel Oil Residual Fuel Less Than 0.31 Percent Sulfur Residual Fuel 0.31 to 1.00 Percent Sulfur Residual Fuel Greater Than 1.00 Percent Sulfur Petrochemical Feedstocks Naphtha For Petro. Feed. Use Other Oils For Petro. Feed. Use Special Naphthas Lubricants Waxes Petroleum Coke Marketable Petroleum Coke Catalyst Petroleum Coke Asphalt and Road Oil Still Gas Miscellaneous Products Processing Gain(-) or Loss(+) Period-Unit: Monthly-Thousand Barrels Monthly-Thousand Barrels per Day Annual-Thousand Barrels Annual-Thousand Barrels per Day

14

U.S. Refinery and Blender Net Production  

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

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History Total 6,567,929 6,641,293 6,527,069 6,735,067 6,815,590 6,794,407 1981-2012 Liquefied Refinery Gases 238,904 230,431 227,470 240,454 225,992 230,413 1981-2012 Ethane/Ethylene 7,323 6,671 7,069 7,228 7,148 6,597 1981-2012 Ethane 5,145 4,608 5,229 5,200 5,105 4,835 1993-2012 Ethylene 2,178 2,063 1,840 2,028 2,043 1,762 1993-2012 Propane/Propylene 205,179 190,020 196,011 204,223 201,492 202,309 1981-2012 Propane 120,596 114,268 106,177 102,913 98,508 100,933 1995-2012 Propylene 84,583 75,752 89,834 101,310 102,984 101,376 1993-2012 Normal Butane/Butylene 24,285 30,887 24,148 30,281 17,449 20,580 1981-2012 Normal Butane 25,715 33,092 25,825 32,094 19,263 22,965 1993-2012

15

U.S. Refinery and Blender Net Production  

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

Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History Total 559,639 599,643 591,916 616,905 613,451 578,101 1981-2013 Liquefied Refinery Gases 24,599 26,928 25,443 26,819 25,951 19,023 1981-2013 Ethane/Ethylene 464 426 407 441 487 379 1981-2013 Ethane 317 277 283 312 332 232 1993-2013 Ethylene 147 149 124 129 155 147 1993-2013 Propane/Propylene 16,840 17,792 16,966 17,839 18,063 17,254 1981-2013 Propane 8,051 8,949 8,756 9,002 9,153 8,816 1995-2013 Propylene 8,789 8,843 8,210 8,837 8,910 8,438 1993-2013 Normal Butane/Butylene 7,270 8,876 8,122 8,676 7,664 1,738 1981-2013 Normal Butane 7,447 9,044 8,314 8,832 8,067 1,743 1993-2013 Butylene -177 -168 -192 -156 -403 -5 1993-2013 Isobutane/Isobutylene

16

Gas Separation Membrane Use in the Refinery and Petrochemical Industries  

E-Print Network [OSTI]

Membranes have gained commercial acceptance as proven methods to recover valuable gases from waste gas streams. This paper explores ways in which gas separation membranes are used in the refinery and petrochemical industries to recover and purify...

Vari, J.

17

Refinery Capacity Report  

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

Refinery Capacity Report Refinery Capacity Report With Data as of January 1, 2013 | Release Date: June 21, 2013 | Next Release Date: June 20, 2014 Previous Issues Year: 2013 2012 2011 2010 2009 2008 2007 2006 2005 2004 2003 2002 2001 2000 1999 1997 1995 1994 Go Data series include fuel, electricity, and steam purchased for consumption at the refinery; refinery receipts of crude oil by method of transportation; and current and projected atmospheric crude oil distillation, downstream charge, and production capacities. Respondents are operators of all operating and idle petroleum refineries (including new refineries under construction) and refineries shut down during the previous year, located in the 50 States, the District of Columbia, Puerto Rico, the Virgin Islands, Guam, and other U.S. possessions.

18

Magnetic liquefier for hydrogen  

SciTech Connect (OSTI)

This document summarizes work done at the Astronautics Technology Center of the Astronautics Corporation of America (ACA) in Phase 1 of a four phase program leading to the development of a magnetic liquefier for hydrogen. The project involves the design, fabrication, installation, and operation of a hydrogen liquefier providing significantly reduced capital and operating costs, compared to present liquefiers. To achieve this goal, magnetic refrigeration, a recently developed, highly efficient refrigeration technology, will be used for the liquefaction process. Phase 1 project tasks included liquefier conceptual design and analysis, preliminary design of promising configurations, design selection, and detailed design of the selected design. Fabrication drawings and vendor specifications for the selected design were completed during detailed design. The design of a subscale, demonstration magnetic hydrogen liquefier represents a significant advance in liquefaction technology. The cost reductions that can be realized in hydrogen liquefaction in both the subscale and, more importantly, in the full-scale device are expected to have considerable impact on the use of liquid hydrogen in transportation, chemical, and electronic industries. The benefits to the nation from this technological advance will continue to have importance well into the 21st century.

NONE

1992-12-31T23:59:59.000Z

19

U.S. Refinery  

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

Crude Oil and Petroleum Products Crude Oil and Petroleum Products 354,918 353,802 345,413 343,062 345,025 342,763 1993-2013 Crude Oil 98,082 97,563 90,880 93,075 97,586 90,778 1981-2013 All Oils (Excluding Crude Oil) 256,836 256,239 254,533 249,987 247,439 251,985 1993-2013 Pentanes Plus 947 867 828 805 708 856 1993-2013 Liquefied Petroleum Gases 12,896 14,096 15,761 16,662 18,296 18,683 1993-2013 Ethane/Ethylene 281 321 261 242 205 171 1993-2013 Propane/Propylene 2,692 2,994 3,569 3,518 4,099 4,104 1993-2013 Normal Butane/Butylene 7,627 8,451 9,511 10,757 11,921 12,147 1993-2013 Isobutane/Butylene 2,296 2,330 2,420 2,145 2,071 2,261 1993-2013 Other Hydrocarbons 19 43 49 33 26 21 2009-2013 Oxygenates (excluding Fuel Ethanol) 116 99 100 82 71 78 2009-2013

20

U.S. Refinery  

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

Crude Oil and Petroleum Products Crude Oil and Petroleum Products 346,915 338,782 331,615 339,907 336,327 341,211 1993-2012 Crude Oil 89,070 86,598 90,944 88,982 90,640 88,781 1981-2012 All Oils (Excluding Crude Oil) 257,845 252,184 240,671 250,925 245,687 252,430 1993-2012 Pentanes Plus 949 997 1,006 971 895 884 1993-2012 Liquefied Petroleum Gases 13,161 12,456 12,611 14,896 14,429 15,934 1993-2012 Ethane/Ethylene 31 185 118 220 223 214 1993-2012 Propane/Propylene 4,120 3,293 3,577 4,278 4,087 4,574 1993-2012 Normal Butane/Butylene 6,320 6,482 6,478 7,818 7,794 8,774 1993-2012 Isobutane/Butylene 2,690 2,496 2,438 2,580 2,325 2,372 1993-2012 Other Hydrocarbons 29 20 41 42 2009-2012 Oxygenates (excluding Fuel Ethanol) 47 24 58 112 2009-2012

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Refinery Outages: Fall 2014  

Reports and Publications (EIA)

This report examines refinery outages planned for Fall 2014 and the potential implications for available refinery capacity, petroleum product markets and supply of gasoline and middle distillate fuel oil (diesel, jet fuel, and heating oil). EIA believes that dissemination of such analyses can be beneficial to market participants who may otherwise be unable to access such information.

2014-01-01T23:59:59.000Z

22

TABLE29.CHP:Corel VENTURA  

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

9. Refinery Net Production of Finished Petroleum Products by PAD and Refining Districts, July 2004 Liquefied Refinery Gases ... 2,082 70...

23

Refinery Capacity Report  

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

Refinery Capacity Report Refinery Capacity Report June 2013 With Data as of January 1, 2013 Independent Statistics & Analysis www.eia.gov U.S. Department of Energy Washington, DC 20585 This report was prepared by the U.S. Energy Information Administration (EIA), the statistical and analytical agency within the U.S. Department of Energy. By law, EIA's data, analyses, and forecasts are independent of approval by any other officer or employee of the United States Government. The views in this report therefore should not be construed as representing those of the Department of Energy or other Federal agencies. Table 1. Number and Capacity of Operable Petroleum Refineries by PAD District and State as of January 1, 2013

24

Alternative Fuels Data Center: Liquefied Gas Tax  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Gas Tax to Liquefied Gas Tax to someone by E-mail Share Alternative Fuels Data Center: Liquefied Gas Tax on Facebook Tweet about Alternative Fuels Data Center: Liquefied Gas Tax on Twitter Bookmark Alternative Fuels Data Center: Liquefied Gas Tax on Google Bookmark Alternative Fuels Data Center: Liquefied Gas Tax on Delicious Rank Alternative Fuels Data Center: Liquefied Gas Tax on Digg Find More places to share Alternative Fuels Data Center: Liquefied Gas Tax on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type Liquefied Gas Tax A use tax of $0.14 per gallon is imposed on liquefied gas used for operating motor vehicles on public highways in addition to a pre-paid annual vehicle tax according to the following: Maximum Gross Vehicle Weight Rating Tax

25

Liquefied Natural Gas Safety Research  

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

| May 2012 | May 2012 Liquefied Natural Gas (LNG) Safety Research | Page 1 Liquefied Natural Gas Safety Research Report to Congress May 2012 United States Department of Energy Washington, DC 20585 Department of Energy | May 2012 Liquefied Natural Gas (LNG) Safety Research | Page i Message from the Assistant Secretary for Fossil Energy The Explanatory Statement accompanying the Consolidated Appropriations Act, 2008 1 and the House Report on the House of Representatives version of the related bill 2 requested the Department of Energy to submit a report to Congress addressing several key liquefied natural gas (LNG) research priorities. These issues are identified in the February 2007 Government Accountability Office Report (GAO Report 07-316), Public Safety Consequences of a Terrorist

26

Liquefied Natural Gas: Understanding the Basic Facts | Department...  

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

Liquefied Natural Gas: Understanding the Basic Facts Liquefied Natural Gas: Understanding the Basic Facts Liquefied Natural Gas: Understanding the Basic Facts More Documents &...

27

Refinery Capacity Report  

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

1 1 Idle Operating Total Stream Day Barrels per Idle Operating Total Calendar Day Barrels per Atmospheric Crude Oil Distillation Capacity Idle Operating Total Operable Refineries Number of State and PAD District a b b 14 10 4 1,617,500 1,205,000 412,500 1,708,500 1,273,500 435,000 ............................................................................................................................................... PAD District I 1 0 1 182,200 0 182,200 190,200 0 190,200 ................................................................................................................................................................................................................................................................................................ Delaware......................................

28

Propane, Liquefied Petroleum Gas (LPG)  

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

Propane: Liquefied Petroleum Gas (LPG) Propane: Liquefied Petroleum Gas (LPG) Ford F-150 (Dual-Fuel LPG) Propane or liquefied petroleum gas (LPG) is a clean-burning fossil fuel that can be used to power internal combustion engines. LPG-fueled vehicles can produce significantly lower amounts of some harmful emissions and the greenhouse gas carbon dioxide (CO2). LPG is usually less expensive than gasoline, it can be used without degrading vehicle performance, and most LPG used in U.S. comes from domestic sources. The availability of LPG-fueled light-duty passenger vehicles is currently limited. A few light-duty vehicles-mostly larger trucks and vans-can be ordered from a dealer with a prep-ready engine package and converted to use propane. Existing conventional vehicles can also be converted for LPG use.

29

Case Study - Liquefied Natural Gas  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Environmental Environmental Science Enviro Express Kenworth LNG tractor. Connecticut Clean Cities Future Fuels Project Case Study - Liquefied Natural Gas As a part of the U.S. Department of Energy's broad effort to develop cleaner transportation technologies that reduce U.S. dependence on imported oil, this study examines advanced 2011 natural gas fueled trucks using liquefied natural gas (LNG) replacing older diesel fueled trucks. The trucks are used 6 days per week in regional city-to-landfill long hauls of incinerator waste with two fills per day. This is a workable fit for the limited range LNG trucks. Reduction of fuel costs and harmful emissions relative to the replaced trucks are significant. Introduction The American Recovery and Reinvestment Act legislation

30

Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Petroleum Liquefied Petroleum Gas (Propane) License to someone by E-mail Share Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on Facebook Tweet about Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on Twitter Bookmark Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on Google Bookmark Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on Delicious Rank Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on Digg Find More places to share Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) License on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type Liquefied Petroleum Gas (Propane) License

31

Liquefied Natural Gas | Department of Energy  

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

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

32

Encon Motivation in European Refineries  

E-Print Network [OSTI]

One essential element in a successful energy conservation or Encon program is effective motivation of employees and organizations to conserve energy. Encon motivation in our European refineries is a continuing effort that requires utilization...

Gambera, S.; Lockett, W., Jr.

1982-01-01T23:59:59.000Z

33

A Louisiana Refinery Success Story  

E-Print Network [OSTI]

manager, operations manager and production manager. From 2004 through 2006, the team presented a series of ESG seminars at the refinery site. The numerous models demonstrated quantitative savings with 3- to 12-mo paybacks. For a complete SSI turnkey...

Kacsur, D.

34

The safe use of low temperature liquefied gases 1. Introduction  

E-Print Network [OSTI]

signs 6. Materials and equipment 6.1 Liquid nitrogen, argon, oxygen and carbon dioxide 6.2 Liquid helium nitrogen, oxygen, argon and carbon dioxide into vacuum insulated tanks and evaporators (VITs and Vl dioxide TABLE 1 Property Oxygen (O2) Nitrogen (N2) Argon (Ar) Helium (He) Carbon dioxide (CO2) Molecular

Martin, Ralph R.

35

Proposed Procedures for Liquefied Natural Gas Export Decisions...  

Office of Environmental Management (EM)

Proposed Procedures for Liquefied Natural Gas Export Decisions Proposed Procedures for Liquefied Natural Gas Export Decisions On August 15, 2014, the Department of Energy's (DOE)...

36

Energy Department Authorizes Freeport LNG to Export Liquefied...  

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

Freeport LNG to Export Liquefied Natural Gas Energy Department Authorizes Freeport LNG to Export Liquefied Natural Gas November 14, 2014 - 2:00pm Addthis News Media Contact...

37

EIS-0498: Magnolia Liquefied Natural Gas Project, Calcasieu Parish...  

Energy Savers [EERE]

Magnolia Liquefied Natural Gas Project, Calcasieu Parish, Louisiana EIS-0498: Magnolia Liquefied Natural Gas Project, Calcasieu Parish, Louisiana Summary The Federal Energy...

38

Price of Lake Charles, LA Liquefied Natural Gas Total Imports...  

Gasoline and Diesel Fuel Update (EIA)

Liquefied Natural Gas Total Imports (Dollars per Thousand Cubic Feet) Price of Lake Charles, LA Liquefied Natural Gas Total Imports (Dollars per Thousand Cubic Feet) Decade Year-0...

39

Kenai, AK Liquefied Natural Gas Exports to Russia (Dollars per...  

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

Kenai, AK Liquefied Natural Gas Exports to Russia (Dollars per Thousand Cubic Feet) Kenai, AK Liquefied Natural Gas Exports to Russia (Dollars per Thousand Cubic Feet) Decade...

40

Development of a thermoacoustic natural gas liquefier.  

SciTech Connect (OSTI)

Praxair, in conjunction with the Los Alamos National Laboratory, is developing a new technology, thermoacoustic heat engines and refrigerators, for liquefaction of natural gas. This is the only technology capable of producing refrigeration power at cryogenic temperatures with no moving parts. A prototype, with a projected natural gas liquefaction capacity of 500 gallons/day, has been built and tested. The power source is a natural gas burner. Systems will be developed with liquefaction capacities up to 10,000 to 20,000 gallons per day. The technology, the development project, accomplishments and applications are discussed. In February 2001 Praxair, Inc. purchased the acoustic heat engine and refrigeration development program from Chart Industries. Chart (formerly Cryenco, which Chart purchased in 1997) and Los Alamos had been working on the technology development program since 1994. The purchase included assets and intellectual property rights for thermoacoustically driven orifice pulse tube refrigerators (TADOPTR), a new and revolutionary Thermoacoustic Stirling Heat Engine (TASHE) technology, aspects of Orifice Pulse Tube Refrigeration (OPTR) and linear motor compressors as OPTR drivers. Praxair, in cooperation with Los Alamos National Laboratory (LANL), the licensor of the TADOPTR and TASHE patents, is continuing the development of TASHE-OPTR natural gas powered, natural gas liquefiers. The liquefaction of natural gas, which occurs at -161 C (-259 F) at atmospheric pressure, has previously required rather sophisticated refrigeration machinery. The 1990 TADOPTR invention by Drs. Greg Swift (LANL) and Ray Radebaugh (NIST) demonstrated the first technology to produce cryogenic refrigeration with no moving parts. Thermoacoustic engines and refrigerators use acoustic phenomena to produce refrigeration from heat. The basic driver and refrigerator consist of nothing more than helium-filled heat exchangers and pipes, made of common materials, without exacting tolerances. The liquefier development program is divided into two components: Thermoacoustically driven refrigerators and linear motor driven refrigerators (LOPTRs). LOPTR technology will, for the foreseeable future, be limited to natural gas liquefaction capacities on the order of hundreds of gallons per day. TASHE-OPTR technology is expected to achieve liquefaction capacities of tens of thousands of gallons per day. This paper will focus on the TASHE-OPTR technology because its natural gas liquefaction capacity has greater market opportunity. LOPTR development will be mentioned briefly. The thermoacoustically driven refrigerator development program is now in the process of demonstrating the technology at a capacity of about 500 gallon/day (gpd) i.e., approximately 42,000 standard cubic feet/day, which requires about 7 kW of refrigeration power. This capacity is big enough to illuminate the issues of large-scale acoustic liquefaction at reasonable cost and to demonstrate the liquefaction of about 70% of an input gas stream, while burning about 30%. Subsequent to this demonstration a system with a capacity of approximately 10{sup 6} standard cubic feet/day (scfd) = 10,000 gpd with a projected liquefaction rate of about 85% of the input gas stream will be developed. When commercialized, the TASHE-OPTRs will be a totally new type of heat-driven cryogenic refrigerator, with projected low manufacturing cost, high reliability, long life, and low maintenance. A TASHE-OPTR will be able to liquefy a broad range of gases, one of the most important being natural gas (NG). Potential NG applications range from distributed liquefaction of pipeline gas as fuel for heavy-duty fleet and long haul vehicles to large-scale liquefaction at on-shore and offshore gas wellheads. An alternative to the thermoacoustic driver, but with many similar technical and market advantages, is the linear motor compressor. Linear motors convert electrical power directly into oscillating linear, or axial, motion. Attachment of a piston to the oscillator results in a direct drive compressor. Such a compressor

Wollan, J. J. (John J.); Swift, G. W. (Gregory W.); Backhaus, S. N. (Scott N.); Gardner, D. L. (David L.)

2002-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Motiva Refinery | Department of Energy  

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

Refinery Refinery Motiva Refinery May 18, 2006 - 10:45am Addthis Remarks Prepared for Energy Secretary Bodman Much of my time lately has been devoted to explaining why the price of gasoline has risen so sharply. President Bush understands the pinch this is creating for American consumers and has come forward with a variety of steps to address the problem. Rapid economic growth in emerging economies like China and India-and the growth here in the U.S.-have pushed up demand. Political unrest in some oil-producing regions has tightened supply. The transition from winter gasoline to summer blends, and the phase out of the additive MTBE in favor of ethanol, have increased the pressure on the market. Most significantly, we have very little spare refining capacity in this

42

Making Refinery Wastewater Clean | GE Global Research  

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

Making Refinery Wastewater Clean Making Refinery Wastewater Clean Lei Wang 2014.09.23 About four years ago, I visited Ordos, Inner Mongolia, to work on a project. When I arrived,...

43

Present and Future Alkylation Processes in Refineries  

Science Journals Connector (OSTI)

Present and Future Alkylation Processes in Refineries ... Second, an accident at a Texas refinery released considerable amounts of gaseous HF. ... In addition, following an accident, it is uncertain whether the sprays would still be operable. ...

Lyle F. Albright

2009-01-08T23:59:59.000Z

44

Integration of Nonlinear CDU Models in RefineryCDU Models in Refinery  

E-Print Network [OSTI]

planning models Optimizing refinery operation C d l ti Crude selection Maximizing profit; minimizing costIntegration of Nonlinear CDU Models in RefineryCDU Models in Refinery Planning Optimization Carnegie Mellon University EWO Meeting ­ March 2011 1 #12;I t d tiIntroduction Refinery production

Grossmann, Ignacio E.

45

Reformulated Gasoline Foreign Refinery Rules  

Gasoline and Diesel Fuel Update (EIA)

Reformulated Gasoline Reformulated Gasoline Foreign Refinery Rules Contents * Introduction o Table 1. History of Foreign Refiner Regulations * Foreign Refinery Baseline * Monitoring Imported Conventional Gasoline * Endnotes Related EIA Short-Term Forecast Analysis Products * Areas Participating in the Reformulated Gasoline Program * Environmental Regulations and Changes in Petroleum Refining Operations * Oxygenate Supply/Demand Balances in the Short-Term Integrated Forecasting Model * Refiners Switch to Reformulated Gasoline Complex Model * Demand, Supply, and Price Outlook for Reformulated Motor Gasoline, 1995 Introduction On August 27, 1997, the EPA promulgated revised the rules that allow foreign refiners to establish and use individual baselines, but it would not be mandatory (the optional use of an

46

Integration of light hydrocarbons cryogenic separation process in refinery based on LNG cold energy utilization  

Science Journals Connector (OSTI)

Abstract China depends on naphtha (derived from oil) as the main feedstock for ethylene plants, resulting in margins that are negatively co-related with the price of oil. Clearly, light hydrocarbons provide cost advantages over the conventional naphtha feedstock. Consequently, the recovery of light hydrocarbons from refinery gas has been gathering more and more significance. Nonetheless, the cryogenic separation needs low process temperatures, substantially increasing the refrigeration load requirements and, attendantly, the compression requirements associated with the refrigeration system. In this paper, the cold energy of liquefied natural gas (LNG) is applied to light hydrocarbons cryogenic separation process to replace the compression refrigeration system on the basis of one China refinery. The results show that LNG can provide 14,373 kW cold energy for the separation process, resulting in a direct compression power saving of 7973 kW and making the utilization rate of LNG cold energy as high as 71.9%.

Yajun Li; Hao Luo

2014-01-01T23:59:59.000Z

47

Liquefied Natural Gas (Iowa) | Department of Energy  

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

Liquefied Natural Gas (Iowa) Liquefied Natural Gas (Iowa) Liquefied Natural Gas (Iowa) < Back Eligibility Agricultural Commercial Construction Fed. Government Fuel Distributor General Public/Consumer Industrial Installer/Contractor Institutional Investor-Owned Utility Local Government Low-Income Residential Multi-Family Residential Municipal/Public Utility Nonprofit Residential Retail Supplier Rural Electric Cooperative Schools State/Provincial Govt Systems Integrator Transportation Tribal Government Utility Savings Category Alternative Fuel Vehicles Hydrogen & Fuel Cells Program Info State Iowa Program Type Environmental Regulations Provider Iowa Department of Public Safety This document adopts the standards promulgated by the National Fire Protection Association as rules for the transportation, storage, handling,

48

liquefied natural gas LNG | OpenEI  

Open Energy Info (EERE)

liquefied natural gas LNG liquefied natural gas LNG Dataset Summary Description Alternative fueling stations are located throughout the United States and their availability continues to grow. The Alternative Fuels Data Center (AFDC) maintains a website where you can find alternative fuels stations near you or on a route, obtain counts of alternative fuels stations by state, Source Alternative Fuels Data Center Date Released December 13th, 2010 (4 years ago) Date Updated December 13th, 2010 (4 years ago) Keywords alt fuel alternative fuels alternative fuels stations biodiesel CNG compressed natural gas E85 Electricity ethanol hydrogen liquefied natural gas LNG liquefied petroleum gas LPG propane station locations Data text/csv icon alt_fuel_stations_apr_4_2012.csv (csv, 2.3 MiB) Quality Metrics

49

U.S. Fuel Consumed at Refineries  

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

Barrels, Except Where Noted) Barrels, Except Where Noted) Area: U.S. East Coast (PADD 1) Midwest (PADD 2) Gulf Coast (PADD 3) Rocky Mountain (PADD 4) West Coast (PADD 5) Period: Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Product Area 2007 2008 2009 2010 2011 2012 View History Crude Oil 0 0 0 0 0 0 1986-2012 Liquefied Petroleum Gases 2,663 2,930 2,866 2,404 1,291 1,521 1986-2012 Distillate Fuel Oil 420 472 339 440 483 539 1986-2012 Residual Fuel Oil 1,844 1,390 1,249 980 759 540 1986-2012 Still Gas 247,106 237,161 220,191 219,890 217,716 220,094 1986-2012 Petroleum Coke 88,015 81,811 82,516 82,971 84,053 85,190 1986-2012 Marketable Petroleum Coke

50

Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Natural Gas Liquefied Natural Gas (LNG) Measurement to someone by E-mail Share Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on Facebook Tweet about Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on Twitter Bookmark Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on Google Bookmark Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on Delicious Rank Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on Digg Find More places to share Alternative Fuels Data Center: Liquefied Natural Gas (LNG) Measurement on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type Liquefied Natural Gas (LNG) Measurement LNG is taxed based on the gasoline gallon equivalent, or 6.6 pounds of LNG

51

Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Natural Gas Liquefied Natural Gas Powers Trucks in Connecticut to someone by E-mail Share Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on Facebook Tweet about Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on Twitter Bookmark Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on Google Bookmark Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on Delicious Rank Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on Digg Find More places to share Alternative Fuels Data Center: Liquefied Natural Gas Powers Trucks in Connecticut on AddThis.com... June 4, 2011 Liquefied Natural Gas Powers Trucks in Connecticut

52

Opportunities for Biorenewables in Petroleum Refineries  

SciTech Connect (OSTI)

a summary of our collaborative 2005 project “Opportunities for Biorenewables in Petroleum Refineries” at the Rio Oil and Gas Conference this September.

Holmgren, Jennifer; Arena, Blaise; Marinangelli, Richard; McCall, Michael; Marker, Terry; Petri, John; Czernik, Stefan; Elliott, Douglas C.; Shonnard, David

2006-10-11T23:59:59.000Z

53

Refinery Production Planning: Multiperiod MINLP with Nonlinear CDU  

E-Print Network [OSTI]

as integrated planning and scheduling refinery operation models are recognized as key 1 Refinery Production Planning: Multiperiod MINLP with Nonlinear CDU Model-Rivera (2011) developed a single-period, nonlinear programing refinery planning model

Grossmann, Ignacio E.

54

EPA's Liquefied Natural Gas Regulatory Roadmap  

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

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

55

Sabine Pass, LA Exports to Brazil Liquefied Natural Gas (Million...  

Gasoline and Diesel Fuel Update (EIA)

Brazil Liquefied Natural Gas (Million Cubic Feet) Sabine Pass, LA Exports to Brazil Liquefied Natural Gas (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec...

56

,"U.S. Liquefied Natural Gas Imports From Egypt (MMcf)"  

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

2015 1:00:03 PM" "Back to Contents","Data 1: U.S. Liquefied Natural Gas Imports From Egypt (MMcf)" "Sourcekey","N9103EG2" "Date","U.S. Liquefied Natural Gas Imports From Egypt...

57

Gulf LNG, Mississippi Liquefied Natural Gas Imports (Million...  

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

Liquefied Natural Gas Imports (Million Cubic Feet) Gulf LNG, Mississippi Liquefied Natural Gas Imports (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

58

Global Liquefied Natural Gas Market: Status and Outlook, The  

Reports and Publications (EIA)

The Global Liquefied Natural Gas Market: Status & Outlook was undertaken to characterize the global liquefied natural gas (LNG) market and to examine recent trends and future prospects in the LNG market.

2003-01-01T23:59:59.000Z

59

Energy Department Approves Gulf Coast Exports of Liquefied Natural...  

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

Approves Gulf Coast Exports of Liquefied Natural Gas Energy Department Approves Gulf Coast Exports of Liquefied Natural Gas May 20, 2011 - 1:00pm Addthis Washington, DC - The U.S....

60

3 , LNG (Liquefied Natural Gas) -165oC  

E-Print Network [OSTI]

, , . . . , . , LNG (Liquefied Natural Gas) -165oC , . (Piped Natural Gas, PNG) , , . PNG, LNG ( 2-3 ), . (Natural Gas Hydrate, NGH) / . -20oC / . Natural Gas Hydrate (NGH) Liquefied Natural Gas (LNG) Modes of Transport and Storage

Hong, Deog Ki

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Petroleum Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity to someone by E-mail Share Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on Facebook Tweet about Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on Twitter Bookmark Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on Google Bookmark Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on Delicious Rank Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on Digg Find More places to share Alternative Fuels Data Center: Liquefied Petroleum Gas (Propane) and Natural Gas Liability Immunity on

62

Sabine Pass, LA Exports to Japan Liquefied Natural Gas (Million...  

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

Japan Liquefied Natural Gas (Million Cubic Feet) Sabine Pass, LA Exports to Japan Liquefied Natural Gas (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

63

Freeport, TX Exports to japan Liquefied Natural Gas (Million...  

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

japan Liquefied Natural Gas (Million Cubic Feet) Freeport, TX Exports to japan Liquefied Natural Gas (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

64

Energy Department Authorizes Jordan Cove to Export Liquefied Natural Gas  

Broader source: Energy.gov [DOE]

Terminal in Coos Bay, Oregon Authorized to Export Liquefied Natural Gas to Non-Free Trade Agreement Countries

65

U.S. Refinery Net Input  

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

Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History Total 320,455 348,984 346,918 365,525 358,673 335,185 2005-2013 Crude Oil 445,937 474,296 474,991 497,241 489,887 468,825 2005-2013 Natural Gas Plant Liquids 11,914 11,407 12,393 13,031 13,377 15,397 2005-2013 Pentanes Plus 4,688 4,040 4,439 4,667 5,044 5,273 2005-2013 Liquefied Petroleum Gases 7,226 7,367 7,954 8,364 8,333 10,124 2005-2013 Normal Butane 2,038 1,829 1,935 1,885 1,987 3,707 2005-2013 Isobutane 5,188 5,538 6,019 6,479 6,346 6,417 2005-2013 Other Liquids -137,396 -136,719 -140,466 -144,747 -144,591 -149,037 2005-2013 Hydrogen/Oxygenates/Renewables/ Other Hydrocarbons 7,511 8,089 7,844 8,541 8,568 8,086 2005-2013 Hydrogen 5,792 6,200 6,050 6,477 6,520 6,226 2009-2013

66

Regional Refinery Utilization Shows Gulf Coast Pressure  

Gasoline and Diesel Fuel Update (EIA)

5 5 Notes: But there is some room for hope. Refineries generally begin maintenance in February or March, and finish in April. The East Coast was experiencing some lengthy refinery maintenance outages, as shown by the drop in utilization that remained low in most of March and April. In the meantime, the East Coast was drawing on extra supplies from the Gulf Coast and imports. The Midwest refineries seem to have been ramping up in April as they finished what maintenance was needed. But the Midwest no longer has the Blue Island refinery, so it also is pulling more product from the Gulf Coast. The high Gulf Coast prices this spring reflect extra "pull" on product from both the Midwest and the East Coast, and probably from California as well. Inputs into Gulf Coast refineries over the last 4 weeks

67

Refinery burner simulation design architecture summary.  

SciTech Connect (OSTI)

This report describes the architectural design for a high fidelity simulation of a refinery and refinery burner, including demonstrations of impacts to the refinery if errors occur during the refinery process. The refinery burner model and simulation are a part of the capabilities within the Sandia National Laboratories Virtual Control System Environment (VCSE). Three components comprise the simulation: HMIs developed with commercial SCADA software, a PLC controller, and visualization software. All of these components run on different machines. This design, documented after the simulation development, incorporates aspects not traditionally seen in an architectural design, but that were utilized in this particular demonstration development. Key to the success of this model development and presented in this report are the concepts of the multiple aspects of model design and development that must be considered to capture the necessary model representation fidelity of the physical systems.

Pollock, Guylaine M.; McDonald, Michael James; Halbgewachs, Ronald D.

2011-10-01T23:59:59.000Z

68

Total Number of Operable Refineries  

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

Data Series: Total Number of Operable Refineries Number of Operating Refineries Number of Idle Refineries Atmospheric Crude Oil Distillation Operable Capacity (B/CD) Atmospheric Crude Oil Distillation Operating Capacity (B/CD) Atmospheric Crude Oil Distillation Idle Capacity (B/CD) Atmospheric Crude Oil Distillation Operable Capacity (B/SD) Atmospheric Crude Oil Distillation Operating Capacity (B/SD) Atmospheric Crude Oil Distillation Idle Capacity (B/SD) Vacuum Distillation Downstream Charge Capacity (B/SD) Thermal Cracking Downstream Charge Capacity (B/SD) Thermal Cracking Total Coking Downstream Charge Capacity (B/SD) Thermal Cracking Delayed Coking Downstream Charge Capacity (B/SD Thermal Cracking Fluid Coking Downstream Charge Capacity (B/SD) Thermal Cracking Visbreaking Downstream Charge Capacity (B/SD) Thermal Cracking Other/Gas Oil Charge Capacity (B/SD) Catalytic Cracking Fresh Feed Charge Capacity (B/SD) Catalytic Cracking Recycle Charge Capacity (B/SD) Catalytic Hydro-Cracking Charge Capacity (B/SD) Catalytic Hydro-Cracking Distillate Charge Capacity (B/SD) Catalytic Hydro-Cracking Gas Oil Charge Capacity (B/SD) Catalytic Hydro-Cracking Residual Charge Capacity (B/SD) Catalytic Reforming Charge Capacity (B/SD) Catalytic Reforming Low Pressure Charge Capacity (B/SD) Catalytic Reforming High Pressure Charge Capacity (B/SD) Catalytic Hydrotreating/Desulfurization Charge Capacity (B/SD) Catalytic Hydrotreating Naphtha/Reformer Feed Charge Cap (B/SD) Catalytic Hydrotreating Gasoline Charge Capacity (B/SD) Catalytic Hydrotreating Heavy Gas Oil Charge Capacity (B/SD) Catalytic Hydrotreating Distillate Charge Capacity (B/SD) Catalytic Hydrotreating Kerosene/Jet Fuel Charge Capacity (B/SD) Catalytic Hydrotreating Diesel Fuel Charge Capacity (B/SD) Catalytic Hydrotreating Other Distillate Charge Capacity (B/SD) Catalytic Hydrotreating Residual/Other Charge Capacity (B/SD) Catalytic Hydrotreating Residual Charge Capacity (B/SD) Catalytic Hydrotreating Other Oils Charge Capacity (B/SD) Fuels Solvent Deasphalting Charge Capacity (B/SD) Catalytic Reforming Downstream Charge Capacity (B/CD) Total Coking Downstream Charge Capacity (B/CD) Catalytic Cracking Fresh Feed Downstream Charge Capacity (B/CD) Catalytic Hydro-Cracking Downstream Charge Capacity (B/CD) Period:

69

Total Refinery Net Input of Crude Oil and Petroleum Products  

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

Input Input Product: Total Crude Oil & Petroleum Products Crude Oil Natural Gas Plant Liquids Pentanes Plus Liquefied Petroleum Gases Normal Butane Isobutane Other Liquids Hydrogen/Oxygenates/Renewables/Other Hydrocarbons Hydrogen Oxygenates (excl. Fuel Ethanol) Methyl Tertiary Butyl Ether (MTBE) All Other Oxygenates Renewable Fuels (incl. Fuel Ethanol) Fuel Ethanol Renewable Diesel Fuel Other Renewable Fuels Other Hydrocarbons Unfinished Oils (net) Unfinished Oils, Naphthas and Lighter Unfinished Oils, Kerosene and Light Gas Oils Unfinished Oils, Heavy Gas Oils Residuum Motor Gasoline Blending Components (MGBC) (net) MGBC - Reformulated MGBC - Reformulated - RBOB MGBC - Reformulated, RBOB for Blending w/ Alcohol MGBC - Reformulated, RBOB for Blending w/ Ether MGBC - Conventional MGBC - CBOB MGBC - Conventional, GTAB MGBC - Other Conventional Aviation Gasoline Blending Components (net) Alaskan Crude Oil Receipts Period-Unit: Monthly-Thousand Barrels Monthly-Thousand Barrels per Day Annual-Thousand Barrels Annual-Thousand Barrels per Day

70

From the Woods to the Refinery  

Broader source: Energy.gov [DOE]

Breakout Session 2D—Building Market Confidence and Understanding II: Carbon Accounting and Woody Biofuels From the Woods to the Refinery Stephen S. Kelley, Principal and Department Head, Department of Forest Biomaterials, North Carolina State University

71

Refinery siting workbook: appendices A and B  

SciTech Connect (OSTI)

The objective of this effort is to develop and provide basic refinery-related information for use by state and local government officials as a basis for establishing responsible refinery siting requirements and policies consistent with the federal clean air and water standards and socio-economic concerns. The report will be organized into two volumes. The main text comprises the basic topics of physical concerns, regulatory requirements, and permitting activities, while the second volume includes the detailed appendix materials such as the applicable laws, and the necessary permits, as available and a glossary of pertinent terms. As a means to this objective, three refinery sizes, 200,000, 100,000 and 30,000 barrels per day crude charge will be discussed in technical terms. Process unit configuration will be presented which will maximize either gasoline or heating oil production with either sweet or sour crude oil feedstocks. The major issues affecting the socio-economic impact of siting the refinery in a given locale will be presented. These data will review the factors affecting the human environment and the issues that must be addressed to assess the impact that a refinery will have on a community. The key federal registrations which impact upon a refinery siting decision shall be reviewed. Summaries of these regulations and a simplified decision diagram for the air and water acts shall be presented to assist both government and refinery officials in understanding the scope of regulatory impact. All pertinent procedures required for refinery permitting shall be reviewed under the generalized headings of air, water, health and safety, land use, and miscellaneous permits. This categorization at the federal, state and local levels of government shall be used as a basis for establishing degrees of emphasis.

Not Available

1980-07-01T23:59:59.000Z

72

Mathematical modeling of a Fermilab helium liquefier coldbox  

SciTech Connect (OSTI)

Fermilab Central Helium Liquefier (CHL) facility is operated 24 hours-a-day to supply 4.6{degrees}K for the Fermilab Tevatron superconducting proton-antiproton collider Ring and to recover warm return gases. The centerpieces of the CHL are two independent cold boxes rated at 4000 and 5400 liters/hour with LN{sub 2} precool. These coldboxes are Claude cycle and have identical heat exchangers trains, but different turbo-expanders. The Tevatron cryogenics demand for higher helium supply from CHL was the driving force to investigate an installation of an expansion engine in place of the Joule-Thompson valve. A mathematical model was developed to describe the thermo- and gas-dynamic processes for the equipment included in the helium coldbox. The model is based on a finite element approach, opposite to a global variables approach, thus providing for higher accuracy and conversion stability. Though the coefficients used in thermo- and gas-dynamic equations are unique for a given coldbox, the general approach, the equations, the methods of computations, and most of the subroutines written in FORTRAN can be readily applied to different coldboxes. The simulation results are compared against actual operating data to demonstrate applicability of the model.

Geynisman, M.G.; Walker, R.J.

1995-12-01T23:59:59.000Z

73

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

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

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

74

Increased olefins production via recovery of refinery gas hydrocarbons  

SciTech Connect (OSTI)

In the process of catalytically cracking heavy petroleum fractions to make gasoline and light fuel oil, by-product waste gases are also generated. The waste gases, normally used as fuel, are themselves rich sources of ethylene, propylene and other light hydrocarbons which can be recovered inexpensively via a cryogenic dephlegmator process. This gas separation technique is exploited in a system, in operation since spring of 1987, which reclaims C/sub 2/+ hydrocarbons from a refinery gas. The reclamation process bolsters production in a nearby ethylene plant. Causing no disruption of ethylene plant operations, the cryogenic hydrocarbon recovery system functions smoothly with existing systems. The dephlegmation unit operation melds distillation and heat transfer processes in a single easily-controlled step which boosts the hydrocarbon purity and recovery above the levels profitably achievable with conventional cryogenic separation techniques. Very attractive operating economics follow from high purity, high recovery, and high energy efficiency. This paper discusses process concepts, economic benefits, plant operation, and early performance results.

Bernhard, D.P.; Rowles, H.C.; Moss, J.A.; Pickering, J.L. Jr.

1988-01-01T23:59:59.000Z

75

,"U.S. Refinery Crude Oil Input Qualities"  

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

Sulfur Content (Weighted Average) of Crude Oil Input to Refineries (Percent)","U.S. API Gravity (Weighted Average) of Crude Oil Input to Refineries (Degrees)" 31062,0.88,32.64...

76

,"U.S. Refinery Crude Oil Input Qualities"  

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

Sulfur Content (Weighted Average) of Crude Oil Input to Refineries (Percent)","U.S. API Gravity (Weighted Average) of Crude Oil Input to Refineries (Degrees)" 31228,0.91,32.46...

77

Steam System Management Program Yields Fuel Savings for Refinery  

E-Print Network [OSTI]

The Phillips refinery at Borger, Texas, determined the need to develop a utility monitoring system. Shortly after this commitment was made, the refinery was introduced to a flowsheet modeling program that could be used to model and optimize steam...

Gaines, L. D.; Hagan, K. J.

1983-01-01T23:59:59.000Z

78

The Department of Energy's Role in Liquefied Natural Gas Export  

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

The Department of Energy's Role in Liquefied Natural Gas Export The Department of Energy's Role in Liquefied Natural Gas Export Applications The Department of Energy's Role in Liquefied Natural Gas Export Applications November 8, 2011 - 11:34am Addthis Statement of Christopher Smith, Deputy Assistant Secretary for Oil and Natural Gas, Office of Fossil Energy before the Senate Committee on Energy and Natural Resources on DOE's Role in Liquefied Natural Gas Export Applications. Thank you Chairman Bingaman, Ranking Member Murkowski, and members of the Committee; I appreciate the opportunity to be here today to discuss the Department of Energy's (DOE) program regulating the export of natural gas, including liquefied natural gas (LNG). DOE's Statutory Authority DOE's authority to regulate the export of natural gas arises under

79

Clean Cities Moving Fleets Forward with Liquefied Natural Gas | Department  

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

Clean Cities Moving Fleets Forward with Liquefied Natural Gas Clean Cities Moving Fleets Forward with Liquefied Natural Gas Clean Cities Moving Fleets Forward with Liquefied Natural Gas May 30, 2013 - 2:52pm Addthis Waste hauler Enviro Express converted its fleet of heavy-duty trucks to run on liquefied natural gas (LNG) and built the first LNG station east of the Mississippi River with help from the Energy Department's Clean Cities initiative. | Photo courtesy of New Haven Clean Cities Coalition. Waste hauler Enviro Express converted its fleet of heavy-duty trucks to run on liquefied natural gas (LNG) and built the first LNG station east of the Mississippi River with help from the Energy Department's Clean Cities initiative. | Photo courtesy of New Haven Clean Cities Coalition. Shannon Brescher Shea Communications Manager, Clean Cities Program

80

DOE Initiates Series of Liquefied Natural Gas Public Education Forums |  

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

Series of Liquefied Natural Gas Public Education Series of Liquefied Natural Gas Public Education Forums DOE Initiates Series of Liquefied Natural Gas Public Education Forums February 15, 2006 - 11:52am Addthis First Forum Set in Boston, Massachusetts WASHINGTON, D.C. - The first in a series of Department of Energy (DOE)-sponsored public education forums on liquefied natural gas (LNG) has been scheduled for Friday, March 10, 2006, at the John B. Hynes Veterans Memorial Convention Center in Boston, Massachusetts. This series of forums aims to maintain open lines of communication between government officials and interested citizens, and is scheduled in compliance with the National Energy Policy Act of 2005, enacted by President Bush in August 2005. "The Department of Energy's Liquefied Natural Gas forums will initiate

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network [OSTI]

Refinery Technology Profiles: Gasification and SupportingGasification.to be carried out. 18.5 Gasification Gasification provides

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

82

Final Report - Development of New Pressure Swing Adsorption (PSA) Technology to Recover High Valued Products from Chemical Plant and Refinery Waste Systems  

SciTech Connect (OSTI)

Project Objective was to extend pressure swing adsorption (PSA) technology into previously under-exploited applications such as polyolefin production vent gas recovery and H2 recovery from refinery waste gases containing significant amounts of heavy hydrocarbons, aromatics, or H2S.

Keith Ludwig

2004-06-14T23:59:59.000Z

83

Fluor to expand Marathon's Detroit refinery  

Science Journals Connector (OSTI)

Fluor Corp will provide integrated engineering, procurement and construction (EPC) for Marathon Oil Corp's projected US$1.9 billion expansion and upgrade of the company's Detroit refinery. The US$1.6 billion EPC contract includes services, the value of procured materials and the construction contracts under Fluor's direct management.

2008-01-01T23:59:59.000Z

84

Integration of Nonlinear CDU Models in Refinery  

E-Print Network [OSTI]

Hydrotreatment Distillate blending Gas oil blending Cat Crack CDU Crude1, ... Crude2, .... butane Fuel gas Prem. Gasoline Reg. Gasoline Distillate Fuel Oil Treated Residuum SR Fuel gas SR Naphtha SR Gasoline SR Distillate SR GO SR Residuum Product Blending 4 #12;Planning Model Example Information Given Refinery

Grossmann, Ignacio E.

85

liquefied petroleum gas | OpenEI  

Open Energy Info (EERE)

3 3 Varnish cache server Browse Upload data GDR 429 Throttled (bot load) Error 429 Throttled (bot load) Throttled (bot load) Guru Meditation: XID: 2142288523 Varnish cache server liquefied petroleum gas Dataset Summary Description Alternative fueling stations are located throughout the United States and their availability continues to grow. The Alternative Fuels Data Center (AFDC) maintains a website where you can find alternative fuels stations near you or on a route, obtain counts of alternative fuels stations by state, Source Alternative Fuels Data Center Date Released December 13th, 2010 (4 years ago) Date Updated December 13th, 2010 (4 years ago) Keywords alt fuel alternative fuels alternative fuels stations biodiesel CNG compressed natural gas E85 Electricity ethanol

86

Refinery Stocks of Crude Oil and Petroleum Products  

Gasoline and Diesel Fuel Update (EIA)

Product: Crude Oil and Petroleum Products Crude Oil Petroleum Products Pentanes Plus Liquefied Petroleum Gases Ethane/Ethylene Propane/Propylene Normal Butane/Butylene Isobutane/Isobutylene Oxygenates/Renewables/Other Hydrocarbons Oxygenates (excl. Fuel Ethanol) Methyl Tertiary Butyl Ether (MTBE) All Other Oxygenates Renewable Fuels (incl. Fuel Ethanol) Fuel Ethanol Renewable Diesel Fuel Other Renewable Fuels Other Hydrocarbons Unfinished Oils Naphthas and Lighter Kerosene and Light Gas Oils Heavy Gas Oils Residuum Motor Gasoline Blending Components MGBC - Reformulated MGBC - Reformulated - RBOB MGBC - RBOB for Blending with Alcohol* MGBC - RBOB for Blending with Ether* MGBC - Conventional MGBC - Conventional CBOB MGBC - Conventional GTAB MGBC - Conventional Other Aviation Gasoline Blending Components Finished Motor Gasoline Reformulated Reformulated Blended with Fuel Ethanol Reformulated, Other Conventional Gasoline Conventional Gasoline Blended with Fuel Ethanol Conventional Gasoline Blended with Fuel Ethanol, Ed55 and Lower Conventional Other Gasoline Finished Aviation Gasoline Kerosene-Type Jet Fuel Kerosene Distillate Fuel Oil Distillate Fuel Oil, 15 ppm and Under Distillate Fuel Oil, Greater than 15 ppm to 500 ppm Distillate Fuel Oil, Greater than 500 ppm Residual Fuel Oil Less than 0.31 Percent Sulfur 0.31 to 1.00 Percent Sulfur Greater than 1.00 Percent Sulfur Petrochemical Feedstocks Naphtha for Petrochemical Feedstock Use Other Oils for Petrochemical Feedstock Use Special Naphthas Lubricants Waxes Petroleum Coke Marketable Coke Asphalt and Road Oil Miscellaneous Products Period-Units: Monthly-Thousand Barrels Annual-Thousand Barrels

87

U.S. Total Shell Storage Capacity at Operable Refineries  

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

Area: U.S. East Coast (PADD 1) Midwest (PADD 2) Gulf Coast (PADD 3) Rocky Mountain (PADD 4) West Coast (PADD 5) Period: Area: U.S. East Coast (PADD 1) Midwest (PADD 2) Gulf Coast (PADD 3) Rocky Mountain (PADD 4) West Coast (PADD 5) Period: Annual (as of January 1) Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Product Area 2008 2009 2010 2011 2012 2013 View History Total 765,593 758,619 710,413 -- -- -- 1982-2013 Crude Oil 180,830 179,471 180,846 -- -- -- 1985-2013 Liquefied Petroleum Gases 34,772 32,498 33,842 -- -- -- 1982-2013 Propane/Propylene 10,294 8,711 8,513 -- -- -- 1982-2013 Normal Butane/Butylene 24,478 23,787 25,329 -- -- -- 1982-2013 Other Liquids 95,540 96,973 96,157 -- -- -- 1982-2013 Oxygenates 1,336 1,028 1,005 -- -- -- 1994-2013

88

DOE's Program Regulating Liquefied Natural Gas Export Applications |  

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

Program Regulating Liquefied Natural Gas Export Applications Program Regulating Liquefied Natural Gas Export Applications DOE's Program Regulating Liquefied Natural Gas Export Applications March 19, 2013 - 2:52pm Addthis Statement of Christopher Smith, Acting Assistant Secretary for Fossil Energy before the House Committee on Oversight and Government Reform, Subcommittee on Energy Policy, Health Care, and Entitlements View the archived Congressional Hearing on YouTube Thank you Chairman Lankford, Ranking Member Speier, and members of the Committee; I appreciate the opportunity to be here today to discuss the Department of Energy's (DOE) program regulating the export of natural gas, including liquefied natural gas (LNG). Recent Developments in LNG Exports The boom in domestic shale gas provides unprecedented opportunities for the

89

Underground Storage of Natural Gas and Liquefied Petroleum Gas (Nebraska) |  

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

Underground Storage of Natural Gas and Liquefied Petroleum Gas Underground Storage of Natural Gas and Liquefied Petroleum Gas (Nebraska) Underground Storage of Natural Gas and Liquefied Petroleum Gas (Nebraska) < Back Eligibility Agricultural Commercial Construction Fed. Government Fuel Distributor General Public/Consumer Industrial Installer/Contractor Institutional Investor-Owned Utility Local Government Low-Income Residential Multi-Family Residential Municipal/Public Utility Nonprofit Residential Retail Supplier Rural Electric Cooperative Schools State/Provincial Govt Systems Integrator Transportation Tribal Government Utility Program Info State Nebraska Program Type Siting and Permitting Provider Nebraska Oil and Gas Conservation Commission This statute declares underground storage of natural gas and liquefied petroleum gas to be in the public interest if it promotes the conservation

90

Energy Department Approves Gulf Coast Exports of Liquefied Natural Gas |  

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

Approves Gulf Coast Exports of Liquefied Natural Approves Gulf Coast Exports of Liquefied Natural Gas Energy Department Approves Gulf Coast Exports of Liquefied Natural Gas May 20, 2011 - 12:00am Addthis Washington, D.C. - The U.S. Department of Energy today issued a conditional authorization approving an application to export liquefied natural gas (LNG) from the Sabine Pass LNG Terminal in Louisiana, paving the way for thousands of new construction and domestic natural gas production jobs in Louisiana, Texas, and several other states. Subject to final environmental and regulatory approval, Sabine Pass Liquefaction, LLC will retrofit an existing LNG import terminal in Louisiana so that it can also be used for exports. This is the first long-term authorization to export natural gas from the lower 48 states as LNG to all U.S. trading partners.

91

DOE's Program Regulating Liquefied Natural Gas Export Applications |  

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

DOE's Program Regulating Liquefied Natural Gas Export DOE's Program Regulating Liquefied Natural Gas Export Applications DOE's Program Regulating Liquefied Natural Gas Export Applications June 18, 2013 - 10:15am Addthis Statement of Christopher Smith, Acting Assistant Secretary for Fossil Energy before the House Committee on Energy and Commerce Subcommittees on Energy and Power. Thank you Chairman Whitfield, Ranking Member Rush, and members of the Subcommittee; I appreciate the opportunity to be here today to discuss the Department of Energy's (DOE) program regulating the export of natural gas, including liquefied natural gas (LNG). Recent Developments in LNG Exports The boom in domestic shale gas provides unprecedented opportunities for the United States. Over the last several years, domestic natural gas production

92

Freeport, TX Liquefied Natural Gas Exports to Brazil (Million...  

Gasoline and Diesel Fuel Update (EIA)

to Brazil (Million Cubic Feet) Freeport, TX Liquefied Natural Gas Exports to Brazil (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,581 2014 2,664...

93

Elba Island, GA Natural Gas Liquefied Natural Gas Imports from...  

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

Egypt (Million Cubic Feet) Elba Island, GA Natural Gas Liquefied Natural Gas Imports from Egypt (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 5,780...

94

Gulf LNG, Mississippi Liquefied Natural Gas Imports from Egypt...  

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

Egypt (Million Cubic Feet) Gulf LNG, Mississippi Liquefied Natural Gas Imports from Egypt (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,954 - ...

95

Cameron, LA Liquefied Natural Gas Imports from Egypt (Million...  

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

Egypt (Million Cubic Feet) Cameron, LA Liquefied Natural Gas Imports from Egypt (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,971 - No Data...

96

Freeport, TX Natural Gas Liquefied Natural Gas Imports from Egypt...  

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

Egypt (Million Cubic Feet) Freeport, TX Natural Gas Liquefied Natural Gas Imports from Egypt (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,969 -...

97

Gulf LNG, Mississippi Liquefied Natural Gas Imports from Trinidad...  

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

Trinidad and Tobago (Million Cubic Feet) Gulf LNG, Mississippi Liquefied Natural Gas Imports from Trinidad and Tobago (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep...

98

An economic analysis of Floating Liquefied Natural Gas (FLNG)  

E-Print Network [OSTI]

This report includes a discussion of the potential production of stranded natural gas reserves through the implementation of Floating Liquefied Natural Gas (FLNG) in a world of growing energy demand followed by an analysis ...

Marmolejo, Phillip Christian

2014-01-01T23:59:59.000Z

99

Effect of Increased Levels of Liquefied Natural Gas Exports on...  

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

Effect of Increased Levels of Liquefied Natural Gas Exports on U.S. Energy Markets October 2014 Independent Statistics & Analysis www.eia.gov U.S. Department of Energy Washington,...

100

Price Liquefied Sabine Pass, LA Natural Gas Exports Price to...  

Gasoline and Diesel Fuel Update (EIA)

Portugal (Dollars per Thousand Cubic Feet) Price Liquefied Sabine Pass, LA Natural Gas Exports Price to Portugal (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2...

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Port Huron, MI Liquefied Natural Gas Exports (Million Cubic Feet...  

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

(Million Cubic Feet) Port Huron, MI Liquefied Natural Gas Exports (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 1 2014 1 1 1 1 2 1 1 1 1 - No...

102

Port Huron, MI Liquefied Natural Gas Exports to Canada (Million...  

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

to Canada (Million Cubic Feet) Port Huron, MI Liquefied Natural Gas Exports to Canada (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 1 2014 1 1 1 1...

103

Promising technology for recovery and use of liquefied natural gas  

Science Journals Connector (OSTI)

Use of liquefied natural gas is proposed as an alternative to motor fuel. Technology for recovering liquid natural gas based on the principle of internal gas cooling in a turbo-expander, and the equipment require...

E. B. Fedorova; V. V. Fedorov; A. D. Shakhov

2009-03-01T23:59:59.000Z

104

Price Liquefied Sabine Pass, LA Natural Gas Exports Price to...  

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

Japan (Dollars per Thousand Cubic Feet) Price Liquefied Sabine Pass, LA Natural Gas Exports Price to Japan (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

105

Cameron, LA Liquefied Natural Gas Exports to Japan (Million Cubic...  

Gasoline and Diesel Fuel Update (EIA)

Japan (Million Cubic Feet) Cameron, LA Liquefied Natural Gas Exports to Japan (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,741 - No Data...

106

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

Gasoline and Diesel Fuel Update (EIA)

Japan (Dollars per Thousand Cubic Feet) Price Liquefied Freeport, TX Natural Gas Exports Price to Japan (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

107

Port Nikiski, AK Liquefied Natural Gas Exports to Japan (Dollars...  

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

Dollars per Thousand Cubic Feet) Port Nikiski, AK Liquefied Natural Gas Exports to Japan (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6...

108

Port Nikiski, AK Liquefied Natural Gas Exports to Japan (Million...  

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

Million Cubic Feet) Port Nikiski, AK Liquefied Natural Gas Exports to Japan (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1990's...

109

Naphthenic acid corrosion in the refinery  

SciTech Connect (OSTI)

Field tests and laboratory studies of refinery process streams are presented. The effects of temperature, velocity and physical state were studied with respect to alloy selection for corrosion resistant service. The amount of molybdenum in the austenitic stainless steel alloys is the dominant factor in conferring corrosion resistance. The Naphthenic Acid Corrosion Index (NACI) is useful in assessing the severity of corrosion under a variety of circumstances.

Craig, H.L. Jr. [Mobil Research and Development Corp., Paulsboro, NJ (United States)

1995-11-01T23:59:59.000Z

110

PAD District / Refinery Location Total Atmospheric Distillation  

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

Operable Date of Last Operation Date Shutdown Table 11. New, Shutdown and Reactivated Refineries During 2012 a b REACTIVATED PAD District I 185,000 366,700 Monroe Energy LLC Trainer, PA 185,000 366,700 09/12 c SHUTDOWN PAD District I 80,000 47,000 ChevronUSA Inc Perth Amboy, NJ 80,000 47,000 03/08 07/12 PAD District III 16,800 19,500 Western Refining Southwest Inc Bloomfield, NM 16,800 19,500 12/09 11/12 PAD District VI 500,000 1,086,000 Hovensa LLC Kingshill, VI 500,000 1,086,000 02/12 02/12 a b bbl/cd=Barrels per calendar day. bbl/sd=Barrels per stream day. Sources: Energy Information Administration (EIA) Form EIA-810, "Monthly Refinery Report" and Form EIA-820, "Annual Refinery Report." c Formerly owned by ConocoPhillips Company.

111

GreenHunter Biodiesel Refinery Grand Opening | Department of Energy  

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

GreenHunter Biodiesel Refinery Grand Opening GreenHunter Biodiesel Refinery Grand Opening GreenHunter Biodiesel Refinery Grand Opening June 2, 2008 - 12:51pm Addthis Remarks as Prepared for (Acting) Deputy Secretary Kupfer Today, Acting Deputy Secretary Jeffrey Kupfer delivered remarks at the launch of GreenHunter Energy's biodiesel refinery, which will be the nation's single largest biodiesel refinery, producing 105 million gallons of "white-water" B100 biodiesel per year. Thank you Gary. I'm pleased to join with Governor Perry, Congressmen Green and Lampson, and Mayor Garcia in celebrating this important occasion. Today, as we open the nation's largest biodiesel refinery, we reach another milestone in our effort to make America more energy secure. As you know, global energy demand is surging. We must act swiftly and aggressively to

112

Potential Impacts of Reductions in Refinery Activity on Northeast...  

Gasoline and Diesel Fuel Update (EIA)

serving Philadelphia-area refineries primarily handle crude oil and their docks and tanks are not equipped to offload waterborne products. Figure 1. Petroleum Product Assets in...

113

Fuel-Flexible Combustion System for Refinery and Chemical Plant...  

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

low-emission operation across a broad range of fuel compositions, including syngas, biogas, natural gas, and refinery fuel gas. Displacing Natural Gas Consumption and Lowering...

114

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network [OSTI]

refineries with specific energy and cost savings data whenoperations. Typically, energy and cost savings are around 5%the potential energy and cost-savings (Frangopoluos et al. ,

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

115

Projection and Reaction for Decision Support in Refineries: Combining Multiple Theories  

E-Print Network [OSTI]

system to provide decision support for refinery operations personnel (Krebsbach & Musliner 1997; Musliner) used to optimize control parameters during normal operations. Current Refinery Operations HumanProjection and Reaction for Decision Support in Refineries: Combining Multiple Theories Kurt D

Krebsbach, Kurt D.

116

Supply and Disposition of Crude Oil and Petroleum Products  

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

957 15 731 315 -382 -141 33 712 15 735 Crude Oil 614 - - - - 300 -139 -147 -15 638 4 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 342 0 21 11 -304 - - 14 19 9 29...

117

Supply and Disposition of Crude Oil and Petroleum Products  

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

848 14 646 310 -422 -51 0 622 15 707 Crude Oil 527 - - - - 296 -183 -57 3 578 2 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 320 0 11 11 -265 - - 1 17 12 48 Pentanes...

118

Naphthenic acid corrosion in refinery settings  

SciTech Connect (OSTI)

Naphthenic acid corrosion has been a problem in the refining industry for many years. Recently interest in this problem has grown because crudes that contain naphthenic acid are being recovered from areas which were not known to produce this type of crude, such as china, India, and Africa. New techniques for identifying naphthenic acid corrosion and chemical treatments for preventing this attack are presented. Refinery case studies include stream analysis, failure analysis, and inhibitor use. Laboratory tests to show the effect of hydrogen sulfide and phosphorus-based inhibitors are discussed.

Babaian-Kibala, E. (Nalco Chemical Co., Sugar Land, TX (United States)); Craig, H.L. Jr. (Mobil Research and Development Corp., Paulsboro, NJ (United States)); Rusk, G.L. (Mobil Oil Co., Torrance, CA (United States)); Blanchard, K.V.; Rose, T.J.; Uehlein, B.L. (Nalco Chemical Co., Paulsboro, NJ (United States)); Quinter, R.C. (Sun Co., Newtown Square, PA (United States)); Summers, M.A. (Sun Co., Marcus Hook, PA (United States))

1993-04-01T23:59:59.000Z

119

,"U.S. Refinery, Bulk Terminal, and Natural Gas Plant Stocks...  

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

Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)","U.S. Gasoline Blending Components Stocks at Refineries, Bulk Terminals, and Natural Gas Plants...

120

WIMP Dark Matter Direct-Detection Searches in Noble Gases  

E-Print Network [OSTI]

Cosmological observations and the dynamics of the Milky Way provide ample evidence for an invisible and dominant mass component. This so-called dark matter could be made of new, colour and charge neutral particles, which were non-relativistic when they decoupled from ordinary matter in the early universe. Such weakly interacting massive particles (WIMPs) are predicted to have a non-zero coupling to baryons and could be detected via their collisions with atomic nuclei in ultra-low background, deep underground detectors. Among these, detectors based on liquefied noble gases have demonstrated tremendous discovery potential over the last decade. After briefly introducing the phenomenology of direct dark matter detection, I will review the main properties of liquefied argon and xenon as WIMP targets and discuss sources of background. I will then describe existing and planned argon and xenon detectors that employ the so-called single- and dual-phase detection techniques, addressing their complementarity and science...

Baudis, Laura

2014-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

WIMP Dark Matter Direct-Detection Searches in Noble Gases  

E-Print Network [OSTI]

Cosmological observations and the dynamics of the Milky Way provide ample evidence for an invisible and dominant mass component. This so-called dark matter could be made of new, colour and charge neutral particles, which were non-relativistic when they decoupled from ordinary matter in the early universe. Such weakly interacting massive particles (WIMPs) are predicted to have a non-zero coupling to baryons and could be detected via their collisions with atomic nuclei in ultra-low background, deep underground detectors. Among these, detectors based on liquefied noble gases have demonstrated tremendous discovery potential over the last decade. After briefly introducing the phenomenology of direct dark matter detection, I will review the main properties of liquefied argon and xenon as WIMP targets and discuss sources of background. I will then describe existing and planned argon and xenon detectors that employ the so-called single- and dual-phase detection techniques, addressing their complementarity and science reach.

Laura Baudis

2014-08-19T23:59:59.000Z

122

Energy Department Authorizes Second Proposed Facility to Export Liquefied  

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

Second Proposed Facility to Export Second Proposed Facility to Export Liquefied Natural Gas Energy Department Authorizes Second Proposed Facility to Export Liquefied Natural Gas May 17, 2013 - 12:00pm Addthis News Media Contact (202) 586-4940 WASHINGTON - The Energy Department announced today that it has conditionally authorized Freeport LNG Expansion, L.P. and FLNG Liquefaction, LLC (Freeport) to export domestically produced liquefied natural gas (LNG) to countries that do not have a Free Trade Agreement (FTA) with the United States from the Freeport LNG Terminal on Quintana Island, Texas. Freeport previously received approval to export LNG from this facility to FTA countries on February 10, 2011. Subject to environmental review and final regulatory approval, the facility is conditionally authorized to export at a rate of up to 1.4 billion cubic

123

Energy Department Authorizes Third Proposed Facility to Export Liquefied  

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

Third Proposed Facility to Export Third Proposed Facility to Export Liquefied Natural Gas Energy Department Authorizes Third Proposed Facility to Export Liquefied Natural Gas August 7, 2013 - 12:00pm Addthis NEWS MEDIA CONTACT (202) 586-4940 WASHINGTON - The Energy Department announced today that it has conditionally authorized Lake Charles Exports, LLC (Lake Charles) to export domestically produced liquefied natural gas (LNG) to countries that do not have a Free Trade Agreement (FTA) with the United States from the Lake Charles Terminal in Lake Charles, Louisiana. Lake Charles previously received approval to export LNG from this facility to FTA countries on July 22, 2011. Subject to environmental review and final regulatory approval, the facility is conditionally authorized to export at a rate of up to 2.0

124

Price of Liquefied U.S. Natural Gas Re-Exports to Portugal (Dollars...  

Gasoline and Diesel Fuel Update (EIA)

Liquefied U.S. Natural Gas Re-Exports to Portugal (Dollars per Thousand Cubic Feet) Price of Liquefied U.S. Natural Gas Re-Exports to Portugal (Dollars per Thousand Cubic Feet)...

125

,"Liquefied U.S. Natural Gas Re-Exports to Russia (Million Cubic...  

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

2014 1:24:23 PM" "Back to Contents","Data 1: Liquefied U.S. Natural Gas Re-Exports to Russia (Million Cubic Feet)" "Sourcekey","NGMEPG0ERENUS-NRSMMCF" "Date","Liquefied U.S....

126

Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Liquefied Natural Gas Liquefied Natural Gas (LNG) and Propane Tax and User Permit to someone by E-mail Share Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on Facebook Tweet about Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on Twitter Bookmark Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on Google Bookmark Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on Delicious Rank Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on Digg Find More places to share Alternative Fuels Data Center: Liquefied Natural Gas (LNG) and Propane Tax and User Permit on AddThis.com...

127

Reformulated gasoline: Costs and refinery impacts  

SciTech Connect (OSTI)

Studies of reformulated gasoline (RFG) costs and refinery impacts have been performed with the Oak Ridge National Laboratory Refinery Yield Model (ORNL-RYM), a linear program which has been updated to blend gasolines to satisfy emissions constraints defined by preliminary complex emissions models. Policy makers may use the reformulation cost knee (the point at which costs start to rise sharply for incremental emissions control) to set emissions reduction targets, giving due consideration to the differences between model representations and actual refining operations. ORNL-RYM estimates that the reformulation cost knee for the US East Coast (PADD I) is about 15.2 cents per gallon with a 30 percent reduction of volatile organic compounds (VOCs). The estimated cost knee for the US Gulf Coast (PADD III) is about 5.5 cents per gallon with a VOC reduction of 35 percent. Reid vapor pressure (RVP) reduction is the dominant VOC reduction mechanism. Even with anti-dumping constraints, conventional gasoline appears to be an important sink which permits RFG to be blended with lower aromatics and sulfur contents in PADD III. In addition to the potentially large sensitivity of RFG production to different emissions models, RFG production is sensitive to the non-exhaust VOC share assumption for a particular VOC model. ORNL-RYM has also been used to estimate the sensitivity of RFG production to the cost of capital; to the RVP requirements for conventional gasoline; and to the percentage of RFG produced in a refining region.

Hadder, G.R.

1994-02-01T23:59:59.000Z

128

Energy Department Conditionally Authorizes Oregon LNG to Export Liquefied Natural Gas  

Broader source: Energy.gov [DOE]

Terminal in Warrenton, Oregon Authorized to Export Liquefied Natural Gas to Non-Free Trade Agreement Countries

129

Visual Simulation of Offshore Liquefied Natural Gas (LNG) Terminals  

E-Print Network [OSTI]

Visual Simulation of Offshore Liquefied Natural Gas (LNG) Terminals in a Decision-Making Context1, Berkeley. 3/ Liquified Natural Gas Act Stats, 1977, Chap. 855, Page 2506 (effective Sept. 17, 1977 potential offshore Liquified Natural Gas (LNG) sites and the types of terminals that might occupy those

Standiford, Richard B.

130

Effect of parasitic refrigeration on the efficiency of magnetic liquefiers  

SciTech Connect (OSTI)

Our studies have shown that magnetic refrigerators have the potential to liquefy cryogens very efficiently. High efficiency is especially important for liquid hydrogen and natural gas applications where the liquefaction costs are a significant fraction of the total liquid cost. One of the characteristics of magnetic refrigerators is the requirement for a high-field superconducting magnet. Providing a 4.2-K bath for this magnet will require a small amount of parasitic refrigeration at 4.2 K even though the rest of the liquefier may be at 110 K (liquid natural gas) or higher. For several different refrigeration power levels at 4.2 K, we have calculated the efficiency of the magnetic liquefier as a function of power, temperature and the 4.2-K refrigerator efficiency. The results show that if the ratio of the thermal load at 4.2 K to the main refrigerator power is 0.001 or less, the effect on the efficiency of the liquefier is negligible at all temperatures below room temperature provided the 4.2-K refrigerator efficiency is high.

Barclay, J.A.; Stewart, W.F.

1982-01-01T23:59:59.000Z

131

Otay Mesa, CA Liquefied Natural Gas Exports (Million Cubic Feet...  

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

(Million Cubic Feet) Otay Mesa, CA Liquefied Natural Gas Exports (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 8 7 7 5 3 5 2014 6 7 7 8 7 7 9 8 9 8...

132

Capturing, Purifying, and Liquefying Landfill Gas for Transportation Fuel  

E-Print Network [OSTI]

Capturing, Purifying, and Liquefying Landfill Gas for Transportation Fuel TRANSPORTATION ENERGY alternative fuel, and purified landfill gas could provide a renewable domestic source of it. Landfills from landfills and use it in natural gas applications such as fueling motor vehicles. Project

133

Kenai, AK Liquefied Natural Gas Exports to Japan (Million Cubic...  

Gasoline and Diesel Fuel Update (EIA)

Million Cubic Feet) Kenai, AK Liquefied Natural Gas Exports to Japan (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 1,856 1,908 1,915 1,913 1,915...

134

Summary of Market Assessment of Upcoming Planned Refinery Outages  

Gasoline and Diesel Fuel Update (EIA)

Summary of Market Assessment of Upcoming Planned Refinery Outages Summary of Market Assessment of Upcoming Planned Refinery Outages Summary of Market Assessment of Upcoming Planned Refinery Outages Market Assessment of Upcoming Planned Refinery Outages, December 2008 - March 2009 reviews planned U.S. refinery outages from December 2008 though March 2009 in order to identify any regions where outages might create enough supply pressure to impact prices significantly. As required under Section 804 of the Energy Independence and Security Act of 2007 (Pub. L. 110-140), this report reviews the supply implications of planned refinery outages for December 2008 through March 2009, which covers the winter period when demand for distillate fuels (diesel and heating oil) is high. As a result, emphasis in this report is on distillate rather than gasoline. Refinery outages are the result of planned maintenance and unplanned outages. Maintenance is usually scheduled during the times when demand is lowest - in the first quarter and again in the fall. Unplanned outages, which occur for many reasons including mechanical failures, fires, and flooding, can occur at any time.

135

Preliminary life-cycle assessment of biomass-derived refinery feedstocks for reducing CO{sub 2} emissions  

SciTech Connect (OSTI)

The US by ratification of the United Nations Framework Convention on Climate Change has pledged to emit no higher levels of greenhouse gases in the year 2000 than it did in 1990. Biomass-derived products have been touted as a possible solution to the potential problem of global warming. However, past studies related to the production of liquid fuels, chemicals, gaseous products, or electricity from biomass, have only considered the economics of producing these commodities. The environmental benefits have not been fully quantified and factored into these estimates until recently. Evaluating the environmental impact of various biomass systems has begun using life-cycle assessment. A refinery Linear Programming model previously developed has been modified to examine the effects of CO{sub 2}-capping on the US refining industry and the transportation sector as a whole. By incorporating the results of a CO{sub 2} emissions inventory into the model, the economic impact of emissions reduction strategies can be estimated. Thus, the degree to which global warming can be solved by supplementing fossil fuels with biomass-derived products can be measured, allowing research and development to be concentrated on the most environmentally and economically attractive technology mix. Biomass gasification to produce four different refinery feedstocks was considered in this analysis. These biomass-derived products include power, fuel gas, hydrogen for refinery processing, and Fischer-Tropsch liquids for upgrading and blending into finished transportation fuels.

Marano, J.J. [Burns and Roe Services Corp., Pittsburgh, PA (United States); Rogers, S. [Dept. of Energy, Pittsburgh, PA (United States); Spath, P.L.; Mann, M.K. [National Renewable Energy Lab., Golden, CO (United States)

1995-12-31T23:59:59.000Z

136

Motiva Enterprises Refinery Expansion Groundbreaking | Department of Energy  

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

Enterprises Refinery Expansion Groundbreaking Enterprises Refinery Expansion Groundbreaking Motiva Enterprises Refinery Expansion Groundbreaking December 10, 2007 - 4:44pm Addthis Remarks as Prepared for Secretary Bodman Thank you, Bill. It's good to see Congressman Poe, Rob Routs, Mr. Al-Khayyal and Mayor Prince here. Thank you all for inviting me to be part of this occasion. In 1901 Texas wildcatters struck oil near here at a place called Spindletop, setting off the Texas Oil Boom. Like the California Gold Rush some 50 years before, the Texas Oil Boom helped to build America. People moved across the country in search of prosperity. To achieve it, they needed to develop new technologies and build new infrastructure like the original parts of the Port Arthur refinery, which opened here in 1903. As America's need for energy expanded as our demand for oil and gas

137

Secretary Bodman Tours Refinery and Calls for More Domestic Refining  

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

Tours Refinery and Calls for More Domestic Tours Refinery and Calls for More Domestic Refining Capacity Secretary Bodman Tours Refinery and Calls for More Domestic Refining Capacity May 18, 2006 - 10:43am Addthis Highlights President Bush's Four-Point Plan to Combat High Energy Prices PORT ARTHUR, TX - Secretary of Energy Samuel W. Bodman today renewed the call for expanded oil refining capacity in the United States and discussed additional steps the Department of Energy (DOE) is taking to prepare for the upcoming hurricane season. Secretary Bodman made the statements after touring the Motiva Refinery in Port Arthur, Texas. "We need a more robust energy sector; and one way to do that is to strengthen and expand our domestic oil refining capacity. We're hopeful that Motiva will continue to work to expand their capacity to 600,000

138

Effective Fouling Minimization Increases the Efficiency and Productivity of Refineries  

Broader source: Energy.gov [DOE]

This factsheet details a project to improve operating procedures, including physical and chemical methods and the use of high-temperature coatings, to allow refineries to operate equipment below threshold fouling conditions and use the most effective minimization techniques.

139

Low Temperature Waste Energy Recovery at Chemical Plants and Refineries  

E-Print Network [OSTI]

Technologies to economically recover low-temperature waste energy in chemical plants and refineries are the holy grail of industrial energy efficiency. Low temperature waste energy streams were defined by the Texas Industries of the Future Chemical...

Ferland, K.; papar, R.; Quinn, J.; Kumar, S.

2013-01-01T23:59:59.000Z

140

EIS-0498: Magnolia Liquefied Natural Gas Project, Calcasieu Parish, Louisiana  

Broader source: Energy.gov [DOE]

The Federal Energy Regulatory Commission (FERC) is preparing an EIS for a proposal to build and operate a liquefied natural gas (LNG) facility on land at the Port of Lake Charles. DOE is a cooperating agency in preparing the EIS. DOE, Office of Fossil Energy, has an obligation under Section 3 of the Natural Gas Act to authorize the import and export of natural gas, including LNG, unless it finds that the import or export is not consistent with the public interest.

Note: This page contains sample records for the topic "liquefied refinery gases" 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

PAD District / Refinery Location Total Atmospheric Distillation  

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

of Last of Last Operation Date Shutdown Table 13. Refineries Permanently Shutdown By PAD District Between January 1, 1990 and January 1, 2013 PAD District I 542,450 GNC Energy Corp Greensboro, NC 3,000 0 a Primary Energy Corp Richmond, VA 6,100 0 a Saint Mary's Refining Co Saint Mary's, WV 4,000 4,480 02/93 03/93 Cibro Refining Albany, NY 41,850 27,000 07/93 09/93 Calumet Lubricants Co LP Rouseville, PA 12,800 26,820 03/00 06/00 Young Refining Corp. Douglasville, GA 5,400 0 07/04 07/04 Sunoco Inc Westville, NJ 145,000 263,000 11/09 02/10 Western Refining Yorktown Inc Yorktown, VA 66,300 182,600 09/10 12/11 Sunoco Inc Marcus Hook, PA 178,000 278,000 12/11 12/11 ChevronUSA Inc Perth Amboy, NJ 80,000 47,000 03/08 07/12 PAD District II 460,315 Coastal Refining & Mktg El Dorado, KS 0 20,000 b Intercoastal Energy Svcs

142

Separation of polar gases from nonpolar gases  

DOE Patents [OSTI]

Polar gases such as hydrogen sulfide, sulfur dioxide and ammonia may be separated from nonpolar gases such as methane, nitrogen, hydrogen or carbon dioxide by passing a mixture of polar and nonpolar gases over the face of a multicomponent membrane at separation conditions. The multicomponent membrane which is used to effect the separation will comprise a mixture of a glycol plasticizer having a molecular weight of from about 200 to about 600 and an organic polymer cast on a porous support. The use of such membranes as exemplified by polyethylene glycol and silicon rubber composited on polysulfone will permit greater selectivity accompanied by a high flux rate in the separation process.

Kulprathipanja, S.; Kulkarni, S.S.

1986-08-26T23:59:59.000Z

143

Separation of polar gases from nonpolar gases  

DOE Patents [OSTI]

Polar gases such as hydrogen sulfide, sulfur dioxide and ammonia may be separated from nonpolar gases such as methane, nitrogen, hydrogen or carbon dioxide by passing a mixture of polar and nonpolar gases over the face of a multicomponent membrane at separation conditions. The multicomponent membrane which is used to effect the separation will comprise a mixture of a glycol plasticizer having a molecular weight of from about 200 to about 600 and an organic polymer cast on a porous support. The use of such membranes as exemplified by polyethylene glycol and silicon rubber composited on polysulfone will permit greater selectivity accompanied by a high flux rate in the separation process.

Kulprathipanja, Santi (Hoffman Estates, IL); Kulkarni, Sudhir S. (Hoffman Estates, IL)

1986-01-01T23:59:59.000Z

144

,"Liquefied U.S. Natural Gas Re-Exports to Brazil (Million Cubic...  

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

to Brazil (Million Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Liquefied...

145

En kartläggning av den globala handeln med Liquefied Natural Gas, LNG.  

E-Print Network [OSTI]

??Det här arbetet handlar om den globala handeln med Liquefied Natural Gas, LNG. LNG är naturgas som har gjorts flytande och består till mer än… (more)

Waahler, Oskar

2012-01-01T23:59:59.000Z

146

Numerical simulation on dense gas dispersion and fire characteristics after liquefied natural gas release.  

E-Print Network [OSTI]

??This PhD dissertation mainly studies the prediction, simulation and mitigation methods of the two main hazards in LNG (Liquefied Natural Gas) industry, LNG vapor dense… (more)

Sun, Biao

2012-01-01T23:59:59.000Z

147

,"Price of U.S. Liquefied Natural Gas Imports From Algeria (Dollars...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Algeria (Dollars per Thousand Cubic...

148

,"Price of U.S. Liquefied Natural Gas Imports From Peru (Dollars...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Peru (Dollars per Thousand Cubic...

149

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 19. PAD District 4 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 393 - - - - 330 -111 -46 4 562 0 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 406 0 2 15 -333 - - 0 20 9 61 Pentanes Plus .................................................. 58 0 - - - -33 - - 0 6 9 10 Liquefied Petroleum Gases .............................. 348 - - 2 15 -299 - -

150

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 23. PAD District 5 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 1,197 - - - - 1,186 - -47 -4 2,340 0 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 69 0 14 4 - - - -60 83 20 43 Pentanes Plus .................................................. 32 0 - - - - - - -1 26 2 5 Liquefied Petroleum Gases .............................. 37 - - 14 4 - - - -59

151

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 7. PAD District 1 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 24 - - - - 854 -10 42 -28 935 3 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 42 0 27 67 119 - - -30 26 1 259 Pentanes Plus .................................................. 7 0 - - - - - - 0 - 0 7 Liquefied Petroleum Gases .............................. 35 - - 27 67 119 - - -30 26

152

untitled  

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

PAD District 2 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 1,114 - - - - 1,730 800 -85 62 3,442 55 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 446 -16 121 74 -25 - - -12 105 111 395 Pentanes Plus .................................................. 50 -16 - - 1 82 - - -4 31 101 -12 Liquefied Petroleum Gases .............................. 396 - - 121 73 -107 - - -8 74 11 407

153

untitled  

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

PAD District 1 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 26 - - - - 864 11 23 -4 919 9 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 45 0 39 49 73 - - -4 20 8 182 Pentanes Plus .................................................. 8 0 - - 1 0 - - 0 0 1 7 Liquefied Petroleum Gases .............................. 37 - - 39 49 73 - - -4 20 7 175 Ethane/Ethylene ...........................................

154

Petroleum Supply Monthly  

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

6 6 September 2013 Table 20. PAD District 4 - Year-to-Date Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 511 - - - - 289 -169 -49 4 579 0 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 316 0 13 11 -264 - - 2 16 15 44 Pentanes Plus .................................................. 50 0 - - 0 -38 - - 0 6 13 -7 Liquefied Petroleum Gases ..............................

155

DOE - Office of Legacy Management -- International Rare Metals Refinery Inc  

Office of Legacy Management (LM)

Rare Metals Refinery Rare Metals Refinery Inc - NY 38 FUSRAP Considered Sites Site: International Rare Metals Refinery, Inc. (NY.38 ) Eliminated from consideration under FUSRAP Designated Name: Not Designated Alternate Name: Canadian Radium and Uranium Corporation NY.38-1 Location: 69 Kisko Avenue , Mt. Kisko , New York NY.38-1 NY.38-3 Evaluation Year: 1987 NY.38-4 Site Operations: Manufactured and distributed radium and polonium products. NY.38-5 Site Disposition: Eliminated - No Authority - Site was a commercial operation not under the jurisdiction of DOE predecessor agencies NY.38-2 NY.38-4 Radioactive Materials Handled: Yes Primary Radioactive Materials Handled: Radium, Plutonium NY.38-5 Radiological Survey(s): Yes NY.38-1 NY.38-5 Site Status: Eliminated from consideration under FUSRAP

156

VarPetrRef 1 VARIETY AND THE EVOLUTION OF REFINERY PROCESSING  

E-Print Network [OSTI]

VarPetrRef 1 VARIETY AND THE EVOLUTION OF REFINERY PROCESSING Phuong NGUYEN*, Pier-Paolo SAVIOTTI, refinery processes, variety, niche theory, Weitzman measure. JEL classification : L15 -L93 -O3 1

Paris-Sud XI, Université de

157

U.S. Natural Gas Supplemental Gas - Refinery Gas (Million Cubic...  

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

Refinery Gas (Million Cubic Feet) U.S. Natural Gas Supplemental Gas - Refinery Gas (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9...

158

JANUARY 2007 THE BP U.S. REFINERIES INDEPENDENT SAFETY REVIEW PANEL  

E-Print Network [OSTI]

OF JANUARY 2007 THE REPORT THE BP U.S. REFINERIES INDEPENDENT SAFETY REVIEW PANEL #12;From left;PANEL STATEMENT The B.P. U.S. Refineries Independent Safety Review Panel i Process safety accidents can be prevented. On March 23, 2005, the BP Texas City refinery experienced a catastrophic process accident

Leveson, Nancy

159

Treating refinery wastewaters in microbial fuel cells using separator electrode assembly or spaced electrode configurations  

E-Print Network [OSTI]

Treating refinery wastewaters in microbial fuel cells using separator electrode assembly or spaced 2013 Available online 5 November 2013 Keywords: Microbial fuel cells Refinery wastewater Biodegradability Separator electrode assembly a b s t r a c t The effectiveness of refinery wastewater (RW

160

GDP Formulation of a segmented CDU Swing Cut Model for Refinery Planning  

E-Print Network [OSTI]

AGO HGO HFO RG LPG R95 R100 RG LPG CN CGO RG Refinery Operation and Management - J.P. Favennec Crude1 GDP Formulation of a segmented CDU Swing Cut Model for Refinery Planning (Performance Analysis. Grossmann #12;2 Motivation · Refinery planning is an active area in process systems that strongly relies

Grossmann, Ignacio E.

Note: This page contains sample records for the topic "liquefied refinery gases" 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

GDP Formulation of a segmented CDU Swing Cut Model for Refinery Planning  

E-Print Network [OSTI]

RG LPG R95 R100 RG LPG CN CGO RG Refinery Operation and Management - J.P. Favennec Crude Distillation1 GDP Formulation of a segmented CDU Swing Cut Model for Refinery Planning Department of Chemical · Refinery planning is an active area in process systems that strongly relies on the accuracy of the CDU

Grossmann, Ignacio E.

162

Perception of an emergency Situation by operators in an oil refinery L.Pioche&J.RPineau  

E-Print Network [OSTI]

Perception of an emergency Situation by operators in an oil refinery L.Pioche&J.RPineau Institut de the operators' behaviour during an emergency Situation m an oil refinery. The aim ofthis stage the general objective is to analyse the operators' behaviour during an emergency Situation in an oil refinery

Paris-Sud XI, Université de

163

Price of U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per  

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

U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per Thousand Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1997 NA NA 2001 -- -- -- -- -- -- -- -- -- -- -- -- 2002 -- -- -- -- -- -- -- -- -- -- -- -- 2003 -- -- -- -- -- -- -- -- -- -- -- -- 2004 -- -- -- -- -- -- -- -- -- -- -- -- 2005 -- -- -- -- -- -- -- -- -- -- -- -- 2006 -- -- -- -- -- -- -- -- -- -- -- -- 2007 -- -- -- -- -- -- -- -- -- -- -- -- 2008 -- -- -- -- -- -- -- -- -- -- -- -- 2009 -- -- -- -- -- -- -- -- -- -- -- -- 2010 -- -- -- -- -- -- -- -- -- -- -- -- 2011 -- -- -- -- -- -- -- -- -- -- -- -- 2012 -- -- -- -- -- -- -- -- -- -- -- --

164

Saudi Aramco Mobile Refinery Company (SAMREF) | Open Energy Information  

Open Energy Info (EERE)

Saudi Aramco Mobile Refinery Company (SAMREF) Saudi Aramco Mobile Refinery Company (SAMREF) Jump to: navigation, search Logo: Saudi Aramco Mobile Refinery Company (SAMREF) Name Saudi Aramco Mobile Refinery Company (SAMREF) Address P.O. Box 30078 Place Yanbu, Saudi Arabia Sector Oil and Gas Product Crude Oil Refining Phone number (966) (4) 396-4443 Website http://www.samref.com.sa/ Coordinates 24.0866932°, 38.0585527° 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":24.0866932,"lon":38.0585527,"alt":0,"address":"","icon":"","group":"","inlineLabel":"","visitedicon":""}]}

165

Low temperature thermal treatment for petroleum refinery waste sludges  

SciTech Connect (OSTI)

Treatment requirements for waste sludges generated by petroleum refinery operations and designated as waste codes K048, K049, K050, K051 and K052 under the Resource Conservation and Recovery Act (RCRA) became effective in November, 1990 under the Landban regulations. An experimental program evaluated low temperature thermal treatment of filter cakes produced from these sludges using laboratory and pilot-scale equipment. One set of experiments on waste samples from two different refineries demonstrated the effective removal of organics of concern from the sludges to meet the RCRA Best Demonstrated Available Technology (BDAT) treatment standards. Cyanides were also within the acceptable limit. Combined with stabilization of heavy metals in the treatment residues, low temperature thermal treatment therefore provides an effective and efficient means of treating refinery sludges, with most hydrocarbons recovered and recycled to the refinery. A milder thermal treatment was used to remove the bulk of the water from a previously filtered waste sludge, providing effective waste minimization through a 40% decrease in the mass of sludge to be disposed. The heating value of the sludge was increased simultaneously by one-third, thereby producing a residue of greater value in an alternative fuels program. A process based on this approach was successfully designed and commercialized.

Ayen, R.J.; Swanstrom, C.P. (Geneva Research Center, IL (United States))

1992-05-01T23:59:59.000Z

166

Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by  

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

2: August 13, 2: August 13, 2007 Refinery Output by World Region to someone by E-mail Share Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on Facebook Tweet about Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on Twitter Bookmark Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on Google Bookmark Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on Delicious Rank Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on Digg Find More places to share Vehicle Technologies Office: Fact #482: August 13, 2007 Refinery Output by World Region on AddThis.com... Fact #482: August 13, 2007

167

Liquefied Natural Gas: Global Challenges (released in AEO2008)  

Reports and Publications (EIA)

U.S. imports of liquefied natural gas (LNG) in 2007 were more than triple the 2000 total, and they are expected to grow in the long term as North Americas conventional natural gas production declines. With U.S. dependence on LNG imports increasing, competitive forces in the international markets for natural gas in general and LNG in particular will play a larger role in shaping the U.S. market for LNG. Key factors currently shaping the future of the global LNG market include the evolution of project economics, worldwide demand for natural gas, government policies that affect the development and use of natural resources in countries with LNG facilities, and changes in seasonal patterns of LNG trade.

2008-01-01T23:59:59.000Z

168

Ruling on Liquefied Natural Gas (LNG) Tax Rate Sparks Debate  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

IRS Ruling IRS Ruling On August 7, 1995, the Federal Register reported the Internal Revenue Service (IRS) ruling that liquefied natural gas (LNG) is a liquid fuel and will thus be taxed as a "special motor fuel," effective October 1, 1995. This definition covers all liquids that substitute for gasoline and diesel. The ruling refuted the claim of petitioners, such as the Natural Gas Vehicle (NGV) Coalition, that LNG is the same as compressed natural gas (CNG) and should be taxed at the equivalent excise tax rate. The IRS also rejected the Coalition's proposal that the NGV tax rate be expressed as gasoline gallon equivalent (GGE) rather than in thousand cubic feet (mcf) as provided in the Internal Revenue Code, but stated that no restrictions exist on taxpayers engaged in fuel sales based on

169

Strongly interacting Fermi gases  

E-Print Network [OSTI]

Strongly interacting gases of ultracold fermions have become an amazingly rich test-bed for many-body theories of fermionic matter. Here we present our recent experiments on these systems. Firstly, we discuss high-precision ...

Bakr, W.

170

Pemex to acquire interest in Shell Texas refinery  

SciTech Connect (OSTI)

This paper reports that Petroleos Mexicanos and Shell Oil Co. have signed a memorandum of understanding to form a joint refining venture involving Shell's 225,000 b/d Deer Park, Tex., refinery. Under the agreement, Mexico's state owned oil company is to purchase a 50% interest in the refinery, and Shell is to sell Pemex unleaded gasoline on a long term basis. Under the venture, Shell and Pemex plan to add undisclosed conversion and upgrading units tailored to process heavy Mexican crude. The revamp will allow Pemex to place more than 100,000 b/d of Mayan heavy crude on the U.S. market. Mayan accounts for 70% of Mexico's crude oil exports. In turn, Shell will sell Pemex as much as 45,000 b/d of unleaded gasoline to help meet Mexico's rapidly growing demand.

Not Available

1992-08-31T23:59:59.000Z

171

Kidney cancer and hydrocarbon exposures among petroleum refinery workers  

SciTech Connect (OSTI)

To evaluate the hypothesis of increased kidney cancer risk after exposure to hydrocarbons, especially those present in gasoline, we conducted a case-control study in a cohort of approximately 100,000 male refinery workers from five petroleum companies. A review of 18,323 death certificates identified 102 kidney cancer cases, to each of whom four controls were matched by refinery location and decade of birth. Work histories, containing an average of 15.7 job assignments per subject, were found for 98% of the cases and 94% of the controls. Tb each job, industrial hygienists assigned semiquantitative ratings for the intensity and frequency of exposures to three hydrocarbon categories: nonaromatic liquid gasoline distillates, aromatic hydrocarbons, and the more volatile hydrocarbons. Ratings of {open_quotes}present{close_quotes} or {open_quotes}absent{close_quotes} were assigned for seven additional exposures: higher boiling hydrocarbons, polynuclear aromatic hydrocarbons, asbestos, chlorinated solvents, ionizing radiation, and lead. Each exposure had either no association or a weak association with kidney cancer. For the hydrocarbon category of principal a priori interest, the nonaromatic liquid gasoline distillates, the estimated relative risk (RR) for any exposure above refinery background was 1.0 (95% confidence interval [CI] 0.5-1.9). Analyses of cumulative exposures and of exposures in varying time periods before kidney cancer occurrence also produced null or near-null results. In an analysis of the longest job held by each subject (average duration 9.2 years or 40% of the refiner&y work history), three groups appeared to be at increased risk: laborers (RR = 1.9,95% CI 1.0-3.9); workers in receipt, storage, and movements (RR = 2.5,95% CI 0.9-6.6); and unit cleaners (RR = 2.3, 95% CI 0.5-9.9). 53 refs., 7 tabs.

Poole, C.; Dreyer, N.A.; Satterfield, M.H. [Epidemiology Resources Inc., Newton Lower Falls, MA (United States); Levin, L. [Drexel Univ., Philadelphia, PA (United States)

1993-12-01T23:59:59.000Z

172

Combustion air preheating for refinery heaters using plate-type heat exchangers  

SciTech Connect (OSTI)

Combustion air preheating by recovering heat from combustion gases is a cost effective method of increasing the overall thermal efficiency of the refining and petrochemical processes. This paper presents the advantages of the plate-type air preheaters made of smooth plates without extended surfaces. These exchangers provide a relatively high heat transfer coefficient at a relatively low pressure drop, resulting in a flexible and compact design. The air preheater design can easily be integrated into the heater design. Top mounting with natural draft becomes possible for many applications, eliminating the need for I.D. fan and expensive ductwork. The economical extent of heat recovery function of the fuel fired is presented based on practical experience. The use of porcelain enameled (glass coated) plates and of stainless steel materials allows the operation of the air preheater below the acidic and water dew point. Finally the paper presents the experience of the Canadian refineries and petrochemical plants with plate-type heat exchangers used for combustion air preheating.

Dinulescu, M.

1987-01-01T23:59:59.000Z

173

Chapter 6 - Alternative valorization routes (refinery, cogeneration, and rerefining residue)  

Science Journals Connector (OSTI)

Publisher Summary Waste oil valorization in a refinery must be considered only after having done a complete feasibility evaluation. Wherever the waste oil is introduced, it should not modify the properties of the refinery products, or the normal operations or functions of the rerefining units. Most oil refineries are complex industrial sites characterized by a very large treated tonnage, a permanent operation of a continuous flow of products from desalination and atmospheric distillation upstream to the storage of finished products downstream passing through all the intermediate refining steps, and the necessity of adapting the units' operating conditions to the treated crude to maintain a good level of quality for the finished products. Other priorities include the need to increase the severity of operating conditions of hydrotreatment to produce gasoline, kerosene, and diesel oil from direct distillation or from thermal or catalytic cracking to comply with the standards for sulfur and aromatic compounds. These constraints provide a better understanding of the importance of alternative valorization routes.

François Audibert

2006-01-01T23:59:59.000Z

174

Modeling and Multi-objective Optimization of Refinery Hydrogen Network  

Science Journals Connector (OSTI)

The demand of hydrogen in oil refinery is increasing as market forces and environmental legislation, so hydrogen network management is becoming increasingly important in refineries. Most studies focused on single- objective optimization problem for the hydrogen network, but few account for the multi-objective optimization problem. This paper presents a novel approach for modeling and multi-objective optimization for hydrogen network in refineries. An improved multi-objective optimization model is proposed based on the concept of superstructure. The optimization includes minimization of operating cost and minimization of investment cost of equipment. The proposed methodology for the multi-objective optimization of hydrogen network takes into account flow rate constraints, pressure constraints, purity constraints, impurity constraints, payback period, etc. The method considers all the feasible connections and subjects this to mixed-integer nonlinear programming (MINLP). A deterministic optimization method is applied to solve this multi-objective optimization problem. Finally, a real case study is introduced to illustrate the applicability of the approach.

Yunqiang JIAO; Hongye SU; Zuwei LIAO; Weifeng HOU

2011-01-01T23:59:59.000Z

175

,"Price of U.S. Liquefied Natural Gas Imports From Egypt (Dollars...  

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

PM" "Back to Contents","Data 1: Price of U.S. Liquefied Natural Gas Imports From Egypt (Dollars per Thousand Cubic Feet)" "Sourcekey","N9103EG3" "Date","Price of U.S....

176

Price of U.S. Liquefied Natural Gas Imports From Indonesia (Dollars...  

Gasoline and Diesel Fuel Update (EIA)

Indonesia (Dollars per Thousand Cubic Feet) Price of U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4...

177

Price of Liquefied U.S. Natural Gas Exports by Vessel (Dollars...  

Gasoline and Diesel Fuel Update (EIA)

(Dollars per Thousand Cubic Feet) Price of Liquefied U.S. Natural Gas Exports by Vessel (Dollars per Thousand Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013...

178

Price of Liquefied U.S. Natural Gas Exports to Portugal (Dollars...  

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

Exports to Portugal (Dollars per Thousand Cubic Feet) Price of Liquefied U.S. Natural Gas Exports to Portugal (Dollars per Thousand Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

179

Price of U.S. Liquefied Natural Gas Imports From Canada (Dollars...  

Gasoline and Diesel Fuel Update (EIA)

Date: 10312014 Next Release Date: 11282014 Referring Pages: U.S. Natural Gas Imports by Country U.S. Price of Liquefied Natural Gas Imports by Point of Entry U.S. LNG Imports...

180

,"Liquefied U.S. Natural Gas Re-Exports to Russia (Million Cubic...  

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

Russia (Million Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Liquefied U.S....

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Proposing a novel combined cycle for optimal exergy recovery of liquefied natural gas  

Science Journals Connector (OSTI)

The effective utilization of the cryogenic exergy associated with liquefied natural gas (LNG) vaporization is important. In this paper, a novel combined power cycle is proposed which utilizes LNG in different ......

M. R. Salimpour; M. A. Zahedi

2012-08-01T23:59:59.000Z

182

Liquefied Natural Gas (LNG) Vapor Dispersion Modeling with Computational Fluid Dynamics Codes  

E-Print Network [OSTI]

Federal regulation 49 CFR 193 and standard NFPA 59A require the use of validated consequence models to determine the vapor cloud dispersion exclusion zones for accidental liquefied natural gas (LNG) releases. For modeling purposes, the physical...

Qi, Ruifeng

2012-10-19T23:59:59.000Z

183

,"Liquefied U.S. Natural Gas Re-Exports to Japan (Million Cubic...  

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

Japan (Million Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","Liquefied U.S....

184

Potential Impacts of Reductions in Refinery Activity on Northeast Petroleum Product Markets  

Reports and Publications (EIA)

Potential Impacts of Reductions in Refinery Activity on Northeast Petroleum Product Markets is an update to a previous Energy Information Administration (EIA) report, Reductions in Northeast Refining Activity: Potential Implications for Petroleum Product Markets, released in December 2011. This update analyzes possible market responses and impacts in the event Sunoco's Philadelphia refinery closes this summer, in addition to the recently idled refineries on the East Coast and in the U.S. Virgin Islands.

2012-01-01T23:59:59.000Z

185

Liquefied Gaseous Fuels Safety and Environmental Control Assessment Program: second status report  

SciTech Connect (OSTI)

The Assistant Secretary for Environment has responsibility for identifying, characterizing, and ameliorating the environmental, health, and safety issues and public concerns associated with commercial operation of specific energy systems. The need for developing a safety and environmental control assessment for liquefied gaseous fuels was identified by the Environmental and Safety Engineering Division as a result of discussions with various governmental, industry, and academic persons having expertise with respect to the particular materials involved: liquefied natural gas, liquefied petroleum gas, hydrogen, and anhydrous ammonia. This document is arranged in three volumes and reports on progress in the Liquefied Gaseous Fuels (LGF) Safety and Environmental Control Assessment Program made in Fiscal Year (FY)-1979 and early FY-1980. Volume 1 (Executive Summary) describes the background, purpose and organization of the LGF Program and contains summaries of the 25 reports presented in Volumes 2 and 3. Annotated bibliographies on Liquefied Natural Gas (LNG) Safety and Environmental Control Research and on Fire Safety and Hazards of Liquefied Petroleum Gas (LPG) are included in Volume 1.

Not Available

1980-10-01T23:59:59.000Z

186

Updated estimation of energy efficiencies of U.S. petroleum refineries.  

SciTech Connect (OSTI)

Evaluation of life-cycle (or well-to-wheels, WTW) energy and emission impacts of vehicle/fuel systems requires energy use (or energy efficiencies) of energy processing or conversion activities. In most such studies, petroleum fuels are included. Thus, determination of energy efficiencies of petroleum refineries becomes a necessary step for life-cycle analyses of vehicle/fuel systems. Petroleum refinery energy efficiencies can then be used to determine the total amount of process energy use for refinery operation. Furthermore, since refineries produce multiple products, allocation of energy use and emissions associated with petroleum refineries to various petroleum products is needed for WTW analysis of individual fuels such as gasoline and diesel. In particular, GREET, the life-cycle model developed at Argonne National Laboratory with DOE sponsorship, compares energy use and emissions of various transportation fuels including gasoline and diesel. Energy use in petroleum refineries is key components of well-to-pump (WTP) energy use and emissions of gasoline and diesel. In GREET, petroleum refinery overall energy efficiencies are used to determine petroleum product specific energy efficiencies. Argonne has developed petroleum refining efficiencies from LP simulations of petroleum refineries and EIA survey data of petroleum refineries up to 2006 (see Wang, 2008). This memo documents Argonne's most recent update of petroleum refining efficiencies.

Palou-Rivera, I.; Wang, M. Q. (Energy Systems)

2010-12-08T23:59:59.000Z

187

Control method for mixed refrigerant based natural gas liquefier  

DOE Patents [OSTI]

In a natural gas liquefaction system having a refrigerant storage circuit, a refrigerant circulation circuit in fluid communication with the refrigerant storage circuit, and a natural gas liquefaction circuit in thermal communication with the refrigerant circulation circuit, a method for liquefaction of natural gas in which pressure in the refrigerant circulation circuit is adjusted to below about 175 psig by exchange of refrigerant with the refrigerant storage circuit. A variable speed motor is started whereby operation of a compressor is initiated. The compressor is operated at full discharge capacity. Operation of an expansion valve is initiated whereby suction pressure at the suction pressure port of the compressor is maintained below about 30 psig and discharge pressure at the discharge pressure port of the compressor is maintained below about 350 psig. Refrigerant vapor is introduced from the refrigerant holding tank into the refrigerant circulation circuit until the suction pressure is reduced to below about 15 psig, after which flow of the refrigerant vapor from the refrigerant holding tank is terminated. Natural gas is then introduced into a natural gas liquefier, resulting in liquefaction of the natural gas.

Kountz, Kenneth J. (Palatine, IL); Bishop, Patrick M. (Chicago, IL)

2003-01-01T23:59:59.000Z

188

The application of expansion foam on liquefied natural gas (LNG) to suppress LNG vapor and LNG pool fire thermal radiation.  

E-Print Network [OSTI]

??Liquefied Natural Gas (LNG) hazards include LNG flammable vapor dispersion and LNG pool fire thermal radiation. A large LNG pool fire emits high thermal radiation… (more)

Suardin, Jaffee Arizon

2009-01-01T23:59:59.000Z

189

Cellular glass insulation keeps liquefied gas from vaporizing  

SciTech Connect (OSTI)

The North West Shelf Project, located on the Burrup Peninsula in Western Australia, supplies much of that vast state with natural gas for domestic and industrial applications. Some of the gas is also exported to Japan as liquefied natural gas (LNG). While awaiting shipment to Japan, the LNG is stored at {minus}322 F in four storage tanks, each with a capacity of 2.5 million ft{sup 3}. When Woodside Offshore Petroleum Pty Ltd., operator of the LNG facility, selected insulation material for the storage tanks, it went in search of a material with more than just insulating value. Since the insulation is installed inside the tanks, it must be able to resist wicking or absorbing the LNG. Also, it had to have sufficient strength to withstand the weight of the 2.5 million ft{sup 3} of LNG without being crushed or losing its insulting properties. And, as a safety precaution, the selected materials should neither burn nor support combustion. Ultimately, Woodside selected a cellular glass insulation called Foamglas, from Pittsburgh Corning Corp., that met all the performance criteria and was cost competitive with the lesser-performing alternatives. Foamglas is produced from strong, inert borosilicate glass. Its insulating capability is provided by the tiny, closed cells of air encapsulated within the foam-like structure of the glass. Since the cells are closed,neither liquid nor vapor can enter the structure of the insulation. The inert glass itself will not absorb or react with LNG, nor will it burn or support a fire. The cellular structure provides effective insulation in both not and cold applications, and offers a fire barrier.

NONE

1995-11-01T23:59:59.000Z

190

Liquefied Noble Gas (LNG) detectors for detection of nuclear materials  

Science Journals Connector (OSTI)

Liquefied-noble-gas (LNG) detectors offer, in principle, very good energy resolution for both neutrons and gamma rays, fast response time (hence high-count-rate capabilities), excellent discrimination between neutrons and gamma rays, and scalability to large volumes. They do, however, need cryogenics. LNG detectors in sizes of interest for fissionable material detection in cargo are reaching a certain level of maturity because of the ongoing extensive R&}D effort in high-energy physics regarding their use in the search for dark matter and neutrinoless double beta decay. The unique properties of LNG detectors, especially those using Liquid Argon (LAr) and Liquid Xenon (LXe), call for a study to determine their suitability for Non-Intrusive Inspection (NII) for Special Nuclear Materials (SNM) and possibly for other threats in cargo. Rapiscan Systems Laboratory, Yale University Physics Department, and Adelphi Technology are collaborating in the investigation of the suitability of LAr as a scintillation material for large size inspection systems for air and maritime containers and trucks. This program studies their suitability for NII, determines their potential uses, determines what improvements in performance they offer and recommends changes to their design to further enhance their suitability. An existing 3.1 liter LAr detector (microCLEAN) at Yale University, developed for R&}D on the detection of weakly interacting massive particles (WIMPs) was employed for testing. A larger version of this detector (15 liters), more suitable for the detection of higher energy gamma rays and neutrons is being built for experimental evaluation. Results of measurements and simulations of gamma ray and neutron detection in microCLEAN and a larger detector (326 liter CL38) are presented.

J A Nikkel; T Gozani; C Brown; J Kwong; D N McKinsey; Y Shin; S Kane; C Gary; M Firestone

2012-01-01T23:59:59.000Z

191

Motor System Upgrades Smooth the Way to Savings of $700,000 at Chevron Refinery  

Broader source: Energy.gov [DOE]

Chevron, the largest U.S. refiner operating six gasoline-producing refineries, completed a motor system efficiency improvement project in 1997 at its Richmond, California, refinery that resulted in savings of $700,000 annually. This two-page fact sheet describes how they achieved the savings.

192

Treatability studies on different refinery wastewater samples using high-throughput microbial electrolysis cells (MECs)  

E-Print Network [OSTI]

, 2005), brewery (Feng et al., 2008), animal (Min et al., 2005) and paper recycling wastewaters (HuangTreatability studies on different refinery wastewater samples using high-throughput microbial, University Park, PA 16802, USA h i g h l i g h t s Refinery wastewaters were tested as fuels in MECs

193

STAMP-Based Analysis of a Refinery Overflow Accident Nancy Leveson, Margaret Stringfellow, and John Thomas  

E-Print Network [OSTI]

1 STAMP-Based Analysis of a Refinery Overflow Accident Nancy Leveson, Margaret Stringfellow, and John Thomas As an example of STAMP, we have taken an accident report produced for a real refinery failures and operator actions (or missing actions) related to the loss. But stopping after identifying

Leveson, Nancy

194

Wireless channel characterization and modeling in oil and gas refinery plants  

E-Print Network [OSTI]

Wireless channel characterization and modeling in oil and gas refinery plants Stefano Savazzi1 modeling approach is validated by experimental measurements in two oil refinery sites using industry standard ISA SP100.11a compliant commercial devices operating at 2.4GHz. I. INTRODUCTION The adoption

Savazzi, Stefano

195

High-Octane Fuel from Refinery Exhaust Gas: Upgrading Refinery Off-Gas to High-Octane Alkylate  

SciTech Connect (OSTI)

Broad Funding Opportunity Announcement Project: Exelus is developing a method to convert olefins from oil refinery exhaust gas into alkylate, a clean-burning, high-octane component of gasoline. Traditionally, olefins must be separated from exhaust before they can be converted into another source of useful fuel. Exelus’ process uses catalysts that convert the olefin to alkylate without first separating it from the exhaust. The ability to turn up to 50% of exhaust directly into gasoline blends could result in an additional 46 million gallons of gasoline in the U.S. each year.

None

2009-12-01T23:59:59.000Z

196

Comparison of predicted and measured noise levels for refinery units  

Science Journals Connector (OSTI)

Predicting noise levels from new refinery units is a vital part of environmental assessment and designing units to meet noise limits. The accuracy of those noise predictions is a very important concern. The simplest way to assess the accuracy of predictions is to compare predicted and measured noise levels. This is usually difficult because measured levels are strongly affected by noise from adjacent units and by atmospheric effects on sound propagation. Further actual noise levels of significant sources often deviate from expected levels used in the noise prediction model. Thus to meaningfully compare predicted and measured levels the actual noise source levels for the major sources atmospheric conditions and noise levels from adjacent units must all be accounted for. Predicted and measured levels are compared for two large refinery units. Measurements were made at locations where noise from adjacent units has little effect and close enough so that atmospheric conditions have little impact on the measured levels. Measured operational noise levels of major sources were used to update the noise prediction model. Accuracy of the predictions is evaluated.

Frank H. Brittain; Mark M. Gmerek

1998-01-01T23:59:59.000Z

197

The Energy Minimization Method: A Multiobjective Fitness Evaluation Technique and Its Application to the Production Scheduling in a Petroleum Refinery  

E-Print Network [OSTI]

to the Production Scheduling in a Petroleum Refinery Mayron Rodrigues de Almeida Sílvio Hamacher Industrial applied to production scheduling of a petroleum refinery. The experimental results are presented of the method when applied to the production scheduling in a petroleum refinery. Section 5 discusses

Coello, Carlos A. Coello

198

Fuel switch could bring big savings for HECO Liquefied natural gas beats low-sulfur oil in cost and equipment  

E-Print Network [OSTI]

Fuel switch could bring big savings for HECO Liquefied natural gas beats low-sulfur oil in cost gas instead of continuing to burn low-sulfur fuel oil, a report said. Switching to liquefied natural who switch from gasoline-powered vehicles to ones fueled by compressed natural gas could save as much

199

Market Assessment of Planned Refinery Outages March … June 2009  

Gasoline and Diesel Fuel Update (EIA)

09)/1 09)/1 Market Assessment of Planned Refinery Outages March - June 2009 March 2009 Energy Information Administration Office of Oil and Gas U.S. Department of Energy Washington, DC 20585 This report was prepared by the Energy Information Administration, the independent statistical and analytical agency within the U.S. Department of Energy. The information contained herein should be attributed to the Energy Information Administration and should not be construed as advocating or reflecting any policy position of the U.S. Department of Energy or any other organization. Service Reports are prepared by the Energy Information Administration upon special request and are based on assumptions specified by the requestor.

200

,"U.S. Production Capacity of Operable Petroleum Refineries"  

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

Production Capacity of Operable Petroleum Refineries" Production Capacity of Operable Petroleum Refineries" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Production Capacity of Operable Petroleum Refineries",11,"Annual",2013,"6/30/1982" ,"Release Date:","6/21/2013" ,"Next Release Date:","6/20/2014" ,"Excel File Name:","pet_pnp_capprod_dcu_nus_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capprod_dcu_nus_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov"

Note: This page contains sample records for the topic "liquefied refinery gases" 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

,"U.S. Downstream Charge Capacity of Operable Petroleum Refineries"  

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

Charge Capacity of Operable Petroleum Refineries" Charge Capacity of Operable Petroleum Refineries" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Downstream Charge Capacity of Operable Petroleum Refineries",32,"Annual",2013,"6/30/1982" ,"Release Date:","6/21/2013" ,"Next Release Date:","6/20/2014" ,"Excel File Name:","pet_pnp_capchg_dcu_nus_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capchg_dcu_nus_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov"

202

,"U.S. Total Shell Storage Capacity at Operable Refineries"  

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

Shell Storage Capacity at Operable Refineries" Shell Storage Capacity at Operable Refineries" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Total Shell Storage Capacity at Operable Refineries",28,"Annual",2013,"6/30/1982" ,"Release Date:","6/21/2013" ,"Next Release Date:","6/20/2014" ,"Excel File Name:","pet_pnp_capshell_dcu_nus_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capshell_dcu_nus_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov"

203

,"U.S. Working Storage Capacity at Operable Refineries"  

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

Storage Capacity at Operable Refineries" Storage Capacity at Operable Refineries" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Working Storage Capacity at Operable Refineries",28,"Annual",2013,"6/30/1982" ,"Release Date:","6/21/2013" ,"Next Release Date:","6/20/2014" ,"Excel File Name:","pet_pnp_capwork_dcu_nus_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capwork_dcu_nus_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov"

204

Control of pollutants in flue gases and fuel gases  

E-Print Network [OSTI]

and gasification technologies for heat and power . . . . . . . . 2-3 2.4 Waste incineration and waste . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2-1 2.2 Flue gases and fuel gases: combustion, gasification, pyrolysis, incineration and other . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3-3 3.3 Formation of sulphur compounds during combustion and gasification . 3-5 3.4 Emission

Laughlin, Robert B.

205

Control of pollutants in flue gases and fuel gases  

E-Print Network [OSTI]

. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2-1 2.2 Flue gases and fuel gases: combustion, gasification, pyrolysis, incineration and other and gasification technologies for heat and power . . . . . . . . 2-3 2.4 Waste incineration and waste . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3-3 3.3 Formation of sulphur compounds during combustion and gasification . . 3-5 3.4 Emission

Zevenhoven, Ron

206

Everett, MA Natural Gas Liquefied Natural Gas Imports from Trinidad and  

Gasoline and Diesel Fuel Update (EIA)

Liquefied Natural Gas Imports from Trinidad and Tobago (Million Cubic Feet) Liquefied Natural Gas Imports from Trinidad and Tobago (Million Cubic Feet) Everett, MA Natural Gas Liquefied Natural Gas Imports from Trinidad and Tobago (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 10,240 11,488 7,086 8,271 8,126 8,150 7,731 7,870 5,199 5,520 9,264 4,691 2012 9,482 8,458 7,661 1,447 4,940 5,465 6,646 10,377 5,634 4,748 2,553 2,581 2013 5,126 5,003 4,629 5,171 5,626 5,173 8,023 5,961 2,995 2,674 - = 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: U.S. Liquefied Natural Gas Imports by Point of Entry Everett, MA LNG Imports from Trinidad/Tobago

207

Compressed Natural Gas and Liquefied Petroleum Gas Conversions: The National Renewable Energy Laboratory's Experience  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Compressed Natural Gas and Liquefied Petroleum Gas Conversions: Compressed Natural Gas and Liquefied Petroleum Gas Conversions: The National Renewable Energy Laboratory's Experience N T Y A U E O F E N E R G D E P A R T M E N I T E D S T A T S O F A E R I C M Compressed Natural Gas and Liquefied Petroleum Gas Conversions: The National Renewable Energy Laboratory's Experience N T Y A U E O F E N E R G D E P A R T M E N I T E D S T A T S O F A E R I C M Robert C. Motta Kenneth J. Kelly William W. Warnock Executive Summary The National Renewable Energy Laboratory (NREL) contracted with conversion companies in six states to convert approximately 900 light-duty Federal fleet vehicles to operate on compressed natural gas (CNG) or liquefied petroleum gas (LPG). The contracts were initiated in order to help the Federal government meet the vehicle acquisition requirements of the Energy Policy Act of 1992 (EPACT) during a period of limited

208

Exergy Analysis of Exhaust-Gas of Burning Liquefied-Gas in a Chinese Kitchen  

Science Journals Connector (OSTI)

The research analyzes distribution laws of exhaust-gas of burning liquefied-gas in closed kitchen without any kitchen hood or fan with the exergy indicator; and compares the distribution results from the exergy analysis with those from the concentration ... Keywords: Exhaust-gas, exergy distribution, CFD simulation, tecplot fitting

Ao Yong-an; Gao Xing-quan; Shen Lin; Wang Yue-ren; Feng Guo-hui

2009-10-01T23:59:59.000Z

209

Liquefied U.S. Natural Gas Exports to Brazil (Million Cubic Feet...  

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

Brazil (Million Cubic Feet) Liquefied U.S. Natural Gas Exports to Brazil (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2010 0 0 0 0 0 0 0 0 0 0 3,279 0...

210

Impact of Liquefied Natural Gas usage and payload size on Hybrid Wing Body aircraft fuel efficiency  

E-Print Network [OSTI]

This work assessed Hybrid Wing Body (HWB) aircraft in the context of Liquefied Natural Gas (LNG) fuel usage and payload/range scalability at three scales: H1 (B737), H2 (B787) and H3 (B777). The aircraft were optimized for ...

Mody, Pritesh (Pritesh Chetan)

2010-01-01T23:59:59.000Z

211

Energy Department Authorizes Cameron LNG and Carib Energy to Export Liquefied Natural Gas  

Broader source: Energy.gov [DOE]

The Energy Department announced today that it has issued the final authorization to Cameron LNG, LLC (Cameron) and Carib Energy LLC (Carib) to export domestically produced liquefied natural gas (LNG) to countries that do not have a Free Trade Agreement (FTA) with the United States.

212

Liquefied U.S. Natural Gas Exports to Russia (Million Cubic Feet...  

Gasoline and Diesel Fuel Update (EIA)

Russia (Million Cubic Feet) Liquefied U.S. Natural Gas Exports to Russia (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2007 0 0 0 0 0 0 0 0 0 1,895 0 0...

213

Application of landfill gas as a liquefied natural gas fuel for refuse trucks in Texas  

E-Print Network [OSTI]

truck operations. The purpose of this thesis is to develop a methodology that can be used to evaluate the use of LFG generated at landfills as a Liquefied Natural Gas (LNG) fuel source for refuse trucks in Texas. The methodology simulates the gas...

Gokhale, Bhushan

2007-04-25T23:59:59.000Z

214

Control of Vapor Dispersion and Pool Fire of Liquefied Natural Gas (LNG) with Expansion Foam  

E-Print Network [OSTI]

Liquefied Natural Gas (LNG) is flammable when it forms a 5 – 15 percent volumetric concentration mixture with air at atmospheric conditions. When the LNG vapor comes in contact with an ignition source, it may result in fire and/or explosion. Because...

Yun, Geun Woong

2011-10-21T23:59:59.000Z

215

Federal Energy Management Program: Greenhouse Gases  

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

Greenhouse Gases Greenhouse Gases to someone by E-mail Share Federal Energy Management Program: Greenhouse Gases on Facebook Tweet about Federal Energy Management Program: Greenhouse Gases on Twitter Bookmark Federal Energy Management Program: Greenhouse Gases on Google Bookmark Federal Energy Management Program: Greenhouse Gases on Delicious Rank Federal Energy Management Program: Greenhouse Gases on Digg Find More places to share Federal Energy Management Program: Greenhouse Gases on AddThis.com... Sustainable Buildings & Campuses Operations & Maintenance Greenhouse Gases Basics Federal Requirements Guidance & Reporting Inventories & Performance Mitigation Planning Resources Contacts Water Efficiency Data Center Energy Efficiency Industrial Facilities Sustainable Federal Fleets

216

Voluntary Reporting of Greenhouse Gases  

Reports and Publications (EIA)

The Voluntary Reporting of Greenhouse Gases Program was suspended May 2011. It was a mechanism by which corporations, government agencies, individuals, voluntary organizations, etc., could report to the Energy Information Administration, any actions taken that have or are expected to reduce/avoid emissions of greenhouse gases or sequester carbon.

2011-01-01T23:59:59.000Z

217

House Passage of H.R. 5254 - The Refinery Permit Process Schedule Act |  

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

Passage of H.R. 5254 - The Refinery Permit Process Schedule Passage of H.R. 5254 - The Refinery Permit Process Schedule Act House Passage of H.R. 5254 - The Refinery Permit Process Schedule Act June 8, 2006 - 2:17pm Addthis Statement from Secretary Bodman WASHINGTON, DC - The following is a statement from the Secretary Samuel W. Bodman of the Department of Energy on the passage of House Resolution 5254, The Refinery Permit Process Schedule Act: "I commend the House of Representatives for their passage of this important piece of legislation. Expanding our nation's refining capacity is an important part of President Bush's four-point plan to confront high gasoline prices and is a key component to strengthening our nation's energy security. By increasing our nation's domestic refining capacity we can help grow our nation's economy and reduce our reliance on foreign sources

218

Market Assessment of Refinery Outages Planned for March 2011 through June 2011  

Gasoline and Diesel Fuel Update (EIA)

Assessment of Refinery Assessment of Refinery Outages Planned for March 2011 through June 2011 APRIL 2011 www.eia.gov U.S. Department of Energy Washington, DC 20585 U.S. Energy Information Administration / Market Assessment of Planned Refinery Outages / March 2011 - June 2011 ii This report was prepared by the U.S. Energy Information Administration (EIA), the statistical and analytical agency within the U.S. Department of Energy. By law, EIA's data, analyses, and forecasts are independent of approval by any other officer or employee of the United States Government. The views in this report therefore should not be construed as representing those of the Department of Energy or other Federal agencies. U.S. Energy Information Administration / Market Assessment of Planned Refinery Outages /

219

Appendix D Short-Term Analysis of Refinery Costs and Supply  

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

Short-Term Analysis of Refinery Costs and Supply 9302 Appendix D Short-Term Analysis of Refinery Costs and Supply As a result of the new regulations issued by the U.S. Estimating Components of the Distillate Environmental Protection Agency (EPA) for ultra-low- Blend Pool sulfur diesel fuel (ULSD) the U.S. refining industry faces two major challenges: to meet the more stringent specifi- The initial step of the analysis was to analyze the poten- cations for diesel product, and to keep up with demand tial economics of producing ULSD for each refinery. by producing more diesel product from feedstocks of Using input and output data submitted to the Energy lower quality. Some refineries in the United States and Information Administration (E1A) by refiners, the cur-

220

Hydrogen Sulfide Exposure among Oil Refinery Workers at Marathon Petroleum Company in Canton, Ohio.  

E-Print Network [OSTI]

??Air monitoring surveys were conducted during loading operations at three locations inside of Marathon Petroleum Company’s Canton, Ohio oil refinery. These three locations—the sulfur truck… (more)

Beil, Christine A

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

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

E-Print Network [OSTI]

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

Meacher, J. S.

1981-01-01T23:59:59.000Z

222

Regulation: EPA sued for undercounting toxic emissions at refineries, chemical plants  

Science Journals Connector (OSTI)

Several community organizations have filed a lawsuit to force the Environmental Protection Agency to review the way it measures toxic air pollution from oil refineries and petrochemical plants along the Texas-Louisiana Gulf Coast. ... Recent independent studies at Marathon Oil, Shell, and BP refineries measured actual emissions at levels 10 to 100 times higher than estimates based on the methods facilities currently use to report their releases, the suit says. ...

GLENN HESS

2013-05-13T23:59:59.000Z

223

Assuring Mechanical Integrity of Refinery Equipment Through Global ON-Stream Inspection  

SciTech Connect (OSTI)

The development of global on-stream inspection technology will have a dramatic effect on how refinery operations are managed in the U.S. in the future. Global on-stream inspection will provide assurance of the mechanical integrity of critical plant equipment and will allow refineries to operate more efficiently with less impact on our environment and with an increased margin of safety.

John W. Berthold

2006-02-22T23:59:59.000Z

224

Petroleum Refinery Jobs and Economic Development Impact (JEDI) Model User Reference Guide  

SciTech Connect (OSTI)

The Jobs and Economic Development Impact (JEDI) models, developed through the National Renewable Energy Laboratory (NREL), are user-friendly tools utilized to estimate the economic impacts at the local level of constructing and operating fuel and power generation projects for a range of conventional and renewable energy technologies. The JEDI Petroleum Refinery Model User Reference Guide was developed to assist users in employing and understanding the model. This guide provides information on the model's underlying methodology, as well as the parameters and references used to develop the cost data utilized in the model. This guide also provides basic instruction on model add-in features, operation of the model, and a discussion of how the results should be interpreted. Based on project-specific inputs from the user, the model estimates job creation, earning and output (total economic activity) for a given petroleum refinery. This includes the direct, indirect and induced economic impacts to the local economy associated with the refinery's construction and operation phases. Project cost and job data used in the model are derived from the most current cost estimations available. Local direct and indirect economic impacts are estimated using economic multipliers derived from IMPLAN software. By determining the regional economic impacts and job creation for a proposed refinery, the JEDI Petroleum Refinery model can be used to field questions about the added value refineries may bring to the local community.

Goldberg, M.

2013-12-31T23:59:59.000Z

225

Integration of hydrogen management in refinery planning with rigorous process models and product quality specifications  

Science Journals Connector (OSTI)

New trends of increased heavy crude markets and clean-fuel legislation, to produce ultra low-sulphur (ULS) gasoline and diesel fuels, are forcing refineries to increase their consumption of hydrogen. This critical situation raises the need to have a tool for operating refineries with flexibility and profitability. This paper addresses the planning of refinery with consideration to hydrogen availability. A systematic method for integrating a hydrogen management strategy within a rigorous refinery planning model is undertaken. The presented model consists of two main building blocks: a set of non-linear processing units' models and a hydrogen balance framework. The two blocks are integrated to produce a refinery-wide planning model with hydrogen management. The hydrogen management alternatives were determined by economic analysis. The proposed model improves the hidden hydrogen unavailability that prevents refineries from achieving their maximum production and profit. The model is illustrated on representative case studies and the results are discussed. It was found that an additional annual profit equivalent to $7 million could be achieved with a one-time investment of $13 million in a new purification unit.

Ali Elkamel; Ibrahim Alhajri; A. Almansoori; Yousef Saif

2011-01-01T23:59:59.000Z

226

Advanced refinery process heater. Final report, (October 1983-September 1988)  

SciTech Connect (OSTI)

A prototype refinery process heater was designed, built and successfully tested, demonstrating the improvements available to heater design through the use of Zone-Controlled Pyrocore radiant gas burners. The 10 MMBtu/hr rated heater released 17 ppm NOx (corrected to 3% oxygen) under full load operation, the lowest NOx emissions technically and commercially achieved in this type of equipment without the use of post-combustion flue-gas processing. Operating with 400F combustion air preheat and a 500F process fluid outlet temperature, the heater achieved overall thermal efficiencies of 92.8% on a LHV basis due in part to the significantly improved performance of the radiant heat exchange section. The radiant burners used in the heater have been proven in performance and reliability, and have also been shown to be applicable to both new heater designs and retrofits into existing heaters. The improved radiant performance of the heater and the use of 'flameless' radiant burners eliminates tube burn-out failures in both the radiant and convective tube coils, further improving the reliability of equipment based on this design. Three separate U.S. Patents have been issued covering the heater design and the use of Zone-Controlled Pyrocore burners in this application.

Minden, A.C.; Buckley, G.G.

1989-04-01T23:59:59.000Z

227

Process simulation of refinery units including chemical reactors  

Science Journals Connector (OSTI)

Process simulation methods for design and operation of refinery units are well established as long as no chemical reactors are included. The feedstocks are divided into pseudo-components which enables calculation of phase equilibria and transport properties. When chemical reactors are present some chemical conversion takes place which obviously affects the nature of the pseudo-components and their properties. The stream leaving the reactor will not only be of a different composition than the stream entering the reactor but in addition, the pseudo-components making up the outlet stream will also have other physical properties than the ones in the inlet stream. These changes affect not only the reactor unit but also the simulation of the whole flow-sheet. The paper presents a detailed model for an adiabatic distillate hydrotreater which takes into account the elemental composition of the feed. A special simulation strategy has been developed to incorporate such reactor units into process simulators. Finally, the simulation strategy is illustrated for a hydrotreating plant.

Jens A. Hansen; Barry H. Cooper

1992-01-01T23:59:59.000Z

228

Table Definitions, Sources, and Explanatory Notes  

Gasoline and Diesel Fuel Update (EIA)

Natural Gas Plant Net Stocks Natural Gas Plant Net Stocks Definitions Key Terms Definition Barrel A unit of volume equal to 42 U.S. gallons. Butylene (C4H8) An olefinic hydrocarbon recovered from refinery processes. Ethane (C2H6) A normally gaseous straight-chain hydrocarbon. It is a colorless paraffinic gas that boils at a temperature of -127.48º F. It is extracted from natural gas and refinery gas streams. Isobutane (C4H10) A normally gaseous branch-chain hydrocarbon. It is a colorless paraffinic gas that boils at a temperature of 10.9º F. It is extracted from natural gas or refinery gas streams. Liquefied Petroleum Gases (LPG) A group of hydrocarbon-based gases derived from crude oil refining or nautral gas fractionation. They include: ethane, ethylene, propane, propylene, normal butane, butylene, isobutane, and isobutylene. For convenience of transportation, these gases are liquefied through pressurization.

229

U.S. Imports of Crude Oil and Petroleum Products  

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

9,240 9,584 9,380 8,815 9,472 9,309 1973-2014 Crude Oil 7,264 7,547 7,165 7,054 7,623 7,471 1920-2014 Natural Gas Plant Liquids and Liquefied Refinery Gases 166 141 99 116 86 90...

230

Supply and Disposition of Crude Oil and Petroleum Products  

Gasoline and Diesel Fuel Update (EIA)

7,134 78 8,072 4,027 -3,603 366 34 7,401 3,285 5,354 Crude Oil 5,259 - - - - 3,454 -222 227 -164 8,685 198 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 1,875 0 534 1...

231

U.S. Exports of Crude Oil and Petroleum Products  

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

3,858 3,966 4,121 4,156 4,479 4,533 1973-2014 Crude Oil 246 268 288 396 401 389 1920-2014 Natural Gas Plant Liquids and Liquefied Refinery Gases 581 697 727 683 765 743 1981-2014...

232

Supply and Disposition of Crude Oil and Petroleum Products  

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

6,046 98 7,569 4,450 -3,757 434 -42 6,943 2,694 5,247 Crude Oil 4,384 - - - - 3,691 -391 312 6 7,952 37 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 1,663 0 411 35 165...

233

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

Broader source: Energy.gov [DOE]

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

234

Large scale production of carbon nanotube arrays on the sphere surface from liquefied petroleum gas at low cost  

Science Journals Connector (OSTI)

Liquefied petroleum gas (LPG), a cheap industrial material, ... and good mobility, leading to the mass production of CNT arrays continuously. The arrays obtained ... easily be produced on large scale at low cost.

Qiang Zhang; JiaQi Huang; Fei Wei; GuangHui Xu; Yao Wang…

2007-11-01T23:59:59.000Z

235

The application of expansion foam on liquefied natural gas (LNG) to suppress LNG vapor and LNG pool fire thermal radiation  

E-Print Network [OSTI]

Liquefied Natural Gas (LNG) hazards include LNG flammable vapor dispersion and LNG pool fire thermal radiation. A large LNG pool fire emits high thermal radiation thus preventing fire fighters from approaching and extinguishing the fire. One...

Suardin, Jaffee Arizon

2009-05-15T23:59:59.000Z

236

Greenhouse Gases | Department of Energy  

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

Greenhouse Gases Greenhouse Gases Greenhouse Gases October 7, 2013 - 9:59am Addthis Executive Order 13514 requires Federal agencies to inventory and manage greenhouse gas (GHG) emissions to meet Federal goals and mitigate climate change. Basics: Read an overview of greenhouse gases. Federal Requirements: Look up requirements for agency greenhouse gas management as outlined in Federal initiatives and executive orders. Guidance and Reporting: Find guidance documents and resources for greenhouse gas accounting and reporting. GHG Inventories and Performance: See detailed comprehensive GHG inventories by Federal agency and progress toward achieving Scope 1 and 2 GHG and Scope 3 GHG reduction targets. Mitigation Planning: Learn how Federal agencies can cost-effectively meet their GHG reduction goals.

237

Degenerate quantum gases of strontium  

E-Print Network [OSTI]

Degenerate quantum gases of alkaline-earth-like elements open new opportunities in research areas ranging from molecular physics to the study of strongly correlated systems. These experiments exploit the rich electronic structure of these elements, which is markedly different from the one of other species for which quantum degeneracy has been attained. Specifically, alkaline-earth-like atoms, such as strontium, feature metastable triplet states, narrow intercombination lines, and a non-magnetic, closed-shell ground state. This review covers the creation of quantum degenerate gases of strontium and the first experiments performed with this new system. It focuses on laser-cooling and evaporation schemes, which enable the creation of Bose-Einstein condensates and degenerate Fermi gases of all strontium isotopes, and shows how they are used for the investigation of optical Feshbach resonances, the study of degenerate gases loaded into an optical lattice, as well as the coherent creation of Sr_2 molecules.

Stellmer, Simon; Killian, Thomas C

2013-01-01T23:59:59.000Z

238

Turning greenhouse gases into gold  

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

gases, with carbon dioxide (CO2) often accused of being the primary instigator of global climate change. As a result, numerous efforts are under way to find ways to prevent,...

239

ARM - What are Greenhouse Gases?  

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

radiative forcing (which means they enhance global warming). Many of these gases are naturally occurring and are essential to life on earth by providing a blanket for marine and...

240

Greenhouse Gases and Emissions Trading  

Science Journals Connector (OSTI)

Atmospheric concentrations of carbon dioxide and other greenhouse gases have grown rapidly since the beginning of this century. Unless emissions are controlled, the world could face rapid climate changes, incl...

Alice LeBlanc; Daniel J. Dudek

1993-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Production of coal-based fuels and value-added products: coal to liquids using petroleum refinery streams  

SciTech Connect (OSTI)

We are studying several processes that utilize coal, coal-derived materials, or biomass in existing refining facilities. A major emphasis is the production of a coal-based replacement for JP-8 jet fuel. This fuel is very similar to Jet A and jet A-1 in commercial variation, so this work has significant carry-over into the private sector. We have been focusing on three processes that would be retrofitted into a refinery: (1) coal tar/refinery stream blending and hydro-treatment; (2) coal extraction using refinery streams followed by hydro-treatment; and (3) co-coking of coal blended with refinery streams. 4 figs., 5 tabs.

Clifford, C.E.B.; Schobert, H.H. [Pennsylvania State University, PA (United States)

2008-07-01T23:59:59.000Z

242

Recovery of hydrogen and other components from refinery gas stream by partial condensation using preliminary reflux condensation  

SciTech Connect (OSTI)

A process is disclosed for separating a hydrogen-containing refinery-type gas mixture into various fractions using reflux condensation, drying and partial condensation and phase separation.

Beddome, R.A.; Fenner, G.W.; Saunders, J.B.

1984-04-17T23:59:59.000Z

243

Liquefied Gaseous Fuels Safety and Environmental Control Assessment Program: second status report  

SciTech Connect (OSTI)

Volume 2 consists of 19 reports describing technical effort performed by Government Contractors in the area of LNG Safety and Environmental Control. Report topics are: simulation of LNG vapor spread and dispersion by finite element methods; modeling of negatively buoyant vapor cloud dispersion; effect of humidity on the energy budget of a liquefied natural gas (LNG) vapor cloud; LNG fire and explosion phenomena research evaluation; modeling of laminar flames in mixtures of vaporized liquefied natural gas (LNG) and air; chemical kinetics in LNG detonations; effects of cellular structure on the behavior of gaseous detonation waves under transient conditions; computer simulation of combustion and fluid dynamics in two and three dimensions; LNG release prevention and control; the feasibility of methods and systems for reducing LNG tanker fire hazards; safety assessment of gelled LNG; and a four band differential radiometer for monitoring LNG vapors.

None

1980-10-01T23:59:59.000Z

244

Current Status and Perspectives of Liquefied Natural Gas (LNG) Plant Design  

Science Journals Connector (OSTI)

The processes can be classified into three general categories based on the type of refrigeration cycle and equipment used: a cascade process using pure refrigerants, a mixed refrigerant process using refrigerant mixtures, and an expander process using expanders instead of Joule–Thomson (J–T) valves. ... To cool the nitrogen to a low-enough temperature to liquefy natural gas, the cLNG process uses both self-cooling and turbo expanders. ...

Wonsub Lim; Kwangho Choi; Il Moon

2012-12-15T23:59:59.000Z

245

Liquefied natural gas as a transportation fuel for heavy-duty trucks: Volume I  

SciTech Connect (OSTI)

This document contains Volume 1 of a three-volume manual designed for use with a 2- to 3-day liquefied natural gas (LNG) training course. Transportation and off-road agricultural, mining, construction, and industrial applications are discussed. This volume provides a brief introduction to the physics and chemistry of LNG; an overview of several ongoing LNG projects, economic considerations, LNG fuel station technology, LNG vehicles, and a summary of federal government programs that encourage conversion to LNG.

NONE

1997-12-01T23:59:59.000Z

246

Franklin County Sanitary Landfill - Landfill Gas (LFG) to Liquefied Natural Gas (LNG) - Project  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

FRANKLIN COUNTY SANITARY FRANKLIN COUNTY SANITARY LANDFILL - LANDFILL GAS (LFG) TO LIQUEFIED NATURAL GAS (LNG) - PROJECT January/February 2005 Prepared for: National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401 Table of Contents Page BACKGROUND AND INTRODUCTION .......................................................................................1 SUMMARY OF EFFORT PERFORMED ......................................................................................2 Task 2B.1 - Literature Search and Contacts Made...................................................................2 Task 2B.2 - LFG Resource/Resource Collection System - Project Phase One.......................3 Conclusion.................................................................................................................................5

247

Emissions of greenhouse gases from the use of transportation fuels and electricity. Volume 1, Main text  

SciTech Connect (OSTI)

This report presents estimates of full fuel-cycle emissions of greenhouse gases from using transportation fuels and electricity. The data cover emissions of carbon dioxide (CO{sub 2}), methane, carbon monoxide, nitrous oxide, nitrogen oxides, and nonmethane organic compounds resulting from the end use of fuels, compression or liquefaction of gaseous transportation fuels, fuel distribution, fuel production, feedstock transport, feedstock recovery, manufacture of motor vehicles, maintenance of transportation systems, manufacture of materials used in major energy facilities, and changes in land use that result from using biomass-derived fuels. The results for electricity use are in grams of CO{sub 2}-equivalent emissions per kilowatt-hour of electricity delivered to end users and cover generating plants powered by coal, oil, natural gas, methanol, biomass, and nuclear energy. The transportation analysis compares CO{sub 2}-equivalent emissions, in grams per mile, from base-case gasoline and diesel fuel cycles with emissions from these alternative- fuel cycles: methanol from coal, natural gas, or wood; compressed or liquefied natural gas; synthetic natural gas from wood; ethanol from corn or wood; liquefied petroleum gas from oil or natural gas; hydrogen from nuclear or solar power; electricity from coal, uranium, oil, natural gas, biomass, or solar energy, used in battery-powered electric vehicles; and hydrogen and methanol used in fuel-cell vehicles.

DeLuchi, M.A. [California Univ., Davis, CA (United States)

1991-11-01T23:59:59.000Z

248

,"U.S. Refinery Net Input"  

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

3,"Monthly","9/2013","1/15/2005" 3,"Monthly","9/2013","1/15/2005" ,"Data 2","Alaskan Crude Oil Receipts",1,"Monthly","9/2013","1/15/1986" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_inpt2_dc_nus_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_inpt2_dc_nus_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:21:05 AM" "Back to Contents","Data 1: Refinery Net Input" "Sourcekey","MTTRO_NUS_1","MCRRO_NUS_1","MNGRO_NUS_1","MPPRO_NUS_1","MLPRO_NUS_1","MBNRO_NUS_1","MBIRO_NUS_1","MOLRO_NUS_1","MOHRO_NUS_1","M_EPOOOH_YIY_NUS_MBBL","M_EPOOXXFE_YIY_NUS_MBBL","MMTRO_NUS_1","MOORO_NUS_1","M_EPOOR_YIY_NUS_MBBL","MFERO_NUS_1","M_EPOORD_YIY_NUS_MBBL","M_EPOORO_YIY_NUS_MBBL","M_EPOOOXH_YIY_NUS_MBBL","MUORO_NUS_1","MNLRO_NUS_1","MKORO_NUS_1","MH1RO_NUS_1","MRURO_NUS_1","MBCRO_NUS_1","MO1RO_NUS_1","M_EPOBGRR_YIY_NUS_MBBL","MO3RO_NUS_1","MO4RO_NUS_1","MO5RO_NUS_1","MO6RO_NUS_1","MO7RO_NUS_1","MO9RO_NUS_1","MBARO_NUS_1"

249

,"U.S. Refinery Net Input"  

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

2,"Annual",2012,"6/30/2005" 2,"Annual",2012,"6/30/2005" ,"Data 2","Alaskan Crude Oil Receipts",1,"Annual",2012,"6/30/1986" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_pnp_inpt2_dc_nus_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_inpt2_dc_nus_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:21:04 AM" "Back to Contents","Data 1: Refinery Net Input" "Sourcekey","MTTRO_NUS_1","MCRRO_NUS_1","MNGRO_NUS_1","MPPRO_NUS_1","MLPRO_NUS_1","MBNRO_NUS_1","MBIRO_NUS_1","MOLRO_NUS_1","MOHRO_NUS_1","M_EPOOOH_YIY_NUS_MBBL","M_EPOOXXFE_YIY_NUS_MBBL","MMTRO_NUS_1","MOORO_NUS_1","M_EPOOR_YIY_NUS_MBBL","MFERO_NUS_1","M_EPOORD_YIY_NUS_MBBL","M_EPOOOXH_YIY_NUS_MBBL","MUORO_NUS_1","MNLRO_NUS_1","MKORO_NUS_1","MH1RO_NUS_1","MRURO_NUS_1","MBCRO_NUS_1","MO1RO_NUS_1","M_EPOBGRR_YIY_NUS_MBBL","MO3RO_NUS_1","MO4RO_NUS_1","MO5RO_NUS_1","MO6RO_NUS_1","MO7RO_NUS_1","MO9RO_NUS_1","MBARO_NUS_1"

250

Increasing Distillate Production at U.S. Refineries … Past Changes and Future Potential  

Gasoline and Diesel Fuel Update (EIA)

Increasing Distillate Production at U.S. Refineries - Past Changes and Future Increasing Distillate Production at U.S. Refineries - Past Changes and Future Potential U.S. Energy Information Administration Office of Petroleum, Gas, and Biofuels Analysis Department of Energy Office of Policy and International Affairs October 2010 Summary World consumption growth for middle distillate fuels (diesel fuel, heating oil, kerosene, and jet fuel) has exceeded the consumption growth for gasoline for some time, and the United States is no exception. Although the decrease in the ratio of total gasoline consumption to consumption for middle distillate fuels has been small in the United States, recent legislation requiring increased use of renewable fuels has resulted in forecasts that project a decline in consumption for petroleum-based gasoline from refineries, which would accelerate the decline in the

251

,"Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities"  

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

Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities" Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities",16,"Monthly","9/2013","1/15/1985" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_crq_a_epc0_ycs_pct_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_crq_a_epc0_ycs_pct_m.htm" ,"Source:","Energy Information Administration"

252

TSNo s02-roberts104537-O Microscopic and Spectroscopic Speciation of Ni in Soils in the Vicinity of a Ni Refinery.  

E-Print Network [OSTI]

in the Vicinity of a Ni Refinery. abstract Accurately predicting the fate and bioavailability of metals in smelter REFINERY ASA-CSSA-SSSA Annual Meetings - October 21 - 25, 2001 - Charlotte, NC #12;

Sparks, Donald L.

253

Methods applied to investigate the major VCE that occured in the TOTAL refinery's Fluid Catalytic Cracking Unit at La Mede,  

E-Print Network [OSTI]

95-35 Methods applied to investigate the major �VCE that occured in the TOTAL refinery's Fluid.V.C.E, occured in the Gas Plant of the TOTAL refinery's Fluid Catalytic Cracking ünit at La Mede, France sources: control room hard copy and electronically stored records: no deviation of process operating

Paris-Sud XI, Université de

254

Climate VISION: Greenhouse Gases Information  

Office of Scientific and Technical Information (OSTI)

GHG Information GHG Information Greenhouse Gases, Global Climate Change, and Energy Emissions of Greenhouse Gases in the United States 2001 [1605(a)] This report, required by Section 1605(a) of the Energy Policy Act of 1992, provides estimates of U.S. emissions of greenhouse gases, as well as information on the methods used to develop the estimates. The estimates are based on activity data and applied emissions factors, not on measured or metered emissions monitoring. Available Energy Footprints Industry NAICS* All Manufacturing Alumina & Aluminum 3313 Cement 327310 Chemicals 325 Fabricated Metals 332 Food and Beverages 311, 312 Forest Products 321, 322 Foundries 3315 Glass & Glass Products, Fiber Glass 3272, 3296 Iron & Steel Mills 331111 Machinery & Equipment 333, 334, 335, 336

255

International LNG trade : the emergence of a short-term market; International liquefied natural gas trade : the emergence of a short-term market.  

E-Print Network [OSTI]

??Natural gas is estimated to be the fastest growing component of world primary energy consumption. Liquefied natural gas (LNG) supply chain is a way of… (more)

Athanasopoulos, Panagiotis G

2006-01-01T23:59:59.000Z

256

,"U.S. Refinery Net Production"  

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

Annual",2012,"6/30/1993" Annual",2012,"6/30/1993" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_pnp_refp2_dc_nus_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_refp2_dc_nus_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:28:05 AM" "Back to Contents","Data 1: U.S. Refinery Net Production" "Sourcekey","MTTRX_NUS_1","MLPRX_NUS_1","METRX_NUS_1","MENRX_NUS_1","MEYRX_NUS_1","MPRRX_NUS_1","MPARX_NUS_1","MPLRX_NUS_1","MBNRX_NUS_1","MBURX_NUS_1","MBYRX_NUS_1","MBIRX_NUS_1","MIIRX_NUS_1","MIYRX_NUS_1","MGFRX_NUS_1","MGRRX_NUS_1","MG1RX_NUS_1","M_EPM0RO_YPY_NUS_MBBL","MG4RX_NUS_1","MG5RX_NUS_1","M_EPM0CAL55_YPY_NUS_MBBL","M_EPM0CAG55_YPY_NUS_MBBL","MG6RX_NUS_1","MGARX_NUS_1","MKJRX_NUS_1","M_EPJKC_YPY_NUS_MBBL","M_EPJKM_YPY_NUS_MBBL","MKERX_NUS_1","MDIRX_NUS_1","MD0RX_NUS_1","MD1RX_NUS_1","MDGRX_NUS_1","MRERX_NUS_1","MRXRX_NUS_1","MRMRX_NUS_1","MRGRX_NUS_1","MPCRX_NUS_1","MPNRX_NUS_1","MPORX_NUS_1","MNSRX_NUS_1","MLURX_NUS_1","M_EPPLN_YPY_NUS_MBBL","M_EPPLP_YPY_NUS_MBBL","MWXRX_NUS_1","MCKRX_NUS_1","MCMRX_NUS_1","MCORX_NUS_1","MAPRX_NUS_1","MSGRX_NUS_1","MMSRX_NUS_1","MMFRX_NUS_1","MMNRX_NUS_1","MPGRX_NUS_1"

257

,"U.S. Refinery Net Production"  

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

Monthly","9/2013","1/15/1993" Monthly","9/2013","1/15/1993" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_refp2_dc_nus_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_refp2_dc_nus_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:28:06 AM" "Back to Contents","Data 1: U.S. Refinery Net Production" "Sourcekey","MTTRX_NUS_1","MLPRX_NUS_1","METRX_NUS_1","MENRX_NUS_1","MEYRX_NUS_1","MPRRX_NUS_1","MPARX_NUS_1","MPLRX_NUS_1","MBNRX_NUS_1","MBURX_NUS_1","MBYRX_NUS_1","MBIRX_NUS_1","MIIRX_NUS_1","MIYRX_NUS_1","MGFRX_NUS_1","MGRRX_NUS_1","MG1RX_NUS_1","M_EPM0RO_YPY_NUS_MBBL","MG4RX_NUS_1","MG5RX_NUS_1","M_EPM0CAL55_YPY_NUS_MBBL","M_EPM0CAG55_YPY_NUS_MBBL","MG6RX_NUS_1","MGARX_NUS_1","MKJRX_NUS_1","M_EPJKC_YPY_NUS_MBBL","M_EPJKM_YPY_NUS_MBBL","MKERX_NUS_1","MDIRX_NUS_1","MD0RX_NUS_1","MD1RX_NUS_1","MDGRX_NUS_1","MRERX_NUS_1","MRXRX_NUS_1","MRMRX_NUS_1","MRGRX_NUS_1","MPCRX_NUS_1","MPNRX_NUS_1","MPORX_NUS_1","MNSRX_NUS_1","MLURX_NUS_1","M_EPPLN_YPY_NUS_MBBL","M_EPPLP_YPY_NUS_MBBL","MWXRX_NUS_1","MCKRX_NUS_1","MCMRX_NUS_1","MCORX_NUS_1","MAPRX_NUS_1","MSGRX_NUS_1","MMSRX_NUS_1","MMFRX_NUS_1","MMNRX_NUS_1","MPGRX_NUS_1"

258

U.S. Refinery Efficiency: Impacts Analysis and Implications for Fuel Carbon Policy Implementation  

Science Journals Connector (OSTI)

The rapid influx of domestically sourced tight light oil and relative demand shifts for gasoline and diesel will impose challenges on the ability of the U.S. refining industry to satisfy both demand and quality requirements. ... For this study Jacobs developed these models in a Generalized Refining Transportation Marketing and Planning System (GRTMPS) format (licensed by Haverly Systems) which were combined with Jacobs’ proprietary refinery technology database. ... The product slate was developed based on knowledge of the markets being served by each refinery, making use of EIA data for regional refined product output and product movements between Petroleum Administration for Defense Districts (PADDs), as well as information on product imports. ...

Grant S. Forman; Vincent B. Divita; Jeongwoo Han; Hao Cai; Amgad Elgowainy; Michael Wang

2014-05-28T23:59:59.000Z

259

Investigating and Using Biomass Gases  

K-12 Energy Lesson Plans and Activities Web site (EERE)

Students will be introduced to biomass gasification and will generate their own biomass gases. Students generate these everyday on their own and find it quite amusing, but this time they’ll do it by heating wood pellets or wood splints in a test tube. They will collect the resulting gases and use the gas to roast a marshmallow. Students will also evaluate which biomass fuel is the best according to their own criteria or by examining the volume of gas produced by each type of fuel.

260

Problem 65 in Section 4.1 (Page 274) Constructing a pipeline Supertankers off-load oil at a docking facility 4 mi offshore. The nearest refinery  

E-Print Network [OSTI]

facility 4 mi offshore. The nearest refinery is 9 mi east of the shore point nearest the docking facility. A pipeline must be constructed connecting the docking facility with the refinery. The pipeline costs $300.42 miles away from the refinery, or equivalently 3.58 miles away from Point A (as the back of the book has

Schilling, Anne

Note: This page contains sample records for the topic "liquefied refinery gases" 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

2:00-2:30 Beverages, 2:30-4 PM Seminar Chevron operates two refineries on the west coast of California. Large parcels of  

E-Print Network [OSTI]

4/18/2014 2:00-2:30 Beverages, 2:30-4 PM Seminar Abstract Chevron operates two refineries fuel must be moved between the refineries by ship to balance production. The El Segundo Marine Terminal these vapors are returned to the refinery for processing via a vapor return pipeline. El Segundo's terminal

262

Clean Gases for Gas Chromatography  

Science Journals Connector (OSTI)

......to purchase such clean gases. Even research grades...no maintenance, at the cost of 500 watts of electrical...Exploration and Production Research Division, Hous...hour. The maintenance cost of the cold trap is only...displaces the contaminated gas which has passed into......

B. Osborne Prescott; Harold L. Wise

1966-02-01T23:59:59.000Z

263

Petroleum Supply Annual  

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

1.PDF 1.PDF Table 11. PAD District 5 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 36,593 - - - - 31,429 - 4,534 890 71,666 - 0 55,877 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 2,154 -11 1,013 192 - - - -786 2,587 629 918 3,544 Pentanes Plus .................................................. 1,013 -11 - - - - - - -35 842 110 85 36 Liquefied Petroleum Gases ..............................

264

Petroleum Supply Monthly  

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

4 4 September 2013 Table 8. PAD District 1 - Year-to-Date Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 32 - - - - 843 -1 230 8 1,061 35 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 71 0 45 40 77 - - 1 16 10 205 Pentanes Plus .................................................. 12 0 - - 1 0 - - 0 0 2 9 Liquefied Petroleum Gases ..............................

265

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 3. U.S. Daily Average Supply and Disposition of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 5,877 - - - - 8,716 83 -218 14,841 53 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 2,351 -20 372 252 - - -417 566 206 2,600 Pentanes Plus .................................................. 296 -20 - - 78 - - 37 172 71 75 Liquefied Petroleum Gases .............................. 2,055 - - 372 174 - - -454 394 135 2,525

266

untitled  

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

PAD District 3 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 3,787 - - - - 4,456 -667 185 23 7,734 4 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 1,476 0 410 32 278 - - 81 299 169 1,648 Pentanes Plus .................................................. 181 0 - - 28 -45 - - -9 116 3 53 Liquefied Petroleum Gases .............................. 1,295 - - 410 4 323 - - 89 183 166

267

untitled  

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

U.S. Daily Average Supply and Disposition of Crude Oil and Petroleum Products, 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 6,486 - - - - 8,527 146 93 14,999 67 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 2,408 -18 630 170 - - 65 509 314 2,301 Pentanes Plus .................................................. 317 -18 - - 29 - - -13 174 118 50 Liquefied Petroleum Gases .............................. 2,091 - - 630 141 - - 79 335 196 2,251 Ethane/Ethylene ...........................................

268

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 5. PAD District 1 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 751 - - - - 26,471 -300 1,308 -869 28,999 100 0 9,902 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 1,313 -7 839 2,091 3,702 - - -929 816 33 8,018 7,618 Pentanes Plus .................................................. 225 -7 - - - - - - 3 - 11 204 31 Liquefied Petroleum Gases

269

Petroleum Supply Annual  

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

1. TABLE1.PDF 1. TABLE1.PDF Table 1. U.S. Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 190,109 - - - - 264,348 6,359 12,794 445,596 2,425 0 1,039,424 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 73,905 -587 13,044 6,935 - - -11,335 15,883 8,313 80,436 118,039 Pentanes Plus .................................................. 8,824 -587 - - 1,699 - - -805 4,946 2,754 3,041 16,791 Liquefied Petroleum Gases

270

Petroleum Supply Annual  

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

2.PDF 2.PDF Table 12. PAD District 5 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 1,180 - - - - 1,014 - 146 29 2,312 - 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 69 0 33 6 - - - -25 83 20 30 Pentanes Plus .................................................. 33 0 - - - - - - -1 27 4 3 Liquefied Petroleum Gases .............................. 37 - - 33 6 - - - -24 56 17 27 Ethane/Ethylene

271

Petroleum Supply Monthly  

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

September 2013 Table 1. U.S. Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 233,810 - - - - 237,344 8,334 7,688 468,825 2,975 0 1,067,149 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 81,196 -552 19,023 4,020 - - 3,027 16,794 13,937 69,929 189,672 Pentanes Plus .................................................. 11,167 -552 - - 772 - - -700 5,666 2,989 3,432 18,036 Liquefied Petroleum Gases

272

untitled  

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

PAD District 1 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 9,431 - - - - 316,140 4,126 8,393 -1,574 336,230 3,434 0 8,328 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 16,548 -84 14,202 18,043 26,704 - - -1,588 7,264 3,052 66,685 6,377 Pentanes Plus .................................................. 2,828 -84 - - 185 -19 - - 12 63 315 2,520 43 Liquefied Petroleum Gases

273

Petroleum Supply Annual  

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

January 2012 January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 190,109 - - - - 264,348 6,359 12,794 445,596 2,425 0 1,039,424 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 73,905 -587 13,044 6,935 - - -11,335 15,883 8,313 80,436 118,039 Pentanes Plus .................................................. 8,824 -587 - - 1,699 - - -805 4,946 2,754 3,041 16,791 Liquefied Petroleum Gases .............................. 65,081 - - 13,044 5,236 - - -10,530 10,937 5,559 77,395 101,248 Ethane/Ethylene

274

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 1. U.S. Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 182,188 - - - - 270,188 2,576 -6,767 460,074 1,646 0 1,026,829 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 72,869 -607 11,545 7,801 - - -12,921 17,534 6,391 80,604 128,709 Pentanes Plus .................................................. 9,170 -607 - - 2,421 - - 1,146 5,321 2,200 2,317 17,598 Liquefied Petroleum Gases

275

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 17. PAD District 4 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 12,175 - - - - 10,226 -3,426 -1,436 132 17,407 1 0 15,969 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 12,584 -10 52 460 -10,314 - - -12 611 282 1,891 1,375 Pentanes Plus .................................................. 1,788 -10 - - - -1,036 - - -15 174 273 310 180 Liquefied Petroleum Gases

276

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 15. PAD District 3 - Daily Average Supply and Disposition of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 3,327 - - - - 4,646 -720 39 -191 7,482 - 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 1,380 -1 304 84 227 - - -113 306 108 1,693 Pentanes Plus .................................................. 155 -1 - - 77 -58 - - 35 106 1 31 Liquefied Petroleum Gases ..............................

277

Petroleum Supply Monthly  

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

2 2 September 2013 Table 16. PAD District 3 - Year-to-Date Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 4,354 - - - - 3,718 -413 345 75 7,905 24 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 1,615 0 454 39 170 - - 62 282 267 1,666 Pentanes Plus .................................................. 195 0 - - 36 -65 - - 15 113 4 35 Liquefied Petroleum Gases

278

Petroleum Supply Annual  

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

TABLE9.PDF TABLE9.PDF Table 9. PAD District 4 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 12,961 - - - - 10,783 -3,879 896 2,868 17,893 0 0 18,695 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 12,770 -9 127 502 -11,116 - - -50 621 280 1,423 1,326 Pentanes Plus .................................................. 1,484 -9 - - - -1,152 - - 7 122 264 -70 187 Liquefied Petroleum Gases

279

Petroleum Supply Annual  

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

.PDF .PDF Table 3. PAD District 1 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 734 - - - - 26,368 419 -1,209 627 25,554 130 0 10,529 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 1,314 -6 923 1,606 2,621 - - -1,556 707 53 7,254 6,409 Pentanes Plus .................................................. 213 -6 - - - - - - 3 5 6 193 34 Liquefied Petroleum Gases ..............................

280

untitled  

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

U.S. Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 2,374,021 - - - - 3,120,755 53,567 34,134 5,489,516 24,693 0 1,060,764 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 881,306 -6,534 230,413 62,192 - - 23,894 186,270 115,054 842,159 153,268 Pentanes Plus .................................................. 116,002 -6,534 - - 10,680 - - -4,857 63,596 43,136 18,273 12,739 Liquefied Petroleum Gases

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Petroleum Supply Monthly  

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

September 2013 Table 4. U.S. Year-to-Date Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 7,340 - - - - 7,778 239 25 15,229 104 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 2,516 -18 716 175 - - 133 465 434 2,358 Pentanes Plus .................................................. 340 -18 - - 38 - - 20 168 134 38 Liquefied Petroleum Gases .............................. 2,176 - - 716

282

Petroleum Supply Monthly  

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

30 30 September 2013 Table 24. PAD District 5 - Year-to-Date Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 1,101 - - - - 1,091 - 115 -14 2,320 1 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 65 0 67 5 - - - 13 63 14 47 Pentanes Plus .................................................. 29 0 - - - - - - 1 21 4 3 Liquefied Petroleum Gases ..............................

283

Petroleum Supply Annual  

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

2012 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 2,374,021 - - - - 3,120,755 53,567 34,134 5,489,516 24,693 0 1,060,764 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 881,306 -6,534 230,413 62,192 - - 23,894 186,270 115,054 842,159 153,268 Pentanes Plus .................................................. 116,002 -6,534 - - 10,680 - - -4,857 63,596 43,136 18,273 12,739 Liquefied Petroleum Gases .............................. 765,304 - - 230,413 51,512 - - 28,751 122,674 71,918

284

Petroleum Supply Annual  

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

.PDF .PDF Table 2. U.S. Daily Average Supply and Disposition of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels per Day) Commodity Supply Disposition Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 6,133 - - - - 8,527 205 413 14,374 78 0 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 2,384 -19 421 224 - - -366 512 268 2,595 Pentanes Plus .................................................. 285 -19 - - 55 - - -26 160 89 98 Liquefied Petroleum Gases .............................. 2,099 - - 421 169 - - -340 353 179 2,497 Ethane/Ethylene

285

On the application of computational fluid dynamics codes for liquefied natural gas dispersion.  

SciTech Connect (OSTI)

Computational fluid dynamics (CFD) codes are increasingly being used in the liquefied natural gas (LNG) industry to predict natural gas dispersion distances. This paper addresses several issues regarding the use of CFD for LNG dispersion such as specification of the domain, grid, boundary and initial conditions. A description of the k-{var_epsilon} model is presented, along with modifications required for atmospheric flows. Validation issues pertaining to the experimental data from the Burro, Coyote, and Falcon series of LNG dispersion experiments are also discussed. A description of the atmosphere is provided as well as discussion on the inclusion of the Coriolis force to model very large LNG spills.

Luketa-Hanlin, Anay Josephine; Koopman, Ronald P. (Lawrence Livermore National Laboratory, Livermore, CA); Ermak, Donald (Lawrence Livermore National Laboratory, Livermore, CA)

2006-02-01T23:59:59.000Z

286

EVOLUTION OF THE STANDARD HELIUM LIQUEFIER AND REFRIGERATOR RANGE DESIGNED BY AIR LIQUIDE DTA, FRANCE.  

Science Journals Connector (OSTI)

The standard helium liquefier and refrigerator range called Helial and designed by Air Liquide DTA has recently been upgraded in order to improve the efficiency of these machines. Indeed over the multi-range markets requiring these cryogenic systems (international laboratories aerospace applications synchrotrons HTS applications…) the technological solution has to provide increasingly high performances. The new Helial Evolution range equipped with very reliable DTA turbo-expanders constitutes a highly efficient product for this wide application field. The optimizations adaptations and results of the Helial Evolution series doubling the performance for the same power consumption will be presented.

A. Caillaud; S. Crispel; V. Grabié; G. Aigouy

2008-01-01T23:59:59.000Z

287

Development of a Small-Scale Natural Gas Liquefier. Final Report  

SciTech Connect (OSTI)

This final report describes the progress during the contract period March 1, 1998 through April 30, 2003, on the design, development, and testing of a novel mixed-refrigerant-based 1000 gal/day natural gas liquefier, together with the associated gas cleanup equipment. Based on the work, it is concluded that a cost-effective 1000 gal/day liquefaction system is technically and economically feasible. A unit based on the same developed technology, with 5000 gal/day capacity, would have much improved economics.

Kountz, K.; Kriha, K.; Liss, W.; Perry, M.; Richards, M.; Zuckerman, D.

2003-04-30T23:59:59.000Z

288

Energy Guideline Factors Provide a Better Measure of Refinery Energy Performance  

E-Print Network [OSTI]

Exxon Company, U.S.A. refineries reduced energy consumption by 25% between 1972 and 1978 compared with an 18% reduction for the U.S. Petroleum Refining Industry over the same period. The Exxon approach to conserving energy in petroleum refining...

Libbers, D. D.

1980-01-01T23:59:59.000Z

289

Integration of Refinery Planning and Crude-Oil Scheduling using Lagrangian Decomposition  

E-Print Network [OSTI]

a large number of crude-oils, finished products such as liquified petroleum gas, gasoline, diesel fuel product blending and shipping. Some examples of nonlinear refinery planning problems including pooling, 2010 #12;crude-blends, and CDU feed charging. This problem has been addressed since the late 90s

Grossmann, Ignacio E.

290

1994 lubricating oil and wax capacities of U. S. and Canadian refineries  

SciTech Connect (OSTI)

The paper consists of several tables which list the names of US and Canadian refineries, their location, and their capacity for production of lubricating oil and waxes categorized by finishing operations and primary processing. A separate table lists US and Canadian re-refiners and their capacity for refining waste lubricating oils.

Not Available

1994-01-01T23:59:59.000Z

291

Radiation doses and hazards from processing of crude oil at the Tema oil refinery in Ghana  

Science Journals Connector (OSTI)

......petroleum products and wastes at the Tema oil refinery...radionuclides in the wastes than the crude oil and...monitoring to establish long-term effect on both public...accumulate at the bottom of storage tanks, tubings and other...uncontrolled release of waste containing TENORM, concentrated......

E. O. Darko; D. O. Kpeglo; E. H. K. Akaho; C. Schandorf; P. A. S. Adu; A. Faanu; E. Abankwah; H. Lawluvi; A. R. Awudu

2012-02-01T23:59:59.000Z

292

Operational planning of oil refineries under uncertainty Special issue: Applied Stochastic Optimization  

Science Journals Connector (OSTI)

......authors developed a general framework for the...aviation kerosene and diesel) or heavy (paraffin, lubricants, light cycle oil, gas oil, coke...1 psc = 1 . The general formulation of the...model for refinery diesel production. Comput...J. (2004) A general modeling framework......

Gabriela P. Ribas; Adriana Leiras; Silvio Hamacher

2012-10-01T23:59:59.000Z

293

Restoration of Refinery Heaters Using the Technique of Prefabricated Ceramic Fiber Lined Panels  

E-Print Network [OSTI]

Refinery heater fuel requirements often represent 50% of a units operating cost. A one percent change in the efficiency of a heater firing 100 MBtu/hr amounts to more than $25,000 per year. Heater efficiency is influenced by casing hot spots, air...

Sento, H. D.

1981-01-01T23:59:59.000Z

294

Table 39. Production Capacity of Operable Petroleum Refineries by State as of January 1, 2003  

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

State/Refiner/Location Alkylates Aromatics State/Refiner/Location Alkylates Aromatics Isobutane Lubricants Isomers Isopentane and Isohexane Asphalt and Road Oil Marketable Petroleum Coke Hydrogen (MMcfd) Sulfur (short tons per day) Table 4. Production Capacity of Operable Petroleum Refineries by State as of January 1, 2013 (Barrels per Stream Day, Except Where Noted) Isooctane a

295

Industrial Gases as a Vehicle for Competitiveness  

E-Print Network [OSTI]

the diversity and options available to enable cost savings and environmentally driven process improvements. Industrial gases have come of age during the last fifteen years. Engineers and scientists have looked beyond the paradigms of their operations...INDUSTRIAL GASES AS A VEHICLE FOR COMPETITIVENESS James R. Dale, Director, Technology Programs, Airco Industrial Gases Division, The BOC Group, Inc., Murray Hill, New Jersey ABSTRACT Industrial gases are produced using compressed air...

Dale, J. R.

296

Greenhouse Gases Converted to Fuel  

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

Greenhouse Greenhouse Gases Converted to Fuel Greenhouse Gases Converted to Fuel carbon-conversion-fig-1.jpg Key Challenges: An important strategy for reducing global CO2 emissions calls for capturing the greenhouse gas and converting it to fuels and chemicals. Although researchers working toward that goal demonstrated in 1992 such a reaction in the lab, a key outstanding scientific challenge was explaining the details of how the reaction took place - its "mechanism." Why it Matters: An important potential strategy for reducing global CO2 emissions calls for capturing the greenhouse gas and converting it electrochemically to fuels and chemicals. Accomplishments: Computation to explain how carbon dioxide can be converted to small organic molecules with little energy input. The

297

Petroleum Supply Monthly  

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

2 2 September 2013 Table 32. Blender Net Inputs of Petroleum Products by PAD District, September 2013 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Natural Gas Plant Liquids and Liquefied Refinery Gases ....................................................... 308 5 313 45 44 345 434 Pentanes Plus ...................................................... - - - - 2 75 77 Liquefied Petroleum Gases .................................. 308 5 313 45 42 270 357 Normal Butane .................................................. 308 5 313 45 42 270 357 Isobutane .......................................................... - - - - - - - Other Liquids ..........................................................

298

Petroleum Supply Annual  

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

0.PDF 0.PDF Table 20. Blender Net Inputs of Petroleum Products by PAD Districts, January 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Natural Gas Plant Liquids and Liquefied Refinery Gases ....................................................... 158 5 163 47 18 168 233 Pentanes Plus ...................................................... 5 - 5 - - 5 5 Liquefied Petroleum Gases .................................. 153 5 158 47 18 163 228 Normal Butane .................................................. 153 5 158 47 18 163 228 Isobutane .......................................................... - - - - - - - Other Liquids ..........................................................

299

untitled  

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

Blender Net Inputs of Petroleum Products by PAD Districts, 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Natural Gas Plant Liquids and Liquefied Refinery Gases ....................................................... 1,744 80 1,824 345 324 2,161 2,830 Pentanes Plus ...................................................... 63 - 63 - - 87 87 Liquefied Petroleum Gases .................................. 1,681 80 1,761 345 324 2,074 2,743 Normal Butane .................................................. 1,681 80 1,761 345 324 2,074 2,743 Isobutane .......................................................... - - - - - - - Other Liquids ..........................................................

300

Experiences in the Remediation of Ground Water Contaminated by Petroleum Hydrocarbons in the Vicinity of a Former Refinery Property  

Science Journals Connector (OSTI)

Since 1985, HPC HARRESS PICKEL CONSULT GMBH has conducted a variety of investigations on the property of a former refinery in the German Lower Rhine region, with the purpose of determining the nature and extent o...

Carsten Munk

1993-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Method for recovering power according to a cascaded rankine cycle by gasifying liquefied natural gas and utilizing the cold potential  

SciTech Connect (OSTI)

The present invention discloses a method for recovering effective energy as power between liquefied natural gas and a high temperature source by cascading two kinds of Rankine cycles when the liquefied natural gas is re-gasified. The method is characterized in that a first medium performs a first Rankine cycle with the liquefied natural gas as a low temperature source, the first medium being mainly a mixture of hydrocarbons having 1-6 carbon atoms or a mixture of halogenated hydrocarbons of boiling points close to those of said hydrocarbons, the first medium having compositions according to which the vapor curve of gasifying the liquefied natural gas substantially corresponds to the low pressure cooling curve of the first medium, the power generated thereby is recovered by a first turbine during the first Rankine cycle, a second medium having a higher boiling point than said first medium performs a second Rankine cycle with part of said first Rankine cycle as the low temperature source, the second medium, being a single hydrocarbon component having 1-6 carbon atoms or a mixture thereof, a single halogenated hydrocarbon whose boiling point is close to that of this hydrocarbon or a mixture thereof, or ammonia, whose low pressure cooling curve substantially corresponds to the vapor curve of the high pressure first medium, said first and second Rankine cycles are cascaded, and a second turbine is disposed to recover power during the second Rankine cycle.

Matsumoto, O.; Aoki, I.

1984-04-24T23:59:59.000Z

302

Reduction of corrosivity of reused water in refinery water circulating systems  

SciTech Connect (OSTI)

This paper discusses the problem of controlling scale formation in heat transfer equipment in refinery recirculating water systems. One of the effective methods for reducing the degree of pitting is acidification of the medium to pH 6-6.5, thus suppressing the activity of the sulfide and manganese inclusions in the metal that play the role of pitting centers. The authors investigated the effects of the AOC and TPP on the characteristics of refinery recirculating water and combined treatment to reduce the amount of scaling and lower the corrosivity. The untreated recirculating water was unstable; the water treated with AOC or with AOC+TPP is capable of dissolving carbonate deposits.

Sorochenko, V.F.; Beskorovainaya, N.J.; Shut'ko, A.P.; Slipchenko, O.G.; Zorina, N.E.

1985-11-01T23:59:59.000Z

303

LPG recovery from refinery flare by waste heat powered absorption refrigeration  

SciTech Connect (OSTI)

A waste heat powered ammonia Absorption Refrigeration Unit (ARU) has commenced operation at the Colorado Refining Company in Commerce City, Colorado. The ARU provides 85 tons of refrigeration at 30 F to refrigerate the net gas/treat gas stream, thereby recovering 65,000 barrels per year of LPG which formerly was flared or burned as fuel. The ARU is powered by the 290 F waste heat content of the reform reactor effluent. An additional 180 tons of refrigeration is available at the ARU to debottleneck the FCC plant wet gas compressors by cooling their inlet vapor. The ARU is directly integrated into the refinery processes, and uses enhanced, highly compact heat and mass exchange components. The refinery's investment will pay back in less than two years from increased recovery of salable product, and CO{sub 2} emissions are decreased by 10,000 tons per year in the Denver area.

Erickson, D.C.; Kelly, F.

1998-07-01T23:59:59.000Z

304

Model for Gasification of Residual Fuels from Petroleum Refineries Using the Equation Oriented (EO) Approach  

Science Journals Connector (OSTI)

An attractive way to use residual fuels from petroleum refineries (vacuum residue and petcoke) is their gasification to produce syngas, which contains mainly H2, CO and small quantities of CH4, CO2, as well as nitrogen and sulfur compounds. ... Vacuum residue and petroleum coke (petcoke) are, respectively, heavy liquid and solid byproducts from crude oil refining, they are often used as fuel in boilers for power production, natural gas has been more commonly used in the past few years in power generation; reducing the market for both vacuum residue and petcoke. ... Regarding petroleum refinery residuals Uson et al.(1) developed a model for cogasification of coal, petcoke and biomass, based on reaction kinetics. ...

Jorge E. Marin-Sanchez; Miguel A. Rodriguez-Toral

2010-07-29T23:59:59.000Z

305

Health hazard evaluation report HETA 83-248-1515, Arco Philadelphia refinery, Philadelphia, Pennsylvania  

SciTech Connect (OSTI)

A bulk sample of fractionator residue was analyzed for polynuclear aromatic (PNA) compounds at the catalytic cracking unit of ARCO Philadelphia Refinery (SIC-2911), Philadelphia, Pennsylvania in May, 1983. The study was requested by the Atlantic Independent Union to determine if skin rashes and skin irritation occurring among refinery workers were caused by PNA in the fractionators. The authors conclude that a health hazard from exposure to chemicals at the cracking unit may exist. No specific chemical agent can be identified. Dust from the catalyst and oily residues that could contaminate workers shoes and clothing may have contributed to some of the dermatitis cases. Recommendations include laundering workers coveralls by dry cleaning to insure the removal of oily residues, providing workers with oil resistant or oil proof work boots, and repairing the ventilator in the sample preparation room adjacent to the block house.

Lewis, F.A.; Parrish, G.

1984-10-01T23:59:59.000Z

306

REFINERY INTEGRATION OF BY-PRODUCTS FROM COAL-DERIVED JET FUELS  

SciTech Connect (OSTI)

This report summarizes the accomplishments toward project goals during the first six months of the project to assess the properties and performance of coal based products. These products are in the gasoline, diesel and fuel oil range and result from coal based jet fuel production from an Air Force funded program. Specific areas of progress include generation of coal based material that has been fractionated into the desired refinery cuts, acquisition and installation of a research gasoline engine, and modification of diesel engines for use in evaluating diesel produced in the project. The desulfurization of sulfur containing components of coal and petroleum is being studied so that effective conversion of blended coal and petroleum streams can be efficiently converted to useful refinery products. Equipment is now in place to begin fuel oil evaluations to assess the quality of coal based fuel oil. Coal samples have procured and are being assessed for cleaning prior to use in coking studies.

Leslie R. Rudnick; Andre Boehman; Chunshan Song; Bruce Miller; John Andresen

2004-04-23T23:59:59.000Z

307

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

SciTech Connect (OSTI)

An increasing share of natural gas supplies distributed to residential appliances in the U.S. may come from liquefied natural gas (LNG) imports. The imported gas will be of a higher Wobbe number than domestic gas, and there is concern that it could produce more pollutant emissions at the point of use. This report will review recently undertaken studies, some of which have observed substantial effects on various appliances when operated on different mixtures of imported LNG. While we will summarize findings of major studies, we will not try to characterize broad effects of LNG, but describe how different components of the appliance itself will be affected by imported LNG. This paper considers how the operation of each major component of the gas appliances may be impacted by a switch to LNG, and how this local impact may affect overall safety, performance and pollutant emissions.

Lekov, Alex; Sturges, Andy; Wong-Parodi, Gabrielle

2009-12-09T23:59:59.000Z

308

Characterization of liquefied natural gas tanker steel from cryogenic to fire temperatures.  

SciTech Connect (OSTI)

The increased demand for Liquefied Natural Gas (LNG) as a fuel source in the U.S. has prompted a study to improve our capability to predict cascading damage to LNG tankers from cryogenic spills and subsequent fire. To support this large modeling and simulation effort, a suite of experiments were conducted on two tanker steels, ABS Grade A steel and ABS Grade EH steel. A thorough and complete understanding of the mechanical behavior of the tanker steels was developed that was heretofore unavailable for the span of temperatures of interest encompassing cryogenic to fire temperatures. This was accomplished by conducting several types of experiments, including tension, notched tension and Charpy impact tests at fourteen temperatures over the range of -191 C to 800 C. Several custom fixtures and special techniques were developed for testing at the various temperatures. The experimental techniques developed and the resulting data will be presented, along with a complete description of the material behavior over the temperature span.

Dempsey, J. Franklin (Sandia National Laboratories, Albuquerque, NM); Wellman, Gerald William (Sandia National Laboratories, Albuquerque, NM); Antoun, Bonnie R.; Connelly, Kevin; Kalan, Robert J. (Sandia National Laboratories, Albuquerque, NM)

2010-03-01T23:59:59.000Z

309

Liquefied gaseous fuels safety and environmental control assessment program: third status report  

SciTech Connect (OSTI)

This Status Report contains contributions from all contractors currently participating in the DOE Liquefied Gaseous Fuels (LG) Safety and Environmental Control Assessment Program and is presented in two principal sections. Section I is an Executive Summary of work done by all program participants. Section II is a presentation of fourteen individual reports (A through N) on specific LGF Program activities. The emphasis of Section II is on research conducted by Lawrence Livermore National Laboratory (Reports A through M). Report N, an annotated bibliography of literature related to LNG safety and environmental control, was prepared by Pacific Northwest Laboratory (PNL) as part of its LGF Safety Studies Project. Other organizations who contributed to this Status Report are Aerojet Energy Conversion Company; Applied Technology Corporation; Arthur D. Little, Incorporated; C/sub v/ International, Incorporated; Institute of Gas Technology; and Massachusetts Institute of Technology. Separate abstracts have been prepared for Reports A through N for inclusion in the Energy Data Base.

Not Available

1982-03-01T23:59:59.000Z

310

The Research and Motor octane numbers of Liquefied Petroleum Gas (LPG)  

Science Journals Connector (OSTI)

This paper presents an experimental study of the Research (RON) and Motor (MON) octane numbers of Liquefied Petroleum Gas (LPG). A comprehensive set of RON and MON data for mixtures of propane, propylene (propene), n-butane and iso-butane are presented, using a method that is consistent with the currently active ASTM Research and Motor test methods for liquid fuels. Empirical models which relate LPG composition to its RON and MON are then developed, such that the simplest relationships between the constituent species’ mole fractions and the mixture octane rating are achieved. This is used to determine the degree of non-linearity between the composition and the RON and MON of different LPG mixtures. Finally, implications for LPG fuel quality standards are discussed briefly, as part of a suggested, more substantial undertaking by the community which also revisits the standard test procedures for measuring the RON and MON of LPG.

Kai J. Morganti; Tien Mun Foong; Michael J. Brear; Gabriel da Silva; Yi Yang; Frederick L. Dryer

2013-01-01T23:59:59.000Z

311

Ford Liquefied Petroleum Gas-Powered F-700 May Set Sales Records  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

he introduction in 1992 of an he introduction in 1992 of an American-made truck with a fully factory-installed/war- ranted liquefied petroleum gas (LPG) engine represents another "Ford first" in the alternative fuel arena. Now the company has introduced an LPG- powered F-700, a medium/heavy- duty truck. According to Tom Steckel, Ford's medium-duty marketing man- ager, Ford's latest sales figures already prove the alternative fuel F-700's popularity. With a little more than 10 months of the model year finished, Ford has produced 1600 units and ordered 600 more, for a total of 2200 units. That's triple the number of LPG units produced and ordered at the same time last year. In addition, the possibility of applying federal and state tax credits is being investigated. Cummins B 5.9G Natural Gas

312

Phase-equilibria for design of coal-gasification processes: dew points of hot gases containing condensible tars. Final report  

SciTech Connect (OSTI)

This research is concerned with the fundamental physical chemistry and thermodynamics of condensation of tars (dew points) from the vapor phase at advanced temperatures and pressures. Fundamental quantitative understanding of dew points is important for rational design of heat exchangers to recover sensible heat from hot, tar-containing gases that are produced in coal gasification. This report includes essentially six contributions toward establishing the desired understanding: (1) Characterization of Coal Tars for Dew-Point Calculations; (2) Fugacity Coefficients for Dew-Point Calculations in Coal-Gasification Process Design; (3) Vapor Pressures of High-Molecular-Weight Hydrocarbons; (4) Estimation of Vapor Pressures of High-Boiling Fractions in Liquefied Fossil Fuels Containing Heteroatoms Nitrogen or Sulfur; and (5) Vapor Pressures of Heavy Liquid Hydrocarbons by a Group-Contribution Method.

Prausnitz, J.M.

1980-05-01T23:59:59.000Z

313

A Case Study of Steam System Evaluation in a Petroleum Refinery  

E-Print Network [OSTI]

on Refinery's management's interest, more technical details and accurate savings & investment estimates will be provided during the Development phase that includes Basic Engineering Design & Detailed Engineering Design. ? Armstrong Service Inc. 176 ESL...-IE-03-05-21 Proceedings from theTwenty-Fifth Industrial Energy Technology Conference, Houston, TX, May 13-16, 2003 Sio-Data of Presenters: Name: Ven V. Venkatesan, Title: Director of Engineering Services Company: Armstrong Service, Inc., 8545...

Venkatesan, V. V.; Iordanova, N.

314

Decision support for integrated refinery supply chains: Part 1. Dynamic simulation  

Science Journals Connector (OSTI)

Supply chain studies are increasingly given top priority in enterprise-wide management. Present-day supply chains involve numerous, heterogeneous, geographically distributed entities with varying dynamics, uncertainties, and complexity. The performance of a supply chain relies on the quality of a multitude of design and operational decisions made by the various entities. In this two-part paper, we demonstrate that a dynamic model of an integrated supply chain can serve as a valuable quantitative tool that aids in such decision-making. In this Part 1, we present a dynamic model of an integrated refinery supply chain. The model explicitly considers the various supply chain activities such as crude oil supply and transportation, along with intra-refinery supply chain activities such as procurement planning, scheduling, and operations management. Discrete supply chain activities are integrated along with continuous production through bridging procurement, production, and demand management activities. Stochastic variations in transportation, yields, prices, and operational problems are considered in the proposed model. The economics of the refinery supply chain includes consideration of different crude slates, product prices, operation costs, transportation, etc. The proposed model has been implemented as a dynamic simulator, called Integrated Refinery In-Silico (IRIS). IRIS allows the user the flexibility to modify not only parameters, but also replace different policies and decision-making algorithms in a plug-and-play manner. It thus allows the user to simulate and analyze different policies, configurations, uncertainties, etc., through an easy-to-use graphical interface. The capabilities of IRIS for strategic and tactical decision support are illustrated using several case studies.

Suresh S. Pitty; Wenkai Li; Arief Adhitya; Rajagopalan Srinivasan; I.A. Karimi

2008-01-01T23:59:59.000Z

315

The Viscosity of Compressed Gases  

Science Journals Connector (OSTI)

New data and a new theory for the viscosity of compressed gases are presented. Data for nitrogen, hydrogen and a mixture of these gases are given, in the calculation of which, the "end effects" are not neglected as has been done in the past. Previous viscosity data are of doubtful validity owing to neglect of this factor. The theory is based on an analogy between the kinetic pressure and viscosity of a gas and is derived using an equation of state of the Lorentz type. Allowance is made for the difference between the viscosity and compressibility covolumes. The theory is substantiated experimentally and further confirmed by the recalculation of other data on the variation of Reynolds' criterion with the pressure, which is here shown to be constant. The mixture data offer a direct opportunity of comparing the Lorentz and linear rules for the calculation of the covolume of a mixture from the covolumes of the components and such comparison indicates that the Lorentz rule is not to be preferred. The substantiation of the new theory is the first direct proof of the validity of the separate treatment of the kinetic and cohesive pressures in the equation of state.

James H. Boyd; Jr.

1930-05-15T23:59:59.000Z

316

ARM - Lesson Plans: Dissolved Gases in Water  

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

released into the air, additional CO2 Would intensify an already-problematic greenhouse effect. Preparation Demonstrate that water contains invisible gases. Collect and cover...

317

Granular gases under extreme driving  

E-Print Network [OSTI]

We study inelastic gases in two dimensions using event-driven molecular dynamics simulations. Our focus is the nature of the stationary state attained by rare injection of large amounts of energy to balance the dissipation due to collisions. We find that under such extreme driving, with the injection rate much smaller than the collision rate, the velocity distribution has a power-law high energy tail. The numerically measured exponent characterizing this tail is in excellent agreement with predictions of kinetic theory over a wide range of system parameters. We conclude that driving by rare but powerful energy injection leads to a well-mixed gas and constitutes an alternative mechanism for agitating granular matter. In this distinct nonequilibrium steady-state, energy cascades from large to small scales. Our simulations also show that when the injection rate is comparable with the collision rate, the velocity distribution has a stretched exponential tail.

W. Kang; J. Machta; E. Ben-Naim

2010-02-04T23:59:59.000Z

318

Refinery Furnaces Retrofit with Gas Turbines Achieve Both Energy Savings and Emission Reductions  

E-Print Network [OSTI]

A., Rome, Italy ABSTRACT Integrating gas turbines with refinery furnaces can be a cost effective means of reducing NO emissions while also generating electricity ~t an attractive heat rate. Design considerations and system costs are presented..., described in Figure 1, 2. The combustion oxygen is carried by a more I I i I' has been used as a design basis. The heater is based on the actual design of a unit built by KTI SpA. The furnace does not include air preheater or steam generation...

Giacobbe, F.; Iaquaniello, G.; Minet, R. G.; Pietrogrande, P.

319

BLENDING PROBLEM A refinery blends four petroleum components into three grades of  

E-Print Network [OSTI]

BLENDING PROBLEM A refinery blends four petroleum components into three grades of gasoline/day $/barrel #1 5,000 $9.00 #2 2,400 7.00 #3 4,000 12.00 #4 1,500 6.00 Blending formulas and selling price 4,000 x4R + x4P + x4L 1,500 #12;blending: (1) x1R / (x1R + x2R + x3R + x4R) .40 or x1R .40(x1R

Shier, Douglas R.

320

LNG plants in the US and abroad. [Liquefied Natural Gas (LNG)  

SciTech Connect (OSTI)

The Institute of Gas Technology recently conducted a comprehensive survey of LNG production and storage facilities in North America. This survey was performed as part of IGT's LNG Observer newsletter which covers both domestic and international LNG news, reports on LNG related economics and statistics, and routinely conducts interviews with key industry leaders. In addition to providing consulting services to the LNG industry, IGT has cosponsored the International Conference on Liquefied Natural Gas for the part 20 years. The objective of this paper is to present a summary of our recent survey results as well as provide an overview of world LNG trade. This information is important in assessing the potential near term availability of LNG for transportation applications. The IGT LNG Survey appraised the capacity and current market activity of LNG peak shaving, satellite storage, and import receiving facilities in the United States and Canada. Information was requested from facilities on three main topics: liquefaction, storage, and regasification. Additional questions were posed regarding the year of operation, designer/contractor for liquefaction cycle and storage, source of LNG (for storage-only facilities), plans for expansion, and level of interest in providing LNG as a vehicle fuel. The IGT LNG Survey has to date received information on 56 LNG peak shaving facilities, 28 satellite storage facilities, and 4 LNG import receiving terminals.

Blazek, C.F.; Biederman, R.T.

1992-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Report on issues regarding the existing New York liquefied natural gas moratorium  

SciTech Connect (OSTI)

The New York Energy Planning Board has prepared this study to provide the Governor and the Legislature with information necessary to determine the need for further extension or modification of the existing State moratorium on the siting of new liquefied natural gas (LNG) facilities and intrastate transportation routes as required by Chapter 385 of the laws of 1997. The report examines existing laws and regulations that would affect new LNG facilities in New York and government initiatives in other states. It reviews existing use of LNG in New York, including safety issues and potential public concerns that may arise with lifting the moratorium. It also discusses the economic and environmental effects of increased LNG usage for New York State. The study concludes that there are economic and environmental advantages for allowing the construction of new LNG facilities as well as the intrastate transportation of LNG over new routes. Additionally, it concludes that safety concerns associated with these facilities are adequately addressed by existing Federal, State and local statutes and regulations.

NONE

1998-11-01T23:59:59.000Z

322

An investigation of the use of odorants in liquefied natural gas used as a vehicle fuel  

SciTech Connect (OSTI)

Interest in liquefied natural gas (LNG) as an alternative vehicle fuel has increased significantly. Its greater storage density relative to compressed natural gas makes it an attractive option for both volume and weight constrained vehicle applications. The public transportation market, specifically transit bus properties, have been very aggressive in pursuing LNG as an alternative vehicle fuel. Naturally, when dealing with the general public and a new transportation fuel, the issue of safety must be addressed. With this in mind, the Gas Research Institute has initiated a number of safety related studies including an investigation of the use of odorants in LNG. This paper presents the preliminary results of an investigation performed by the Institute of Gas Technology to determine both the applicability and effectiveness of odorizing LNG. This includes an overview of the current state-of-the-art in LNG vehicle fueling and safety systems as well as a discussion of an LNG odorization program conducted by San Diego Gas & Electric in the mid 70`s. Finally, the paper discusses the results of the modeling effort to determine whether conventional odorants used in natural gas can be injected and remain soluble in LNG at temperatures and pressures encountered in LNG fueling and on-board storage systems.

Green, T.; Williams, T. [Gas Research Institute, Chicago, IL (United States)

1994-12-31T23:59:59.000Z

323

Blanketing effect of expansion foam on liquefied natural gas (LNG) spillage pool  

Science Journals Connector (OSTI)

Abstract With increasing consumption of natural gas, the safety of liquefied natural gas (LNG) utilization has become an issue that requires a comprehensive study on the risk of LNG spillage in facilities with mitigation measures. The immediate hazard associated with an LNG spill is the vapor hazard, i.e., a flammable vapor cloud at the ground level, due to rapid vaporization and dense gas behavior. It was believed that high expansion foam mitigated LNG vapor hazard through warming effect (raising vapor buoyancy), but the boil-off effect increased vaporization rate due to the heat from water drainage of foam. This work reveals the existence of blocking effect (blocking convection and radiation to the pool) to reduce vaporization rate. The blanketing effect on source term (vaporization rate) is a combination of boil-off and blocking effect, which was quantitatively studied through seven tests conducted in a wind tunnel with liquid nitrogen. Since the blocking effect reduces more heat to the pool than the boil-off effect adds, the blanketing effect contributes to the net reduction of heat convection and radiation to the pool by 70%. Water drainage rate of high expansion foam is essential to determine the effectiveness of blanketing effect, since water provides the boil-off effect.

Bin Zhang; Yi Liu; Tomasz Olewski; Luc Vechot; M. Sam Mannan

2014-01-01T23:59:59.000Z

324

Retrofit design of a boil-off gas handling process in liquefied natural gas receiving terminals  

Science Journals Connector (OSTI)

Generation of Boil-off gas (BOG) in liquefied natural gas (LNG) receiving terminals considerably affects operating costs and the safety of the facility. For the above reasons, a proper BOG handling process is a major determinant in the design of a LNG receiving terminal. This study proposes the concept of a retrofit design for a BOG the handling process using a fundamental analysis. A base design was determined for a minimum send-out case in which the BOG handling becomes the most difficult. In the proposed design, the cryogenic energy of the LNG stream is used to cool other streams inside the process. It leads to a reduction in the operating costs of the compressors in the BOG handling process. Design variables of the retrofit design were optimized with non-linear programming to maximize profitability. Optimization results were compared with the base design to show the effect of the proposed design. The proposed design provides a 22.7% energy saving ratio and a 0.176 year payback period.

Chansaem Park; Kiwook Song; Sangho Lee; Youngsub Lim; Chonghun Han

2012-01-01T23:59:59.000Z

325

Analysis and optimization of cascade Rankine cycle for liquefied natural gas cold energy recovery  

Science Journals Connector (OSTI)

Abstract This study proposes a new concept called the cascade Rankine cycle, which recovers LNG (liquefied natural gas) cold energy for power generation, optimizes the cycle by investigating the effects of key parameters on its performance, and compares its thermal efficiency, exergy efficiency and economic evaluation to those of the conventional alternatives. The cascade Rankine cycle consists of multiple stages of the organic Rankine cycle in a layered structure in which the first stage encompasses the second one that, in turn, encompasses the next. Due to its layered configuration, optimization of the cycle is straightforward and involves sequentially optimizing the individual stages. Optimization of the subsequent stages, however, required process simulation considering the equipment efficiency and the thermodynamic properties of the working fluid. Process simulation indicated that the indicators such as net power output, thermal efficiency, and exergy efficiency generally increase as the number of stages increases. These indicators were, however, significantly affected by the thermodynamic properties of the working fluids. The proposed cycles demonstrated significantly better performance in these indicators than the conventional cycles. The three-stage cascade Rankine cycle with propane as the working fluid exhibited the highest net power output, thermal efficiency and exergy efficiency within the set.

In-Hwan Choi; Sangick Lee; Yutaek Seo; Daejun Chang

2013-01-01T23:59:59.000Z

326

Raman Spectra of Polyatomic Gases  

Science Journals Connector (OSTI)

Raman spectra of gaseous CO2, N2O, NH3, CH4 and C2H4 have been photographed using the line ?2536 of mercury as the exciting radiation. Vibrational transitions have been observed in all the gases investigated, and rotational transitions in the cases of NH3 and CH4. For the frequency shifts due to the vibrational transitions, the following numerical values (in cm-1) have been found: CO2: 1264.5; 1285.1; 1387.7; 1408.4.CH4: 2914.8; 3022.1; 3071.5.N2O: 1281.8C2H4: 1342.4; 1623.3; 2880.1; 3019.3; 3240.3; 3272.3.NH3: 3333.6  Raman spectra of liquid NH3 have been photographed and found to give the two frequency shifts: 3298.4 and 3214.5. In the case of gaseous NH3, pure rotational transitions lead to a moment of inertia having the value I0=2.79×10-40. In the case of methane, the positive and negative branches of the 3022.1 band lead to the value I0=5.17×10-40. The relations between these data and infra-red absorption data are discussed.

R. G. Dickinson, R. T. Dillon, and F. Rasetti

1929-08-15T23:59:59.000Z

327

PAFC fed by biogas produced by the anaerobic fermentation of the waste waters of a beet-sugar refinery  

SciTech Connect (OSTI)

Beet-washing waters of a beet-sugar refinery carry a high COD (Chemical Oxygen Demand), and their conditioning to meet legal constraints before disposal considerably contributes to the operation costs of the refinery. Their fermentation in an anaerobic digestor could instead produce readily disposable non-polluting waters, fertilizers and biogas, useful to feed a phosphoric acid fuel cell (PAFC) heat and power generator system. A real refinery case is considered in this work, where the electrical characteristics V = V(I) of a laboratory PAFC stack, fueled with a dry simulated reforming gas (having the same H{sub 2} and CO{sub 2} content as the biogas obtainable by the above said anaerobic digestion), are determined. The encouraging results show that a possible market niche for fuel cells, in the food-industry waste partial recovery and residual disposal, deserves attention.

Ascoli, A.; Elias, G. [Univ. Diegli Studi di Milano (Italy); Bigoni, L. [CISE Tecnologie Innovative S.p.A., Segrate (Italy); Giachero, R. [Du Pont Pharma Italia, Firenze (Italy)

1996-10-01T23:59:59.000Z

328

Colorado Nonhydrocarbon Gases Removed from Natural Gas (Million...  

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

Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic Feet) Colorado Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3...

329

EIA-Voluntary Reporting of Greenhouse Gases Program - What are...  

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

gases such as hydrofluorocarbons, perfluorocarbons, and sulfur hexafluoride). The Greenhouse Effect Concentrations of several important greenhouse gases have increased by about 33...

330

(Data in kilograms of germanium content, unless otherwise noted) Domestic Production and Use: The value of domestic refinery production of germanium, based on the 1996 producer  

E-Print Network [OSTI]

and Use: The value of domestic refinery production of germanium, based on the 1996 producer price. The domestic industry consisted of three germanium refineries, one each in New York, Oklahoma, and Pennsylvania, and two base metal mining operations, one in Tennessee and another in Alaska. Both of these mining

331

(Data in kilograms of germanium content, unless noted) Domestic Production and Use: The value of domestic refinery production of germanium, based on the 1995  

E-Print Network [OSTI]

: The value of domestic refinery production of germanium, based on the 1995 producer price, was approximately industry consisted of three germanium refineries, one each in New York, Oklahoma, and Pennsylvania, and a mining operation in Tennessee. The company in Tennessee exported germanium-bearing residues generated

332

EIAs Proposed NGL Realignment Statement  

Gasoline and Diesel Fuel Update (EIA)

Statement 1 Statement 1 June 7, 2013 EIA's Proposed NGL Realignment Statement Over the past five years, liquids produced by natural gas processing plants (Natural Gas Plant Liquids, NGPL) and the gas liquids produced in refineries (Liquefied Refinery Gases, LRG) have increased by more than 20 percent. These increases resulted from the development of shale gas and tight oil, as well as growth in production of liquids-rich natural gas, driven by relatively high oil prices. This growth in supply of NGPL and LRG has focused attention on the use of market terms such as natural gas liquids (NGL) and liquefied petroleum gases (LPG). In a recent review of these terms and more than a dozen related definitions, the Energy Information Administration (EIA) found a

333

untitled  

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

Refinery and Blender Net Input of Crude Oil and Petroleum Products by PAD and Refining Districts, 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Crude Oil ................................................................. 302,582 33,648 336,230 808,927 164,619 286,280 1,259,826 Natural Gas Plant Liquids and Liquefied Refinery Gases ....................................................... 7,184 80 7,264 25,975 1,308 11,193 38,476 Pentanes Plus ...................................................... 63 - 63 7,891 53 3,375 11,319 Liquefied Petroleum Gases .................................. 7,121 80 7,201 18,084 1,255 7,818

334

Petroleum Supply Monthly  

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

4 4 September 2013 Table 28. Refinery and Blender Net Input of Crude Oil and Petroleum Products by PAD and Refining Districts, September 2013 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Crude Oil ................................................................. 29,611 2,906 32,517 67,983 12,033 22,460 102,476 Natural Gas Plant Liquids and Liquefied Refinery Gases ....................................................... 793 5 798 2,014 100 1,032 3,146 Pentanes Plus ...................................................... - - - 777 2 340 1,119 Liquefied Petroleum Gases .................................. 793 5 798 1,237 98 692 2,027

335

Achieving very low mercury levels in refinery wastewater by membrane filtration.  

SciTech Connect (OSTI)

Microfiltration (MF), ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO) membranes were evaluated for their ability to achieve the world's most stringent Hg discharge criterion (<1.3 ng/L) in an oil refinery's wastewater. The membrane processes were operated at three different pressures to demonstrate the potential for each membrane technology to achieve the targeted effluent mercury concentrations. The presence of mercury in the particulate form in the refinery wastewater makes the use of MF and UF membrane technologies more attractive in achieving very low mercury levels in the treated wastewater. Both NF and RO were also able to meet the target mercury concentration at lower operating pressures (20.7 bar). However, higher operating pressures ({ge}34.5 bar) had a significant effect on NF and RO flux and fouling rates, as well as on permeate quality. SEM images of the membranes showed that pore blockage and narrowing were the dominant fouling mechanisms for the MF membrane while surface coverage was the dominant fouling mechanism for the other membranes. The correlation between mercury concentration and particle size distribution was also investigated to understand mercury removal mechanisms by membrane filtration. The mean particle diameter decreased with filtration from 1.1 {+-} 0.0 {micro}m to 0.74 {+-} 0.2 {micro}m after UF.

Urgun Demirtas, M.; Benda, P.; Gillenwater, P. S.; Negri, M. C.; Xiong, H.; Snyder, S. W. (Center for Nanoscale Materials); ( ES)

2012-05-15T23:59:59.000Z

336

Forecast of U. S. Refinery Demand for NGL's (natural gas liquids) in 1978-1985  

SciTech Connect (OSTI)

A forecast of U.S. Refinery Demand for NGL's (Natural Gas Liquids) in 1978-1985 is based on a predicted 1.4%/yr decline in motor gasoline consumption from 7.4 to 6.7 million bbl/day (Mbd), including a 2.6%/yr reduction from 5.3 to 4.4 Mbd for automobiles and a 1.3%/yr growth from 2.1 to 2.3 Mbd for trucks, because of slow growth rates in the U.S. automobile fleet (1.1%/yr) and average annual miles driven (0.9%/yr), a 3.9%/yr growth in average mileage from 14.2 to 18.6 mpg, and diesel penetration to the automobile market which should increase from 0.3 to 3.3%. Leaded gasoline's share is expected to decline from 68% of the market (5.1 Mbd, including 0.8 Mbd leaded premium) to 24% (1.7 Mbd, leaded regular only), including a drop from 56 to 6% for automobiles and from approx. 100 to 60% for trucks. This will require increased production of clean-octane reformates and alkylates and reduce the need for straight-run gasolines, but because of the decline in the total gasoline demand, these changes should be minimal. Butane demand from outside-refinery production should decrease by 5-6%/yr, and natural gasoline will be consumed according to available production as an isopentane source.

Laskosky, J.

1980-01-01T23:59:59.000Z

337

Using Relative Risk Analysis to Set Priorities For Pollution Prevention At A Petroleum Refinery  

Science Journals Connector (OSTI)

Publisher Summary This chapter outlines the development of a detailed refinery release inventory that identifies sources and quantities of releases. It identifies options for preventing releases and minimizing health and environmental risks and discusses a system for evaluating and ranking the options in light of cost, risk, regulatory requirements, and other factors. The chapter also describes the methods of evaluating the incentives and obstacles to implementing the pollution prevention options. The chapter highlights the progress that can occur in identifying creative, cost-effective options for pollution prevention when government, industry, and the public establish partnerships rather than operate as adversaries. Pollution prevention cannot be adequately implemented or monitored for effectiveness unless facility operators and regulators know what is being released from the facility and its origin. Government regulatory systems—such as those established by the Clean Water Act or Resource Conservation and Recovery Act (RCRA)—require refineries and other facilities to monitor and measure releases from a few specific points, such as the end of a discharge pipe, or in specific media, such as groundwater. To bridge the gaps in existing data, a multimedia sample collection and analysis effort needs to be undertaken.

Ronald E. Schmitt; Howard Klee; Debora M. Sparks; Mahesh K. Podar

1998-01-01T23:59:59.000Z

338

Apparatus and process for the refrigeration, liquefaction and separation of gases with varying levels of purity  

DOE Patents [OSTI]

A process for the separation and liquefaction of component gasses from a pressurized mix gas stream is disclosed. The process involves cooling the pressurized mixed gas stream in a heat exchanger so as to condensing one or more of the gas components having the highest condensation point; separating the condensed components from the remaining mixed gas stream in a gas-liquid separator; cooling the separated condensed component stream by passing it through an expander; and passing the cooled component stream back through the heat exchanger such that the cooled component stream functions as the refrigerant for the heat exchanger. The cycle is then repeated for the remaining mixed gas stream so as to draw off the next component gas and further cool the remaining mixed gas stream. The process continues until all of the component gases are separated from the desired gas stream. The final gas stream is then passed through a final heat exchanger and expander. The expander decreases the pressure on the gas stream, thereby cooling the stream and causing a portion of the gas stream to liquify within a tank. The portion of the gas which is hot liquefied is passed back through each of the heat exchanges where it functions as a refrigerant.

Bingham, Dennis N. (Idaho Falls, ID); Wilding, Bruce M. (Idaho Falls, ID); McKellar, Michael G. (Idaho Falls, ID)

2002-01-01T23:59:59.000Z

339

Comparing greenhouse gases for policy purposes  

E-Print Network [OSTI]

In order to derive optimal policies for greenhouse gas emissions control, the discounted marginal damages of emissions of different gases must be compared. The greenhouse warming potential (GWP) index, which is most often ...

Schmalensee, Richard

1993-01-01T23:59:59.000Z

340

Voluntary reporting of greenhouse gases, 1995  

SciTech Connect (OSTI)

The Voluntary Reporting Program for greenhouse gases is part of an attempt by the U.S. Government to develop innovative, low-cost, and nonregulatory approaches to limit emissions of greenhouse gases. It is one element in an array of such programs introduced in recent years as part of the effort being made by the United States to comply with its national commitment to stabilize emissions of greenhouse gases under the Framework Convention on Climate Change. The Voluntary Reporting Program, developed pursuant to Section 1605(b) of the Energy Policy Act of 1992, permits corporations, government agencies, households, and voluntary organizations to report to the Energy Information Administration (EIA) on actions taken that have reduced or avoided emissions of greenhouse gases.

NONE

1996-07-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Gases for an SSC muon detector  

SciTech Connect (OSTI)

Recent measurements of electron drift velocities as a function of the density-reduced electric field E/N are reported for a number of unitary gases and the mixtures CO{sub 2}/CH{sub 4} and NH{sub 3}/CF{sub 4}/Ar. Calculated values of the mean electron energy as a function of E/N are also reported for unitary gases and mixtures of CO{sub 2}/CH{sub 4}. 7 refs., 5 figs.

Christophorou, L.G.; Datskos, P.G.; Carter, J.G. (Oak Ridge National Lab., TN (USA) Tennessee Univ., Knoxville, TN (USA). Dept. of Physics and Astronomy)

1990-01-01T23:59:59.000Z

342

THE FUTURE OF ENERGY GASES David G. Howell, Editor  

E-Print Network [OSTI]

totally independent of oil. Methane is found in association with coal; it is a byproduct of metabolic the term "energy gases" to distinguish those natural gases, primarily methane, that have utility for energy consequences associated with an expanded role of energy gases? Energy gases, particularly methane, are commonly

343

Measuring the Isotopic Composition of Solar Wind Noble Gases  

E-Print Network [OSTI]

noble gases. #12;Exploring the Solar Wind94 Light solar wind noble gases were directly measured by mass of the light gases are known to vary with energy, so none of these provided solar isotopic and elemental5 Measuring the Isotopic Composition of Solar Wind Noble Gases Alex Meshik, Charles Hohenberg, Olga

344

Petroleum Supply Annual  

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

9.PDF 9.PDF Table 19. Refinery Net Production of Finished Petroleum Products by PAD and Refining Districts, January 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Liquefied Refinery Gases ......................................... 952 -29 923 1,600 -77 -190 1,333 Ethane/Ethylene ................................................... 3 - 3 - - - - Ethane .............................................................. - - - - - - - Ethylene ............................................................ 3 - 3 - - - - Propane/Propylene ............................................... 1,175 20 1,195 2,531 316 621 3,468 Propane ............................................................

345

Petroleum Supply Monthly  

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

6 6 September 2013 Table 29. Refinery and Blender Net Production of Finished Petroleum Products by PAD and Refining Districts, September 2013 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Liquefied Refinery Gases ......................................... 719 28 747 2,872 146 444 3,462 Ethane/Ethylene ................................................... 9 - 9 - - - - Ethane .............................................................. - - - - - - - Ethylene ............................................................ 9 - 9 - - - - Propane/Propylene ............................................... 1,050 28 1,078 2,342 225 544 3,111 Propane

346

TABLE17.CHP:Corel VENTURA  

Gasoline and Diesel Fuel Update (EIA)

7. 7. Refinery Net Production of Finished Petroleum Products by PAD and Refining Districts, January 1998 Liquefied Refinery Gases ........................................... 576 -7 569 2,415 -51 392 2,756 Ethane/Ethylene ..................................................... 0 0 0 0 0 0 0 Ethane ............................................................... W W W W W W W Ethylene ............................................................ W W W W W W W Propane/Propylene ................................................ 1,656 33 1,689 2,645 329 628 3,602 Propane ............................................................. W W W 1,979 W W W Propylene .......................................................... W W W 666 W W W Normal Butane/Butylene ........................................ -804 -39 -843 -320 -337 -180 -837 Normal Butane ..................................................

347

Petroleum Supply Annual  

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

7.PDF 7.PDF Table 17. Refinery and Blender Net Production of Finished Petroleum Products by PAD and Refining Districts, January 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Liquefied Refinery Gases ......................................... 952 -29 923 1,600 -77 -190 1,333 Ethane/Ethylene ................................................... 3 - 3 - - - - Ethane .............................................................. - - - - - - - Ethylene ............................................................ 3 - 3 - - - - Propane/Propylene ............................................... 1,175 20 1,195 2,531 316 621 3,468 Propane ............................................................

348

Petroleum Supply Monthly  

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

40 40 September 2013 Table 31. Refinery Net Production of Finished Petroleum Products by PAD and Refining Districts, September 2013 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Liquefied Refinery Gases ......................................... 719 28 747 2,872 146 444 3,462 Ethane/Ethylene ................................................... 9 - 9 - - - - Ethane .............................................................. - - - - - - - Ethylene ............................................................ 9 - 9 - - - - Propane/Propylene ............................................... 1,050 28 1,078 2,342 225 544 3,111 Propane ............................................................

349

EIA - Annual Energy Outlook 2014 Early Release  

Gasoline and Diesel Fuel Update (EIA)

Acronyms Acronyms List of Acronyms AEO Annual Energy Outlook LDV Light-duty vehicle AEO2013 Annual Energy Outlook 2013 LED Light emitting diode AEO20014 Annual Energy Outlook 2014 LNG Liquefied natural gas ATRA American Taxpayer Relief Act of 2012 LPG Liquefied petroleum gases bbl Barrels LRG Liquefied refinery gases Btu British thermal units MATS Mercury and Air Toxics Standards CAFE Corporate Average Fuel Economy MECS Manufacturing Energy Consumption Survey CAIR Clean Air Interstate Rule MMbbl/d Million barrels per day CO2 Carbon dioxide MMBtu Million Btu CTL Coal-to-liquids MMst Million short tons DOE U.S. Department of Energy NEMS National Energy Modeling System E85 Motor fuel containing up to 85% ethanol NGL Natural gas liquids

350

,"Price of U.S. Liquefied Natural Gas Imports From Egypt (Dollars per Thousand Cubic Feet)"  

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

Egypt (Dollars per Thousand Cubic Feet)" Egypt (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Egypt (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103eg3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103eg3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

351

,"Price of U.S. Liquefied Natural Gas Imports From Nigeria (Dollars per Thousand Cubic Feet)"  

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

Nigeria (Dollars per Thousand Cubic Feet)" Nigeria (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Nigeria (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103ng3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103ng3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

352

,"Price of U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per Thousand Cubic Feet)"  

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

Indonesia (Dollars per Thousand Cubic Feet)" Indonesia (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Indonesia (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103id3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103id3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

353

,"Price of U.S. Liquefied Natural Gas Imports From Malaysia (Dollars per Thousand Cubic Feet)"  

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

Malaysia (Dollars per Thousand Cubic Feet)" Malaysia (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Malaysia (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103my3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103my3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

354

,"Price of U.S. Liquefied Natural Gas Imports From Australia (Dollars per Thousand Cubic Feet)"  

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

Australia (Dollars per Thousand Cubic Feet)" Australia (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Australia (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103au3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103au3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

355

,"Price of U.S. Liquefied Natural Gas Imports From Qatar (Dollars per Thousand Cubic Feet)"  

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

Qatar (Dollars per Thousand Cubic Feet)" Qatar (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Qatar (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103qr3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103qr3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

356

,"Price of U.S. Liquefied Natural Gas Imports From Brunei (Dollars per Thousand Cubic Feet)"  

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

Brunei (Dollars per Thousand Cubic Feet)" Brunei (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Brunei (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103bx3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103bx3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

357

,"Price of U.S. Liquefied Natural Gas Imports From Oman (Dollars per Thousand Cubic Feet)"  

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

Oman (Dollars per Thousand Cubic Feet)" Oman (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Oman (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103mu3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103mu3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

358

Purchase, Delivery, and Storage of Gases  

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

Purchase, Delivery, and Storage of Gases Print Purchase, Delivery, and Storage of Gases Print ALS users should follow Berkeley Lab policy, as described below, for the purchase, delivery, storage, and use of all gases at the ALS. See Shipping and Receiving for information on any non-gas deliveries. Contacts: Gas purchase or delivery: ALS Receiving, 510-486-4494 Gas use and storage: Experiment Coordination, 510-486-7222, This e-mail address is being protected from spambots. You need JavaScript enabled to view it Gas Storage: Berkeley Lab Chemical Inventory All gas bottles and cylinders at the ALS must be identified with bar code and logged into the Berkeley Lab Chemical Inventory by ALS staff. The inventory will be updated periodically; for more information contact Experiment Coordination. Gases are stored either in the racks between buildings 6 and 7; toxic and corrosive gases are stored in Building 6, room 6C across the walkway from beamline 10.0.

359

Market Assessment of Refinery Outages Planned for October 2010 through January 2011  

Gasoline and Diesel Fuel Update (EIA)

10)/2 10)/2 Market Assessment of Refinery Outages Planned for October 2010 through January 2011 November 2010 Energy Information Administration Office of Petroleum, Gas, and Biofuels Analysis U.S. Department of Energy Washington, DC 20585 This report was prepared by the U.S. Energy Information Administration (EIA), the statistical and analytical agency within the U.S. Department of Energy. By law, EIA's data, analyses, and forecasts are independent of approval by any other officer or employee of the United States Government. The views in this report therefore should not be construed as representing those of the Department of Energy or other Federal agencies. E nergy Information Adminis tration Market As s es s ment of P lanned R

360

Market Assessment of Refinery Outages Planned for October 2009 through January 2010  

Gasoline and Diesel Fuel Update (EIA)

09)/2 09)/2 Market Assessment of Refinery Outages Planned for October 2009 through January 2010 November 2009 Energy Information Administration Office of Oil and Gas U.S. Department of Energy Washington, DC 20585 This report was prepared by the U.S. Energy Information Administration (EIA), the independent statistical and analytical agency within the U.S. Department of Energy. By law, EIA's data, analyses, and forecasts are independent of approval by any other officer or employee of the United States Government. The views herein should not be construed as representing those of the Department or the Administration. Preface and Contacts The Energy Information Administration (EIA) is the independent statistical and analytical

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Bio-char refineries: an accessible approach for the development of biomass-based industry  

Science Journals Connector (OSTI)

Being a by-product of the well-established charcoal industry, slow pyrolysis bio-oil can be an excellent, cost-effective and renewable liquid fuel. However, even in Brazil, a country with a very clean energy profile and large-scale charcoal production, bio-oil is not properly utilised yet. A simple upgrade of traditional methods of charcoal production can significantly increase liquid fuel output. The concept of a bio-char-refinery, introduced in this paper, for production of charcoal, activated carbon, liquid fuel and variety of chemicals presents a possible approach for the development of biomass-based industry. Successful implementation of this concept could provide significant amounts of fuel and chemicals able to enhance economic development and reduce the consumption of petroleum derived products.

Venelin Stamatov; Jose Dilcio Rocha

2007-01-01T23:59:59.000Z

362

Standard guide for evaluating and qualifying oilfield and refinery corrosion inhibitors in the laboratory  

E-Print Network [OSTI]

1.1 This guide covers some generally accepted laboratory methodologies that are used for evaluating corrosion inhibitors for oilfield and refinery applications in well defined flow conditions. 1.2 This guide does not cover detailed calculations and methods, but rather covers a range of approaches which have found application in inhibitor evaluation. 1.3 Only those methodologies that have found wide acceptance in inhibitor evaluation are considered in this guide. 1.4 This guide is intended to assist in the selection of methodologies that can be used for evaluating corrosion inhibitors. 1.5 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory requirements prior to use.

American Society for Testing and Materials. Philadelphia

2006-01-01T23:59:59.000Z

363

Classification of bacterial isolates of the Jordanian oil refinery petroleum sludge  

Science Journals Connector (OSTI)

The aim of this study is to characterise the bacterial isolates of Jordanian oil refinery sludge for the purpose of using microorganisms in treating industrial wastewater effluents that contains hydrocarbons. Morphological, physiological, biochemical, antimicrobial susceptibility tests and 16S-23S rRNA spacer region polymorphism were used to characterise the isolated thermotolerant Bacillus, with specific reference to Bacillus strains. Data were coded and analysed by numerical techniques using the Gower coefficients and by average linkage (UPGMA) analysis. The study resulted in allocation of strains into two areas at 50.0% similarity levels and ten major phenons at 78.0% similarity level. Amplification of 16S-32S rRNA genes divided all strains into two areas at 48.0% similarity level; however, at 78.0% similarity level five taxonomically distinct phenons were evident.

Mohammed N. Battikhi; Bassam Mrayyan; Manar Atoum

2009-01-01T23:59:59.000Z

364

Reformulated Gasoline Foreign Refinery Rules (Released in the STEO January 1998)  

Reports and Publications (EIA)

On August 27, 1997, the Environmental Protection Agency (EPA) promulgated revised the rules that allow foreign refiners to establish and use individual baselines, but it would not be mandatory (the optional use of an individual refinery baseline is not available to domestic refiners.) If a foreign refiner did not establish and use an individual baseline, the gasoline they export to the United States would be regulated through the importer, and subject to the importer's baseline (most likely the statutory baseline). Specific regulatory provisions are implemented to ensure that the option to use an individual baseline would not lead to adverse environmental impacts. This involves monitoring the average quality of imported gasoline, and if a specified benchmark is exceeded, remedial action would be taken by adjusting the requirements applicable to imported gasoline.

1998-01-01T23:59:59.000Z

365

Integrity management of a HIC-damaged pipeline and refinery pressure vessel through hydrogen permeation measurements  

SciTech Connect (OSTI)

Hydrogen permeation measurements were used in the successful operation of a sour gas pipeline subsequent to a hydrogen-induced cracking (HIC) failure in September 1992. Two joints of HIC-resistant pipe were used to repair the failed section and adjacent cut-outs. The pipeline has been operated for five years with no further instances of HIC failure. Hydrogen permeation monitoring was chosen as an integrity management tool because no techniques are currently available to inspect for HIC damage in a pipeline this size. Self-powered electrochemical devices installed on the pipeline were employed to monitor and control the effectiveness of a batch inhibition program in maintaining diffusing hydrogen atom concentrations below the laboratory-measured threshold for initiation of HIC damage. Permeation monitoring of a HIC-damaged refinery pressure vessel indicated very high hydrogen atom flux, despite attempts to inhibit corrosion with ammonium polysulfide injection. In this instance it was decided that replacement of the vessel was necessary.

Hay, M.G.; Rider, D.W. [Shell Canada Ltd., Calgary, Alberta (Canada)

1998-12-31T23:59:59.000Z

366

BIO?REFINERIES: BIOPROCESS TECHNOLOGIES FOR WASTE?WATER TREATMENT, ENERGY AND PRODUCT VALORIZATION  

Science Journals Connector (OSTI)

Increasing pressure is being exerted on communities and nations to source energy from forms other than fossil fuels. Also potable water is becoming a scarce resource in many parts of the world and there remains a large divide in the demand and utilization of plant products derived from genetically modified organisms (GMOs) and non?GMOs. The most extensive user and manager of terrestrial ecosystems is agriculture which is also the de facto steward of natural resources. As stated by Miller (2008) no other industry or institution comes close to the comparative advantage held for this vital responsibility while simultaneously providing food fiber and other biology?based products including energy. Since modern commercial agriculture is transitioning from the production of bulk commodities to the provision of standardized products and specific?attribute raw materials for differentiated markets we can argue that processes such as mass cultivation of microalgae and the concept of bio?refineries be seen as part of a ‘new’ agronomy. EBRU is currently exploring the integration of bioprocess technologies using microalgae as biocatalysts to achieve waste?water treatment water polishing and endocrine disruptor (EDC) removal sustainable energy production and exploitation of the resultant biomass in agriculture as foliar fertilizer and seed coatings and for commercial extraction of bulk commodities such as bio?oils and lecithin. This presentation will address efforts to establish a fully operational solar?driven microalgae bio?refinery for use not only in waste remediation but to transform waste and biomass to energy fuels and other useful materials (valorisation) with particular focus on environmental quality and sustainability goals.

A. Keith Cowan

2010-01-01T23:59:59.000Z

367

Soot and SO[subscript 2] contribution to the supersites in the MILAGRO campaign from elevated flares in the Tula Refinery  

E-Print Network [OSTI]

This work presents a simulation of the plume trajectory emitted by flaring activities of the Miguel Hidalgo Refinery in Mexico. The flame of a representative sour gas flare is modeled with a CFD combustion code in order ...

Molina, Luisa Tan

368

Chemical Properties of the Rare Gases  

Science Journals Connector (OSTI)

... of argon of about 100 atm. I have already shown by an independent method1 that radon, too, forms a hydrate which is much more stable than those of other rare ... , forms a hydrate which is much more stable than those of other rare gases. Radon is easily held by crystals of sulphur dioxide hydrates, when they are formed from ...

B. A. NIKITIN

1937-10-09T23:59:59.000Z

369

New instruments for measuring landfill gases  

Science Journals Connector (OSTI)

New instruments for measuring landfill gases ... The legislation mandates that landfill operators monitor more than 1200 active sites for specific pollution products. ... According to Varian, the instrumentation systems can be adapted easily to meet landfill testing requirements that might be enacted in states other than California. ...

RUDY BAUM

1988-02-01T23:59:59.000Z

370

PEMEX selects the H-Oil{reg_sign} process for their hydrodesulfurization residue complex at the Miguel Hidalgo Refinery  

SciTech Connect (OSTI)

Petroleos Mexicanos (PEMEX) has selected the H-Oil Process for the conversion and upgrading of a blend of Maya and Isthmus vacuum residua at the Miguel Hidalgo Refinery. The 8,450 metric ton/day (50,000 bpsd) H-Oil Plant will produce a low sulfur (0.8 wt%) fuel oil, diesel, naphtha, and LPG. The H-Oil Plant will be a key component of the Hydrodesulfurization Residue (HDR) Complex which will be located at the Miguel Hidalgo Refinery in Tula, State of Hidalgo, Mexico. The project is part of PEMEX`s Ecology Projects currently underway in Mexico. This paper describes the HDR Complex and the design basis of the H-Oil Plant and provides the current status of this project.

Wisdom, L.I.; Colyar, J.J. [Hydrocarbon Research, Inc., Princeton, NJ (United States)

1995-12-31T23:59:59.000Z

371

amount of CO2 ice in a martian polar cap can be set by the condition that it not liquefy at its base as a  

E-Print Network [OSTI]

amount of CO2 ice in a martian polar cap can be set by the condition that it not liquefy at its-particle irradiation experiments with 2.5% H2O in CH4-NH3 atmospheres, organic sol- ids are also plentifully produced

Capone, Douglas G.

372

Refinery Waste Heat Ammonia Absorption Refrigeration Plant (WHAARP) Recovers LPG's and Gasoline, Saves Energy, and Reduces Air Pollution  

E-Print Network [OSTI]

Refinery Waste Heat Ammonia Absorption Refrigeration Plant (WHAARp?) Recovers LPG's and Gasoline, Saves Energy, and Reduces Air Pollution Benjamin Brant Sabine Brueske Donald Erickson Riyaz Papar Planetec Planetec Energy Concepts Company Energy... in Denver, Colorado. The Waste Heat Ammo nia Absorption Refrigeration Plant (WHAARP?) is based on a patented process and cycle design developed by Energy Concepts Co. (ECC) to cost effectively re cover 73,000 barrels a year of salable LPGs and gasoline...

Brant, B.; Brueske, S.; Erickson, D.; Papar, R.

373

Gas Cleaning Methods for Ambient Air and Compressed Gases  

Science Journals Connector (OSTI)

Cleaning air or compressed gases in cleanroom installations requires removal of particulate and/or ... The technology used for cleaning gases for the cleanroom is derived from processes long used in ... fossil fu...

Alvin Lieberman

1992-01-01T23:59:59.000Z

374

Perdido LF-Gase to Electricity | Department of Energy  

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

Perdido LF-Gase to Electricity Perdido LF-Gase to Electricity This presentation was given at the July 17, 2012, Community Renewable Energy Deployment webinar on successful landfill...

375

BOC Lienhwa Industrial Gases BOCLH | Open Energy Information  

Open Energy Info (EERE)

BOC Lienhwa Industrial Gases BOCLH BOC Lienhwa Industrial Gases BOCLH Jump to: navigation, search Name BOC Lienhwa Industrial Gases (BOCLH) Place Taipei, Taiwan Sector Solar Product BOCLH is a joint venture between the Lien Hwa Industrial Corporation and the BOC Group in the United Kingdom and produces high-purity gases used in solar component production. References BOC Lienhwa Industrial Gases (BOCLH)[1] LinkedIn Connections CrunchBase Profile No CrunchBase profile. Create one now! This article is a stub. You can help OpenEI by expanding it. BOC Lienhwa Industrial Gases (BOCLH) is a company located in Taipei, Taiwan . References ↑ "BOC Lienhwa Industrial Gases (BOCLH)" Retrieved from "http://en.openei.org/w/index.php?title=BOC_Lienhwa_Industrial_Gases_BOCLH&oldid=342956

376

Economic and European Union Environmental Sustainability Criteria Assesment of Bio-Oil-Based Biofuel Systems: Refinery Integration Cases  

Science Journals Connector (OSTI)

Between bio-oil gasification and upgrading routes in Figure 2, the former route comprises of proven technologies and “can be commercially deployable by industrial companies with infrastructure and expertise available to produce marketable products”. ... For the scenario with all hydrogen sold by the refinery, (61.5 + 20.67) kmol/t of bio-oil at the market rate of 1200 $/t and stable oil sold by the upgrader to the refinery at the market rate of 490 $/t, 141.8 $/t or 19.8 $/bbl of crude oil of economic incentive from the selling of all the hydrogen and 39.3 $/t or 3.3 $/bbl of crude oil of economic incentive from the replacement of final biodiesel blending by the renewable diesel production from the stable oil coprocessing are obtained. ... Given the volatile and vulnerable petroleum markets, oil companies are under pressure for moving toward a greener future, within which refinery expansion strategy may be a commonplace. ...

Jhuma Sadhukhan; Kok Siew Ng

2011-04-19T23:59:59.000Z

377

Method for enhancing microbial utilization rates of gases using perfluorocarbons  

DOE Patents [OSTI]

A method of enhancing the bacterial reduction of industrial gases using perfluorocarbons (PFCs) is disclosed. Because perfluorocarbons (PFCs) allow for a much greater solubility of gases than water does, PFCs have the potential to deliver gases in higher concentrations to microorganisms when used as an additive to microbial growth media thereby increasing the rate of the industrial gas conversion to economically viable chemicals and gases.

Turick, Charles E. (Idaho Falls, ID)

1997-01-01T23:59:59.000Z

378

,"Price of U.S. Liquefied Natural Gas Imports From Canada (Dollars per Thousand Cubic Feet)"  

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

Canada (Dollars per Thousand Cubic Feet)" Canada (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Canada (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_nus-nca_pml_dmcfm.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_nus-nca_pml_dmcfm.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

379

,"Price of U.S. Liquefied Natural Gas Imports From Norway (Dollars per Thousand Cubic Feet)"  

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

Norway (Dollars per Thousand Cubic Feet)" Norway (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Norway (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_nus-nno_pml_dmcfm.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_nus-nno_pml_dmcfm.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

380

,"Price of U.S. Liquefied Natural Gas Imports From Yemen (Dollars per Thousand Cubic Feet)"  

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

Yemen (Dollars per Thousand Cubic Feet)" Yemen (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Yemen (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_pml_nus-nye_dmcfm.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_pml_nus-nye_dmcfm.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Study of integrated metal hydrides heat pump and cascade utilization of liquefied natural gas cold energy recovery system  

Science Journals Connector (OSTI)

The traditional cold energy utilization of the liquefied natural gas system needs a higher temperature heat source to improve exergy efficiency, which barricades the application of the common low quality thermal energy. The adoption of a metal hydride heat pump system powered by low quality energy could provide the necessary high temperature heat and reduce the overall energy consumption. Thus, an LNG cold energy recovery system integrating metal hydride heat pump was proposed, and the exergy analysis method was applied to study the case. The performance of the proposed integration system was evaluated. Moreover, some key factors were also theoretically investigated about their influences on the system performance. According to the results of the analysis, some optimization directions of the integrated system were also pointed out.

Xiangyu Meng; Feifei Bai; Fusheng Yang; Zewei Bao; Zaoxiao Zhang

2010-01-01T23:59:59.000Z

382

,"Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant Stocks"  

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

Monthly","9/2013","1/15/1993" Monthly","9/2013","1/15/1993" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_stoc_st_a_epm0f_str_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_st_a_epm0f_str_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:32:19 AM" "Back to Contents","Data 1: Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant Stocks" "Sourcekey","MGFSXUS1","MGFSXP11","MGFSXCT1","MGFS3_SDE_1","MGFSXFL1","MGFSXGA1","MGFS3_SME_1","MGFS3_SMD_1","MGFSXMA1","MGFS3_SNH_1","MGFSXNJ1","MGFSXNY1","MGFSXNC1","MGFSXPA1","MGFSXRI1","MGFSXSC1","MGFS3_SVT_1","MGFSXVA1","MGFSXWV1","MGFSXP21","MGFSXIL1","MGFSXIN1","MGFSXIA1","MGFS3_SKS_1","MGFSXKY1","MGFSXMI1","MGFSXMN1","MGFSXMO1","MGFS3_SNE_1","MGFS3_SND_1","MGFSXOH1","MGFSXOK1","MGFS3_SSD_1","MGFSXTN1","MGFSXWI1","MGFSXP31","MGFSXAL1","MGFSXAR1","MGFSXLA1","MGFSXMS1","MGFSXNM1","MGFSXTX1","MGFSXP41","MGFSXCO1","MGFSXID1","MGFSXMT1","MGFSXUT1","MGFSXWY1","MGFSXP51","MGFSXAK1","MGFSXAZ1","MGFSXCA1","MGFSXHI1","MGFSXNV1","MGFSXOR1","MGFSXWA1"

383

,"Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant Stocks"  

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

Annual",2012,"6/30/1993" Annual",2012,"6/30/1993" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_stoc_st_a_epm0f_str_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_st_a_epm0f_str_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:32:18 AM" "Back to Contents","Data 1: Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant Stocks" "Sourcekey","MGFSXUS1","MGFSXP11","MGFSXCT1","MGFS3_SDE_1","MGFSXFL1","MGFSXGA1","MGFS3_SME_1","MGFS3_SMD_1","MGFSXMA1","MGFS3_SNH_1","MGFSXNJ1","MGFSXNY1","MGFSXNC1","MGFSXPA1","MGFSXRI1","MGFSXSC1","MGFS3_SVT_1","MGFSXVA1","MGFSXWV1","MGFSXP21","MGFSXIL1","MGFSXIN1","MGFSXIA1","MGFS3_SKS_1","MGFSXKY1","MGFSXMI1","MGFSXMN1","MGFSXMO1","MGFS3_SNE_1","MGFS3_SND_1","MGFSXOH1","MGFSXOK1","MGFS3_SSD_1","MGFSXTN1","MGFSXWI1","MGFSXP31","MGFSXAL1","MGFSXAR1","MGFSXLA1","MGFSXMS1","MGFSXNM1","MGFSXTX1","MGFSXP41","MGFSXCO1","MGFSXID1","MGFSXMT1","MGFSXUT1","MGFSXWY1","MGFSXP51","MGFSXAK1","MGFSXAZ1","MGFSXCA1","MGFSXHI1","MGFSXNV1","MGFSXOR1","MGFSXWA1"

384

Summary of the proceedings of the workshop on the refinery of the future  

SciTech Connect (OSTI)

This report on the Workshop on the Refinery of the Future has been prepared for participants to provide them with a succinct summary of the presentations, deliberations, and discussions. In preparing the summary, we have striven to capture the key findings (conclusions) and highlight the issues and concerns raised during the plenary and breakout sessions. The presentation of the summary of the proceedings follows the final workshop agenda, which is given in Section I; each section is tabbed to facilitate access to specific workshop topics. The material presented relies heavily on the outline summaries prepared and presented by the Plenary Session Chairman and the Facilitators for each breakout group. These summaries are included essentially as presented. In addition, individuals were assigned to take notes during each session; these notes were used to reconstruct critical issues that were discussed in more detail. The key comments made by the participants, which tended to represent the range of views expressed relative to the issues, are presented immediately following the facilitator`s summary outline in order to convey the flavor of the discussions. The comments are not attributed to individuals, since in many instances they represent a composite of several similar views expressed during the discussion. The facilitators were asked to review the writeups describing the outcomes of their sessions for accuracy and content; their suggested changes were incorporated. Every effort has thus been made to reconstruct the views expressed as accurately as possible; however, errors and/or misinterpretations undoubtedly have occurred.

Not Available

1994-06-01T23:59:59.000Z

385

IFDM modelling for optimal siting of air quality monitoring stations around five oil refineries  

Science Journals Connector (OSTI)

An IFDM modelling study has been conducted to determine the optimal siting of air quality monitoring stations around five oil refineries. The purpose of this immission monitoring network is specified in environmental legislation. The most appropriate output parameter of the IFDM model for this study is the 98th percentile of the moving 24 h averages, P98,m24h. Modelling for the optimal siting of air quality monitoring stations turned out to be different from modelling for permit granting. Of interest is not the peak value of a relevant immission parameter, but the places where this parameter is most likely to have a higher peak value compared with neighbouring places. For this study, modelling has been done for eleven years of hourly meteorological data. The eleven yearly immission fields obtained by modelling are synthesized using the minimum, median and maximum values of the P98,m24h values obtained for each receptor point. This synthesis of the modelling results was complemented with an analysis of the available immission data for the region, so that the resulting air quality monitoring network is expected to monitor the impact of all emissions, not only those emissions that are in the emission inventory used for modelling.

G. Cosemans; G. Dumont; E. Roekens; J.G. Kretzschmar

1997-01-01T23:59:59.000Z

386

Cracking of simulated oil refinery off-gas over a coal char, petroleum coke, and quartz  

SciTech Connect (OSTI)

The cracking of oil refinery off-gas, simulated with a gas mixture containing methane (51%), ethylene (21.4%), ethane (21.1%), and propane (6.5%), over a coal char, petroleum coke, and quartz, respectively, has been studied in a fixed bed reactor. The experiments were performed at temperatures between 850 and 1000{sup o}C and at atmospheric pressure. The results show that the conversions of all species considered increased with increasing temperature. Ethane and propane completely decomposed over all three bed materials in the temperature range investigated. However, the higher initial conversion rates of methane and ethylene cracking at all temperatures were observed only over the coal char and not on the petroleum coke and quartz, indicating a significant catalytic effect of the coal char on methane and ethylene cracking. Methane and ethylene conversions decreased with reaction time due to deactivation of the coal char by carbon deposition on the char surface and, in the later stage of a cracking experiment, became negative, suggesting that methane and ethylene had been formed during the cracking of ethane and propane. 16 refs., 13 figs., 2 tabs.

Yuan Zhang; Jin-hu Wu; Dong-ke Zhang [Chinese Academy of Sciences, Taiyuan (China). Institute of Coal Chemistry

2008-03-15T23:59:59.000Z

387

Gasification of refinery sludge in an updraft reactor for syngas production  

Science Journals Connector (OSTI)

The study probes into the investigation on gasification of dry refinery sludge. The details of the study includes; influence of operation time oxidation temperature and equivalence ratios on carbon gas conversion rate gasification efficiency heating value and fuel gas yield are presented. The results show that the oxidation temperature increased sharply up to 858°C as the operating time increased up to 36 min then bridging occurred at 39 min which cause drop in reaction temperature up to 819 °C. This bridging was found to affect also the syngas compositions meanwhile as the temperature decreased the CO H 2 CH 4 compositions are also found to be decreases. Higher temperature catalyzed the reduction reaction ( CO 2 + C ?=?450?2 CO ) and accelerated the carbon conversion and gasification efficiencies resulted in more solid fuel is converted to a high heating value gas fuel. The equivalence ratio of 0.195 was found to be the optimum value for carbon conversion and cold gas efficiencies high heating value of gas and fuel gas yield to reach their maximum values of 96.1 % and 53.7 % 5.42 MJ Nm?3 of and 2.5 Nm3 kg?1 respectively.

2014-01-01T23:59:59.000Z

388

Unusual refinery boiler tube failures due to corrosion by sulfuric acid induced by steam leaks  

SciTech Connect (OSTI)

Corrosion by sulfuric acid in boilers is a low probability event because gas temperature and metal temperature of boiler tubes are high enough to avoid the condensation of sulfuric acid from flue gases. This degradation mechanism is frequently considered as an important cause of air preheaters materials degradation, where flue gases are cooled by heat transfer to the combustion air. Corrosion is associated to the presence of sulfuric acid, which condensates if metal temperature (or gas temperature) is below of the acid dew point. In economizer tubes, sulfuric acid corrosion is an unlikely event because flue gas and tube temperatures are normally over the acid dewpoint. In this paper, the failure analysis of generator tubes (similar to the economizer of bigger boilers) of two small oil-fired subcritical boilers is reported. It is concluded that sulfuric acid corrosion was the cause of the failure. The sulfuric acid condensation was due to the contact of flue gases containing SO{sub 3} with water-steam spray coming from leaks at the interface of rolled tube to the drum. Considering the information gathered from these two cases studied, an analysis of this failure mechanism is presented including a description of the thermodynamics condition of water leaking from the drum, and an analysis of the factors favoring it.

Lopez-Lopez, D.; Wong-Moreno, A. [Instituto de Investigaciones Electricas, Cuernavaca (Mexico)

1998-12-31T23:59:59.000Z

389

Efficieny handling effluent gases through chemical scrubbing  

SciTech Connect (OSTI)

This paper is presented as an information source for efficiencies of chemical scrubbing. In it, we will discuss the specific problems of scrubbing silane, disilane, diborane, phosphine, hydrogen selenide and arsine. We will explain the scrubber dynamics, gases and flow rates used along with liquid mediums. The equipment and procedures used for testing, as well as the determination of the results, will be discussed. We intend to give examples of possible reactions and documentation of our efficiencies. Installation and maintenance will be touched, as well as our experiments into accidental catastrophic releases. From all of this we will derive conclusions as to the best possible means of wet chemical scrubbing.

Herman, T.; Soden, S.

1988-07-15T23:59:59.000Z

390

Heat conduction in relativistic neutral gases revisited  

E-Print Network [OSTI]

The kinetic theory of dilute gases to first order in the gradients yields linear relations between forces and fluxes. The heat flux for the relativistic gas has been shown to be related not only to the temperature gradient but also to the density gradient in the representation where number density, temperature and hydrodynamic velocity are the independent state variables. In this work we show the calculation of the corresponding transport coefficients from the full Boltzmann equation and compare the magnitude of the relativistic correction.

A. L. Garcia-Perciante; A. R. Mendez

2010-09-30T23:59:59.000Z

391

Economic impacts of oil spills: Spill unit costs for tankers, pipelines, refineries, and offshore facilities. [Task 1, Final report  

SciTech Connect (OSTI)

The impacts of oil spills -- ranging from the large, widely publicized Exxon Valdez tanker incident to smaller pipeline and refinery spills -- have been costly to both the oil industry and the public. For example, the estimated costs to Exxon of the Valdez tanker spill are on the order of $4 billion, including $2.8 billion (in 1993 dollars) for direct cleanup costs and $1.125 billion (in 1992 dollars) for settlement of damages claims caused by the spill. Application of contingent valuation costs and civil lawsuits pending in the State of Alaska could raise these costs appreciably. Even the costs of the much smaller 1991 oil spill at Texaco`s refinery near Anacortes, Washington led to costs of $8 to 9 million. As a result, inexpensive waming, response and remediation technologies could lower oil spin costs, helping both the oil industry, the associated marine industries, and the environment. One means for reducing the impact and costs of oil spills is to undertake research and development on key aspects of the oil spill prevention, warming, and response and remediation systems. To target these funds to their best use, it is important to have sound data on the nature and size of spills, their likely occurrence and their unit costs. This information could then allow scarce R&D dollars to be spent on areas and activities having the largest impact. This report is intended to provide the ``unit cost`` portion of this crucial information. The report examines the three key components of the US oil supply system, namely, tankers and barges; pipelines and refineries; and offshore production facilities. The specific purpose of the study was to establish the unit costs of oil spills. By manipulating this key information into a larger matrix that includes the size and frequency of occurrence of oil spills, it will be possible` to estimate the likely future impacts, costs, and sources of oil spills.

Not Available

1993-10-15T23:59:59.000Z

392

Determination of naphthenic acids in California crudes and refinery waste waters by fluoride ion chemical ionization mass spectrometry  

SciTech Connect (OSTI)

A method based on negative ion chemical ionization mass spectrometry using fluoride (F/sup -/) ions produced from NF/sub 3/ reagent gas has been applied to the analysis of naphthenic acids in California crude oils and refinery waste waters. Since complex mixtures of naphthenic acids cannot be separated into individual components, only the determination of relative distribution of acids classified by the hydrogen deficiency was possible. The identities and relative distribution of paraffinic and mono-, di-, tri, and higher polycyclic acids were obtained from the intensities of the carboxylate (RCOO/sup -/) ions.

Dzidic, I.; Somerville, A.C.; Raia, J.C.; Hart, H.V.

1988-07-01T23:59:59.000Z

393

Feasibility study for the retrofitting of used oil re-refineries to the BETC solvent treatment/distillation process  

SciTech Connect (OSTI)

Federal policy encourages recycle of used oil, but requires that recycling be done in an environmentally sound manner. In order to encourage such recycling the Bartlesville Energy Technology Center of the US Department of Energy has developed the DOE/BETA solvent treatment/distillation re-refining process. The feasibility of retrofitting existing used oil re-refineries to the DOE/BETC process has been studied in this work. Twelve potential sites were chosen from almost 300 firms thought to be interested in re-refining technology. Three of these twelve sites have been recommended as prime candidates.

Weinstein, N.J.; Brinkman, D.W.

1980-09-01T23:59:59.000Z

394

Superfund Record of Decision (EPA Region 6): Fourth Street Abandoned Refinery Site, Oklahoma City, OK, September 1993  

SciTech Connect (OSTI)

The decision document presents the selected remedial action for the Fourth Street Refinery Site (FSR site), Oklahoma City, Oklahoma, for the Ground Water Operable Unit. The Record of Decision (ROD) addresses the contamination in the ground water, which includes non-aqueous phase liquids. Principal threat wastes include 'pools' of dense non-aqueous phase liquids (DNAPLs) submerged beneath the ground water or in fractured bedrock, or NAPLs floating on water. This Ground Water Operable Unit addresses the principal threat at the site by monitoring the ground water to ensure that the contaminant levels are reduced with time due to natural attenuation, once the surface contamination is removed.

Not Available

1993-09-01T23:59:59.000Z

395

Superfund record of decision (EPA Region 6): Double Eagle Refinery Site, operable unit 2, Oklahoma City, OK, April 19, 1994  

SciTech Connect (OSTI)

The decision document presents the selected remedial action for the Double Eagle Refinery Site (DER site), in Oklahoma City, Oklahoma, for the Ground Water Operable Unit. Principal threat wastes include `pools` of dense non-aqueous phase liquids (DNAPLs) submerged beneath the ground water or in fractured bedrock. The Ground Water Operable Unit (GOU) addresses the principal threat at the site by monitoring the ground water to ensure that the contaminant levels are reduced with time due to natural attenuation, once the surface contamination is addressed, so that the surface contamination will no longer provide a source of contamination to the ground water.

NONE

1995-02-01T23:59:59.000Z

396

EIA-Voluntary Reporting of Greenhouse Gases Program - Greenhouse Gases and  

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

Greenhouse Gases and Global Warming Potentials (GWP) Greenhouse Gases and Global Warming Potentials (GWP) Voluntary Reporting of Greenhouse Gases Program Greenhouse Gases and Global Warming Potentials (GWP) (From Appendix E of the instructions to Form EIA-1605) GREENHOUSE GAS NAME GREENHOUSE GAS CODE FORMULA GWP TAR1 AR42 (1) Carbon Dioxide CO2 CO2 1 1 (2) Methane CH4 CH4 23 25 (3) Nitrous Oxide N2O N2O 296 298 (4) Hydroflourocarbons HFC-23 (trifluoromethane) 15 CHF3 12000 14800 HFC-32 (difluoromethane) 16 CH2F2 550 675 HFC-41 (monofluoromethane) 43 CH3F 97 -3 HFC-125 (pentafluoroethane) 17 CHF2CF3 3400 3500 HFC-134 (1,1,2,2-tetrafluoroethane) 44 CHF2CHF2 1100 -3 HFC-134a (1,1,1,2-tetrafluoroethane) 18 CH2FCF3 1300 1430 HFC-143 (1,1,2-trifluorethane) 45 CHF2CH2F 330 -3 HFC-143a (1,1,1-trifluoroethane) 46 CF3CH3 4300 4470 HFC-152 (1,2-difluorethane) 47 CH2FCH2F

397

Asia-wide emissions of greenhouse gases  

SciTech Connect (OSTI)

Emissions of principal greenhouse gases (GHGs) from Asia are increasing faster than those from any other continent. This is a result of rapid economic growth, as well as the fact that almost half of the world`s population lives in Asian countries. In this paper, the author provides estimates of emissions of the two principal greenhouse gases, carbon dioxide (CO{sub 2}) and methane (CH{sub 4}), from individual countries and areas. Recent literature has been reviewed for emission estimates for individual sources, such as carbon dioxide from cement manufacture, and methane from rice fields. There are very large uncertainties in many of these estimates, so several estimates are provided, where available. The largest anthropogenic source of CO{sub 2} emissions is the use of fossil fuels. Energy consumption data from 1992 have been used to calculate estimated emissions of CO{sub 2} from this source. In view of the ongoing negotiations to limit future greenhouse gas emissions, estimates of projected CO{sub 2} emissions from the developing countries of Asia are also provided. These are likely to be 3 times their 1986 levels by 2010, under business as usual scenarios. Even with the implementation of energy efficiency measures and fuel switching where feasible, the emissions of CO{sub 2} are likely to double within the same time period.

Siddiqi, T.A. [East-West Center, Honolulu, HI (United States). Program on Environment

1995-11-01T23:59:59.000Z

398

The greenhouse gases HFCs, PFCs Danish consumption and emissions, 2007  

E-Print Network [OSTI]

The greenhouse gases HFCs, PFCs and SF6 Danish consumption and emissions, 2007 Tomas Sander Poulsen AND EMISSION OF F-GASES 7 1.1.1 Consumption 7 1.1.2 Emission 7 1.1.3 Trends in total GWP contribution from F 21 4 EMISSION OF F-GASES 23 4.1.1 Emissions of HFCs from refrigerants 23 4.1.2 Emissions of HFCs from

399

Suspended two-dimensional electron and hole gases  

SciTech Connect (OSTI)

We report on the fabrication of fully suspended two-dimensional electron and hole gases in III-V heterostructures. Low temperature transport measurements verify that the properties of the suspended gases are only slightly degraded with respect to the non-suspended gases. Focused ion beam technology is used to pattern suspended nanostructures with minimum damage from the ion beam, due to the small width of the suspended membrane.

Kazazis, D.; Bourhis, E.; Gierak, J.; Gennser, U. [Laboratoire de Photonique et de Nanostructures, CNRS-LPN, Route de Nozay, 91460 Marcoussis (France); Bourgeois, O. [Institut Néel, CNRS-UJF, BP 166, 38042 Grenoble Cedex 9 (France); Antoni, T. [Laboratoire de Photonique et de Nanostructures, CNRS-LPN, Route de Nozay, 91460 Marcoussis, France and Laboratoire Kastler Brossel, Université Pierre et Marie Curie, 4 Place Jussieu, 75005 Paris (France)

2013-12-04T23:59:59.000Z

400

Petroleum Supply Monthly  

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

6 6 September 2013 Table 10. PAD District 2 - Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 366,285 - - - - 501,418 159,175 -109,633 -12,929 918,349 11,825 0 102,610 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 122,918 -4,579 37,556 21,926 4,444 - - 15,132 24,244 34,819 108,070 58,830 Pentanes Plus ..................................................

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Petroleum Supply Monthly  

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

20 20 September 2013 Table 14. PAD District 3 - Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 1,188,751 - - - - 1,015,091 -112,708 94,064 20,399 2,158,191 6,608 0 882,207 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 440,766 -88 123,986 10,625 46,383 - - 16,960 76,972 72,880 454,860 114,138 Pentanes Plus ..................................................

402

Petroleum Supply Monthly  

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

September 2013 Table 2. U.S. Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports Adjust- ments 1 Stock Change 2 Refinery and Blender Net Inputs Exports Products Supplied 3 Crude Oil 4 ............................................................ 2,003,948 - - - - 2,123,490 65,265 6,899 4,157,486 28,318 0 1,067,149 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 686,936 -4,909 195,516 47,812 - - 36,219 127,051 118,364 643,721 189,672 Pentanes Plus .................................................. 92,842 -4,909 - - 10,243 - -

403

Petroleum Supply Annual  

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

TABLE7.PDF TABLE7.PDF Table 7. PAD District 3 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 109,919 - - - - 142,073 -20,272 -3,481 6,003 222,236 - 0 858,776 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 43,678 -17 9,648 1,838 7,546 - - -2,299 8,340 4,663 51,989 65,215 Pentanes Plus .................................................. 4,840 -17 - - 1,688 -3,010 - -

404

Petroleum Supply Monthly  

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

8 8 September 2013 Table 22. PAD District 5 - Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 300,668 - - - - 297,837 - 31,342 -3,713 633,292 267 0 52,719 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 17,739 -73 18,288 1,401 - - - 3,536 17,170 3,791 12,858 8,270 Pentanes Plus .................................................. 7,914

405

Petroleum Supply Monthly  

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

September 2013 Table 6. PAD District 1 - Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 8,672 - - - - 230,125 -359 62,824 2,069 289,586 9,606 0 10,326 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 19,329 -83 12,151 10,808 21,118 - - 168 4,287 2,821 56,047 6,541 Pentanes Plus ..................................................

406

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

December 2011 December 2011 Table 9. PAD District 2 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, December 2011 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 29,019 - - - - 52,699 26,041 2,973 12 109,175 1,544 0 93,189 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 14,079 -560 812 2,541 -423 - - -6,605 4,051 2,114 16,889 48,197 Pentanes Plus .................................................. 1,354 -560 - - 21 2,843 - - 110 1,049

407

Petroleum Supply Annual  

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

TABLE5.PDF TABLE5.PDF Table 5. PAD District 2 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 29,902 - - - - 53,695 23,732 5,619 2,406 108,247 2,295 0 95,547 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 13,989 -544 1,333 2,797 949 - - -6,644 3,628 2,687 18,853 41,545 Pentanes Plus .................................................. 1,274 -544 - - 11 4,162 - - 233 966

408

Petroleum Supply Monthly  

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

4 4 September 2013 Table 18. PAD District 4 - Year-to-Date Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, January-September 2013 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil ............................................................. 139,573 - - - - 79,019 -46,108 -13,333 1,073 158,068 10 0 19,287 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 86,184 -86 3,535 3,052 -71,945 - - 423 4,378 4,054 11,885 1,893 Pentanes Plus ..................................................

409

untitled  

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

PAD District 3 - Supply, Disposition, and Ending Stocks of Crude Oil and Petroleum Products, 2012 (Thousand Barrels) Commodity Supply Disposition Ending Stocks Field Production Renewable Fuels and Oxygenate Plant Net Production Refinery and Blender Net Production Imports (PADD of Entry) 1 Net Receipts 2 Adjust- ments 3 Stock Change 4 Refinery and Blender Net Inputs Exports Products Supplied 5 Crude Oil 6 ............................................................ 1,386,172 - - - - 1,630,908 -244,084 67,631 8,560 2,830,779 1,288 0 861,333 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 540,336 -180 150,143 11,694 101,692 - - 29,480 109,476 61,693 603,036 96,994 Pentanes Plus .................................................. 66,222 -180 - - 10,282 -16,515 - -

410

EIA-Voluntary Reporting of Greenhouse Gases Program - Emission...  

Gasoline and Diesel Fuel Update (EIA)

AP-42 Volume 2 mobile sources Global Warming Potentials The Intergovernmental Panel on Climate Change (IPCC) revised GWPs for certain greenhouse gases in 2007 for the Fourth...

411

Energetic Materials for EGS Well Stimulation (solids, liquids, gases)  

Broader source: Energy.gov [DOE]

Energetic Materials for EGS Well Stimulation (solids, liquids, gases) presentation at the April 2013 peer review meeting held in Denver, Colorado.

412

Liquefaction process wherein solvents derived from the material liquefied and containing increased concentrations of donor species are employed  

DOE Patents [OSTI]

An improved process for the liquefaction of solid carbonaceous materials wherein a solvent or diluent derived from the solid carbonaceous material being liquefied is used to form a slurry of the solid carbonaceous material and wherein the solvent or diluent comprises from about 65 to about 85 wt. % hydroaromatic components. The solvent is prepared by first separating a solvent or diluent distillate fraction from the liquefaction product, subjecting this distillate fraction to hydrogenation and then extracting the naphthenic components from the hydrogenated product. The extracted naphthenic components are then dehydrogenated and hydrotreated to produce additional hydroaromatic components. These components are combined with the solvent or diluent distillate fraction. The solvent may also contain hydroaromatic constituents prepared by extracting naphthenic components from a heavy naphtha, dehydrogenating the same and then hydrotreating the dehydrogenated product. When the amount of solvent produced in this manner exceeds that required for steady state operation of the liquefaction process a portion of the solvent or diluent distillated fraction will be withdrawn as product.

Fant, B. T. (Kingwood, TX); Miller, John D. (Baytown, TX); Ryan, D. F. (Friendswood, TX)

1982-01-01T23:59:59.000Z

413

Liquefaction process wherein solvents derived from the material liquefied and containing increased concentrations of donor species are employed  

SciTech Connect (OSTI)

An improved process is disclosed for the liquefaction of solid carbonaceous materials. A solvent or diluent derived from the solid carbonaceous material being liquefied is used to form a slurry of the solid carbonaceous material. The solvent or diluent comprises from about 65 to about 85 wt. % hydroaromatic components. The solvent is prepared by first separating a solvent or diluent distillate fraction from the liquefaction product, subjecting this distillate fraction to hydrogenation and then extracting the naphthenic components from the hydrogenated product. The extracted naphthenic components are then dehydrogenated and hydrotreated to produce additional hydroaromatic components. These components are combined with the solvent or diluent distillate fraction. The solvent may also contain hydroaromatic constituents prepared by extracting naphthenic components from a heavy naphtha, dehydrogenating the same and then hydrotreating the dehydrogenated product. When the amount of solvent produced in this manner exceeds that required for steady state operation of the liquefaction process a portion of the solvent or diluent distillated fraction will be withdrawn as product.

Fant, B.; Miller, J.D.; Ryan, D.F.

1982-01-19T23:59:59.000Z

414

Thermodynamic analysis of an SOFC–GT–ORC integrated power system with liquefied natural gas as heat sink  

Science Journals Connector (OSTI)

To recover the waste heat from solid oxide fuel cell (SOFC) and improve the overall electrical efficiency, a new integrated power system driven by SOFC is proposed to achieve the cascade energy utilization. This system integrates an SOFC–GT system with an organic Rankine cycle (ORC) using liquefied natural gas (LNG) as heat sink to recover the cryogenic energy of LNG. Based on the mathematical model, a parametric analysis is conducted to examine the effects of some key thermodynamic parameters on the system performance. The results indicate that the overall electrical efficiency of 67% can be easily achieved for the current system, which can be further improved with parametric optimization. An increase in fuel flow rate of SOFC can raise the net power output, but it has a negative effect on SOFC and overall electrical efficiency. The compressor pressure ratio contributes to an increase in SOFC and overall electrical efficiency, which are contrary to the effects of air flow rate and steam-to-carbon ratio. Under the given conditions, compared with the Kalina sub-system, the ORC sub-system produces 12.6% more power output by utilizing the cryogenic energy of LNG with simple configuration.

Zhequan Yan; Pan Zhao; Jiangfeng Wang; Yiping Dai

2013-01-01T23:59:59.000Z

415

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

Science Journals Connector (OSTI)

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

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

2008-01-01T23:59:59.000Z

416

FLAMMABILITY CHARACTERISTICS OF COMBUSTIBLE GASES AND VAPORS  

Office of Scientific and Technical Information (OSTI)

Bulletin 627 Bulletin 627 BUREAU o b MINES FLAMMABILITY CHARACTERISTICS OF COMBUSTIBLE GASES AND VAPORS By Michael G. Zabetakis 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 herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement,

417

Shortcuts to adiabaticity for trapped ultracold gases  

E-Print Network [OSTI]

We study, experimentally and theoretically, the controlled transfer of harmonically trapped ultracold gases between different quantum states. In particular we experimentally demonstrate a fast decompression and displacement of both a non-interacting gas and an interacting Bose-Einstein condensate which are initially at equilibrium. The decompression parameters are engineered such that the final state is identical to that obtained after a perfectly adiabatic transformation despite the fact that the fast decompression is performed in the strongly non-adiabatic regime. During the transfer the atomic sample goes through strongly out-of-equilibrium states while the external confinement is modified until the system reaches the desired stationary state. The scheme is theoretically based on the invariants of motion and scaling equations techniques and can be generalized to decompression trajectories including an arbitrary deformation of the trap. It is also directly applicable to arbitrary initial non-equilibrium sta...

Schaff, Jean-François; Labeyrie, Guillaume; Vignolo, Patrizia

2011-01-01T23:59:59.000Z

418

Shortcuts to adiabaticity for trapped ultracold gases  

E-Print Network [OSTI]

We study, experimentally and theoretically, the controlled transfer of harmonically trapped ultracold gases between different quantum states. In particular we experimentally demonstrate a fast decompression and displacement of both a non-interacting gas and an interacting Bose-Einstein condensate which are initially at equilibrium. The decompression parameters are engineered such that the final state is identical to that obtained after a perfectly adiabatic transformation despite the fact that the fast decompression is performed in the strongly non-adiabatic regime. During the transfer the atomic sample goes through strongly out-of-equilibrium states while the external confinement is modified until the system reaches the desired stationary state. The scheme is theoretically based on the invariants of motion and scaling equations techniques and can be generalized to decompression trajectories including an arbitrary deformation of the trap. It is also directly applicable to arbitrary initial non-equilibrium states.

Jean-François Schaff; Pablo Capuzzi; Guillaume Labeyrie; Patrizia Vignolo

2011-05-11T23:59:59.000Z

419

Voluntary reporting of greenhouse gases 1997  

SciTech Connect (OSTI)

The Voluntary Reporting of Greenhouse Gases Program, required by Section 1605(b) of the Energy Policy Act of 1992, records the results of voluntary measures to reduce, avoid, or sequester greenhouse gas emissions. In 1998, 156 US companies and other organizations reported to the Energy information Administration that, during 1997, they had achieved greenhouse gas emission reductions and carbon sequestration equivalent to 166 million tons of carbon dioxide, or about 2.5% of total US emissions for the year. For the 1,229 emission reduction projects reported, reductions usually were measured by comparing an estimate of actual emissions with an estimate of what emissions would have been had the project not been implemented.

NONE

1999-05-01T23:59:59.000Z

420

Bogoliubov spectrum of interacting Bose gases  

E-Print Network [OSTI]

We study the large-N limit of a system of N bosons interacting with a potential of intensity 1/N. When the ground state energy is to the first order given by Hartree's theory, we study the next order, predicted by Bogoliubov's theory. We show the convergence of the lower eigenvalues and eigenfunctions towards that of the Bogoliubov Hamiltonian (up to a convenient unitary transform). We also prove the convergence of the free energy when the system is sufficiently trapped. Our results are valid in an abstract setting, our main assumptions being that the Hartree ground state is unique and non-degenerate, and that there is complete Bose-Einstein condensation on this state. Using our method we then treat two applications: atoms with ''bosonic'' electrons on one hand, and trapped 2D and 3D Coulomb gases on the other hand.

Mathieu Lewin; Phan Thành Nam; Sylvia Serfaty; Jan Philip Solovej

2014-03-11T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Method of converting environmentally pollutant waste gases to methanol  

SciTech Connect (OSTI)

A continuous flow method is described of converting environmentally pollutant by-product gases emitted during the manufacture of silicon carbide to methanol comprising: (a) operating a plurality of batch furnaces of a silicon carbide manufacturing plant thereby producing silicon carbide and emitting by-product gases during the operation of the furnaces; (b) staggering the operation of the batch furnaces to achieve a continuous emission of the by-product gases; (c) continuously flowing the by-product gases as emitted from the batch furnaces directly to a methanol manufacturing plant; (d) cleansing the by-product gases of particulate matter, including removing the element sulfur from the by-product gases, as they are flowed to the methanol manufacturing plant, sufficiently for use of the by-product gases in producing methanol; and (e) immediately producing methanol from the by-product gases at the methanol manufacturing plant whereby the producing of silicon carbide is joined with the producing of methanol as a unified process.

Pfingstl, H.; Martyniuk, W.; Hennepin, A. Ill; McNally, T.; Myers, R.; Eberle, L.

1993-08-03T23:59:59.000Z

422

OBTAINING LAWS OF THERMODYNAMICS FOR IDEAL GASES USING ELASTIC COLLISIONS  

E-Print Network [OSTI]

OBTAINING LAWS OF THERMODYNAMICS FOR IDEAL GASES USING ELASTIC COLLISIONS STEPHEN MONTGOMERY law of expansion of ideal gases. 1. The Second Law of Thermodynamics A thermally isolated container-SMITH AND HANNAH MORGAN Abstract. The purpose of this note is to see to what extent ideal gas laws can be obtained

Montgomery-Smith, Stephen

423

Continuous cryopump with a method for removal of solidified gases  

DOE Patents [OSTI]

An improved cryopump for the removal of gases from a high vacuum, comprising a cryopanel incorporating honeycomb structure, refrigerant means thermally connected to the cryopanel, and a rotatable channel moving azimuthally around an axis located near the center of the cryopanel, removing gases adsorbed within the honeycomb structure by subliming them and conducting them outside the vacuum vessel. 4 figs.

Carlson, L.W.; Herman, H.

1988-05-05T23:59:59.000Z

424

Supply and Disposition of Crude Oil and Petroleum Products  

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

,980 842 4,204 1,948 672 -339 187 3,995 240 4,886 ,980 842 4,204 1,948 672 -339 187 3,995 240 4,886 Crude Oil 1,472 - - - - 1,839 556 -359 17 3,416 76 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 508 -17 115 63 -14 - - 75 105 71 404 Pentanes Plus 63 -17 - - 0 98 - - -18 37 53 72 Liquefied Petroleum Gases 444 - - 115 63 -112 - - 93 68 18 332 Ethane/Ethylene 163 - - - 0 -100 - - 11 - - 52 Propane/Propylene 186 - - 104 49 -22 - - 66 - 7 244 Normal Butane/Butylene 52 - - 16 5 5 - - 22 17 11 29 Isobutane/Isobutylene 43 - - -4 8 5 - - -6 50 - 7 Other Liquids - - 858 - - 12 -143 127 346 474 40 -6 Hydrogen/Oxygenates/Renewables/Other Hydrocarbons - - 858 - - 5 -547 -8 11 271 26 0 Hydrogen - - - - - - 23 - - 23 0 - -

425

Petroleum Supply Monthly  

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

0 0 September 2013 Table 49. Exports of Crude Oil and Petroleum Products by PAD District, September 2013 (Thousand Barrels) Commodity PAD Districts U.S. Total 1 2 3 4 5 Total Daily Average Crude Oil 1 ............................................................ 94 2,282 598 1 - 2,975 99 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 453 2,129 10,579 380 396 13,937 465 Pentanes Plus .................................................. 300 1,599 652 346 92 2,989 100 Liquefied Petroleum Gases .............................. 153 530 9,927 34 304 10,947 365 Ethane/Ethylene ........................................... - - - - - - - Propane/Propylene ....................................... 126 199 9,412 4 299 10,040 335 Normal Butane/Butylene ...............................

426

Supply and Disposition of Crude Oil and Petroleum Products  

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

562 822 4,163 1,839 735 -69 52 3,955 244 4,801 562 822 4,163 1,839 735 -69 52 3,955 244 4,801 Crude Oil 1,116 - - - - 1,730 800 -87 62 3,442 55 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 446 -16 121 74 -25 - - -12 105 111 395 Pentanes Plus 50 -16 - - 1 82 - - -4 31 101 -12 Liquefied Petroleum Gases 396 - - 121 73 -107 - - -8 74 11 407 Ethane/Ethylene 163 - - - 0 -108 - - -2 - - 58 Propane/Propylene 156 - - 108 59 -24 - - -3 - 2 300 Normal Butane/Butylene 48 - - 11 9 10 - - -4 29 9 45 Isobutane/Isobutylene 29 - - 2 6 14 - - 1 46 - 5 Other Liquids - - 838 - - 5 -258 -159 8 408 25 -16 Hydrogen/Oxygenates/Renewables/Other Hydrocarbons - - 838 - - 3 -565 4 1 257 21 0 Hydrogen - - - - - - 22 - - 22 0 - -

427

Supply and Disposition of Crude Oil and Petroleum Products  

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

124 22 3,585 1,761 3,291 117 -137 3,532 241 5,264 124 22 3,585 1,761 3,291 117 -137 3,532 241 5,264 Crude Oil 34 - - - - 897 1 113 -43 1,084 3 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 90 0 25 32 86 - - 16 27 15 174 Pentanes Plus 15 0 - - - - - - 0 - 10 4 Liquefied Petroleum Gases 75 - - 25 32 86 - - 16 27 5 169 Ethane/Ethylene 1 - - 0 - - - - 0 - - 1 Propane/Propylene 51 - - 36 27 83 - - 24 - 4 168 Normal Butane/Butylene 16 - - -11 3 3 - - -8 17 1 0 Isobutane/Isobutylene 8 - - 0 2 - - - -1 9 - 0 Other Liquids - - 22 - - 555 1,614 193 -31 2,421 5 -10 Hydrogen/Oxygenates/Renewables/Other Hydrocarbons - - 22 - - 25 273 -19 -35 332 5 0 Hydrogen - - - - - - 4 - - 4 0 - - Oxygenates (excl. Fuel Ethanol)

428

Supply and Disposition of Crude Oil and Petroleum Products  

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

1,164 20 3,171 1,425 308 193 28 2,990 349 2,914 1,164 20 3,171 1,425 308 193 28 2,990 349 2,914 Crude Oil 1,104 - - - - 1,209 - 140 10 2,443 - 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 61 0 66 4 - - - 36 59 13 22 Pentanes Plus 26 0 - - - - - - 5 18 3 -1 Liquefied Petroleum Gases 34 - - 66 4 - - - 30 41 10 23 Ethane/Ethylene 0 - - - - - - - - - - 0 Propane/Propylene 14 - - 49 4 - - - 12 - 10 45 Normal Butane/Butylene 5 - - 15 0 - - - 13 19 0 -11 Isobutane/Isobutylene 15 - - 1 - - - - 5 22 - -12 Other Liquids - - 20 - - 107 252 94 -71 488 13 43 Hydrogen/Oxygenates/Renewables/Other Hydrocarbons - - 20 - - 19 143 37 -2 219 3 0 Hydrogen - - - - - - 47 - - 47 0 - - Oxygenates (excl. Fuel Ethanol)

429

Supply and Disposition of Crude Oil and Petroleum Products  

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

1,173 16 2,988 1,321 324 106 21 2,811 344 2,751 1,173 16 2,988 1,321 324 106 21 2,811 344 2,751 Crude Oil 1,111 - - - - 1,160 2 62 4 2,331 0 0 Natural Gas Plant Liquids and Liquefied Refinery Gases 61 0 50 5 - - - 1 66 15 35 Pentanes Plus 28 0 - - - - - - 0 21 3 4 Liquefied Petroleum Gases 33 - - 50 5 - - - 1 45 12 31 Ethane/Ethylene 0 - - - - - - - - - - 0 Propane/Propylene 12 - - 46 4 - - - 1 - 10 51 Normal Butane/Butylene 6 - - 6 1 - - - 0 26 1 -14 Isobutane/Isobutylene 15 - - -2 0 - - - 0 20 - -7 Other Liquids - - 16 - - 74 245 103 11 414 13 1 Hydrogen/Oxygenates/Renewables/Other Hydrocarbons - - 16 - - 7 138 37 2 193 3 0 Hydrogen - - - - - - 43 - - 43 0 - - Oxygenates (excl. Fuel Ethanol) - - - - 1 1 0

430

Petroleum Supply Annual  

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

5.PDF 5.PDF Table 25. Imports of Crude Oil and Petroleum Products by PAD District, January 2012 (Thousand Barrels, Except Where Noted) Commodity PAD Districts U.S. Total 1 2 3 4 5 Total Daily Average Crude Oil 1,2 ................................................................................. 26,390 54,466 143,796 8,286 31,410 264,348 8,527 Natural Gas Plant Liquids and Liquefied Refinery Gases ...... 1,606 2,797 1,838 502 192 6,935 224 Pentanes Plus .......................................................................... - 11 1,688 - - 1,699 55 Liquefied Petroleum Gases ...................................................... 1,606 2,786 150 502 192 5,236 169 Ethane .................................................................................. - - - - - - - Ethylene ................................................................................

431

Petroleum Supply Monthly  

Gasoline and Diesel Fuel Update (EIA)

4 4 December 2011 Table 50. Year-to-Date Exports of Crude Oil and Petroleum Products by PAD District, January-December 2011 (Thousand Barrels) Commodity PAD Districts U.S. Total 1 2 3 4 5 Total Daily Average Crude Oil 1 ............................................................ 2,147 13,574 1,237 191 9 17,158 47 Natural Gas Plant Liquids and Liquefied Refinery Gases ................................................... 3,739 15,542 42,403 2,288 6,081 70,053 192 Pentanes Plus .................................................. 2,075 11,913 179 1,415 340 15,922 44 Liquefied Petroleum Gases .............................. 1,664 3,628 42,224 873 5,741 54,131 148 Ethane/Ethylene ........................................... - - - - - - - Propane/Propylene ....................................... 401 514 40,084 58 4,187 45,243

432

EIA - Greenhouse Gas Emissions - High-GWP gases  

Gasoline and Diesel Fuel Update (EIA)

5. High-GWP gases 5. High-GWP gases 5.1. Total emissions Greenhouse gases with high global warming potential (high-GWP gases) are hydrofluorocarbons (HFCs), perfluorocarbons (PFCs), and sulfur hexafluoride (SF6), which together represented 3 percent of U.S. greenhouse gas emissions in 2009. Emissions estimates for the high-GWP gases are provided to EIA by the EPA's Office of Air and Radiation. The estimates for emissions of HFCs not related to industrial processes or electric transmission are derived from the EPA Vintaging Model. Emissions from manufacturing and utilities are derived by the EPA from a mix of public and proprietary data, including from the EPA's voluntary emission reduction partnership programs. For this year's EIA inventory, 2008 values for HFC-23 from HCFC-22

433

The Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation  

Open Energy Info (EERE)

Gases, Regulated Emissions, and Energy Use in Transportation Gases, Regulated Emissions, and Energy Use in Transportation Model (GREET) Jump to: navigation, search Tool Summary Name: The Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation Model (GREET Fleet) Agency/Company /Organization: Argonne National Laboratory Sector: Energy Focus Area: Greenhouse Gas, Transportation Phase: Determine Baseline, Evaluate Options Topics: Baseline projection, GHG inventory Resource Type: Software/modeling tools User Interface: Spreadsheet Website: greet.es.anl.gov/main Cost: Free OpenEI Keyword(s): EERE tool, The Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation Model, GREET References: GREET Fleet Main Page[1] Logo: The Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation Model (GREET Fleet)

434

EIA-Voluntary Reporting of Greenhouse Gases Program  

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

of Greenhouse Gases Program of Greenhouse Gases Program Voluntary Reporting of Greenhouse Gases Program ***THE VOLUNTARY REPORTING OF GREENHOUSE GASES ("1605(b)") PROGRAM HAS BEEN SUSPENDED.*** This affects all survey respondents. Please visit the What's New page for full details. What Is the Voluntary Reporting Program? logo Established by Section 1605(b) of the Energy Policy Act of 1992, the Voluntary Reporting of Greenhouse Gases Program encourages corporations, government agencies, non-profit organizations, households, and other private and public entities to submit annual reports of their greenhouse gas emissions, emission reductions, and sequestration activities. The Program provides a means for voluntary reporting that is complete, reliable, and consistent. More information on the program...

435

A blending problem (Taha, Example 2.3-7, almost) An oil refinery has three stages of production: a distillation tower, which  

E-Print Network [OSTI]

of feedstock; and a blender unit which blends feedstock and gasoline stock (at no loss). (Note that "ONA blending problem (Taha, Example 2.3-7, almost) An oil refinery has three stages of production in feedstock (maximum 200,000 bbl/day) and produces gasoline stock with 98 ON at a rate of .5 bbl per bbl

Galvin, David

436

Measuring non-condensable gases in steam  

SciTech Connect (OSTI)

In surgery, medical devices that are used should be sterilized. To obtain surface steam sterilization conditions, not only in the sterilizer chamber itself but also in the loads to be sterilized, the amount of non-condensable gases (NCGs), for instance air, should be very low. Even rather small fractions of NCGs (below 1 %) seriously hamper steam penetration in porous materials or devices with hollow channels (e.g., endoscopes). A recently developed instrument which might detect the presence of residual NCGs in a reliable and reproducible way is the 3M{sup TM} Electronic Test System (ETS). In this paper, a physical model is presented that describes the behavior of this instrument. This model has been validated by experiments in which known fractions of NCGs were introduced in a sterilizer chamber in which an ETS was placed. Despite several approximations made in the model, a good agreement is found between the model predictions and the experimental results. The basic principle of the ETS, measuring the heat transfer by condensation on a cooled surface, permits a very sensitive detection of NCGs in harsh environments like water vapor at high temperatures and pressures. Our model may serve to develop adapted and optimized versions of this instrument for use outside the field of sterilization, e.g., in heat exchangers based on steam condensation.

Doornmalen, J. P. C. M. van; Kopinga, K., E-mail: k.kopinga@tue.nl [Department of Applied Physics, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven (Netherlands)

2013-11-15T23:59:59.000Z

437

1 - Solubility of Atmospheric Gases in Freshwater  

Science Journals Connector (OSTI)

This chapter presents tabular information on the standard air saturation concentration (moist air at 1 atm) for oxygen, nitrogen, argon, and carbon dioxide gas in terms of ?mol/kg, mg/L, and mL/L; and in terms of Bunsen coefficients L real gas/(L atm); mg real gas/(L mmHg); and mg real gas/(L kPa) for 0–40°C and freshwater conditions. Because the mole fraction of carbon dioxide in the atmosphere is changing, solubility information is provided for 2010 (390 ?atm) and for 2030 (440 ?atm) based on projected atmospheric values. Tabular information is also provided to allow computation of standard air saturation concentrations of carbon dioxide gas directly as a function of atmospheric mole fraction. Conversion factors are presented to convert these concentrations to other commonly used units. Equations and tabular information are provided to compute air saturation concentration for moist air at local barometric pressure for the four atmospheric gases. Because of the importance of dissolved oxygen in biological processes, the air solubility concentration is also presented as a function of elevation for both metric and English elevations. Equations and tabular information are provided to allow conversion of concentrations in mg/L to partial pressures in mmHg. Sample problems are included for representative examples. Keywords gas solubility, freshwater, oxygen, nitrogen, argon, carbon dioxide, standard air solubility, air solubility, Bunsen coefficients, partial pressures

John Colt

2012-01-01T23:59:59.000Z

438

Feasibility Study of Economics and Performance of Solar Photovoltaics at the Former St. Marks Refinery in St. Marks, Florida  

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

853 853 September 2010 Feasibility Study of Economics and Performance of Solar Photovoltaics at the Former St. Marks Refinery in St. Marks, Florida A Study Prepared in Partnership with the Environmental Protection Agency for the RE-Powering America's Lands Initiative: Siting Renewable Energy on Potentially Contaminated Land and Mine Sites Lars Lisell and Gail Mosey National Renewable Energy Laboratory 1617 Cole Boulevard, Golden, Colorado 80401-3393 303-275-3000 * www.nrel.gov NREL is a national laboratory of the U.S. Department of Energy Office of Energy Efficiency and Renewable Energy Operated by the Alliance for Sustainable Energy, LLC Contract No. DE-AC36-08-GO28308 Technical Report NREL/TP-6A2-48853 September 2010 Feasibility Study of Economics

439

Energy Efficiency and Greenhouse Gases | Department of Energy  

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

Energy Efficiency Energy Efficiency and Greenhouse Gases Energy Efficiency and Greenhouse Gases Mission The team establishes an energy conservation program as defined in Executive Order (EO) 13423, Strengthening Federal Environmental, Energy, and Transportation Management, and (EO) 13514, Federal Leadership in Environmental, Energy, and Economic Performance, and DOE Order 436.1, Departmental Sustainability, and approved by LM. The team incorporates requirements for energy efficiency and reductions in greenhouse gases, and it advocates conserving environmental resources and improving operational capabilities and mission sustainability. Scope The team evaluates how to maintain and operate its buildings and facilities in a resource-efficient, sustainable, and economically viable manner. The

440

Unified Theory of Lattice Boltzmann Models for Nonideal Gases  

SciTech Connect (OSTI)

A nonideal gas lattice Boltzmann model is directly derived, in an {ital a priori} fashion, from the Enskog equation for dense gases. The model is rigorously obtained by a systematic procedure to discretize the Enskog equation (in the presence of an external force) in both phase space and time. The lattice Boltzmann model derived here is thermodynamically consistent and is free of the defects which exist in previous lattice Boltzmann models for nonideal gases. The existing lattice Boltzmann models for nonideal gases are analyzed and compared with the model derived here. {copyright} {ital 1998} {ital The American Physical Society}

Luo, L. [ICASE, MS 403, NASA Langley Research Center, 6 North Dryden Street, Building 1298, Hampton, Virginia 23681-0001 (United States)] [ICASE, MS 403, NASA Langley Research Center, 6 North Dryden Street, Building 1298, Hampton, Virginia 23681-0001 (United States)

1998-08-01T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

Global warming description using Daisyworld model with greenhouse gases  

Science Journals Connector (OSTI)

Abstract Daisyworld is an archetypal model of the earth that is able to describe the global regulation that can emerge from the interaction between life and environment. This article proposes a model based on the original Daisyworld considering greenhouse gases emission and absorption, allowing the description of the global warming phenomenon. Global and local analyses are discussed evaluating the influence of greenhouse gases in the planet dynamics. Numerical simulations are carried out showing the general qualitative behavior of the Daisyworld for different scenarios that includes solar luminosity variations and greenhouse gases effect. Nonlinear dynamics perspective is of concern discussing a way that helps the comprehension of the global warming phenomenon.

Susana L.D. Paiva; Marcelo A. Savi; Flavio M. Viola; Albino J.K. Leiroz

2014-01-01T23:59:59.000Z

442

,"Price of U.S. Liquefied Natural Gas Imports From Other Countries (Dollars per Thousand Cubic Feet)"  

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

Other Countries (Dollars per Thousand Cubic Feet)" Other Countries (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Other Countries (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103983m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103983m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov"

443

,"Price of U.S. Liquefied Natural Gas Imports From Equatorial Guinea (Dollars per Thousand Cubic Feet)"  

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

Equatorial Guinea (Dollars per Thousand Cubic Feet)" Equatorial Guinea (Dollars per Thousand Cubic Feet)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Price of U.S. Liquefied Natural Gas Imports From Equatorial Guinea (Dollars per Thousand Cubic Feet)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_nus-nek_pml_dmcfm.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_nus-nek_pml_dmcfm.htm" ,"Source:","Energy Information Administration"

444

Sorption of organic gases in residential rooms  

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

residential rooms residential rooms Title Sorption of organic gases in residential rooms Publication Type Journal Article LBNL Report Number LBNL-59303 Year of Publication 2007 Authors Singer, Brett C., Alfred T. Hodgson, Toshifumi Hotchi, Katherine Y. Ming, Richard G. Sextro, Emily E. Wood, and Nancy J. Brown Journal Atmospheric Environment Volume 41 Start Page Chapter Pagination 3251-3265 Keywords adsorption, hazardous air pollutants, nerve agents, sink effect, volatile organic compounds Abstract Experiments were conducted to characterize organic gas sorption in residential rooms studied ''as-is'' with furnishings and material surfaces unaltered and in a furnished chamber designed to simulate a residential room. Results are presented for 10 rooms (five bedrooms, two bathrooms, a home office, and two multi-function spaces) and the chamber. Exposed materials were characterized and areas quantified. A mixture of volatile organic compounds (VOCs) was rapidly volatilized within each room as it was closed and sealed for a 5-h Adsorb phase; this was followed by 30-min Flush and 2-h closed-room Desorb phases. Included were alkane, aromatic, and oxygenated VOCs representing a range of ambient and indoor air pollutants. Three organophosphorus compounds served as surrogates for Sarin-like nerve agents. Measured gas-phase concentrations were fit to three variations of a mathematical model that considers sorption occurring at a surface sink and potentially a second, embedded sink. The 3-parameter sink-diffusion model provided acceptable fits for most compounds and the 4-parameter two-sink model provided acceptable fits for the others. Initial adsorption rates and sorptive partitioning increased with decreasing vapor pressure for the alkanes, aromatics and oxygenated VOCs. Best-fit sorption parameters obtained from experimental data from the chamber produced best-fit sorption parameters similar to those obtained from the residential rooms

445

Analysis of air pollution and greenhouse gases  

SciTech Connect (OSTI)

The current objective of the project Analysis of Air Pollution and Greenhouse Gases'' is to develop a study of emissions and emission sources that could easily be linked to models of economic activity. Initial studies were conducted to evaluate data currently available linking activity rates and emissions estimates. The emissions inventory developed for the National Acid Precipitation Assessment Program (NAPAP) presents one of the most comprehensive data sets, and was chosen for our initial studies, which are described in this report. Over 99% of the SO{sub 2} emissions, 98% of the NO{sub x} emission and 57% of the VOC emissions from area sources are related to fuel combustion. The majority of emission from these sources are generated by the transportation sector. Activity rates for area sources are not archived with the NAPAP inventory; alternative derivations of these data will be part of the future activities of this project. The availability and completeness of the fuel heat content data in the NAPAP inventory were also studied. Approximately 10% of the SO{sub 2} emissions, 13% of the NO{sub x} emissions and 46% of the VOC emissions are generated by sources with unavailable data for fuel heat content. Initial estimates of pollutant emission rate per unit fuel heat content. Initial estimates of pollutant emission rate per unit fuel heat content were generated. Future studies for this project include the derivation of activity rates for area sources, improved explanations for the default fuel parameters defined in the NAPAP inventory and the development of links to data bases of economic activity.

Benkovitz, C.M.

1992-03-01T23:59:59.000Z

446

Global Research Alliance on Agricultural Greenhouse Gases | Open Energy  

Open Energy Info (EERE)

Global Research Alliance on Agricultural Greenhouse Gases Global Research Alliance on Agricultural Greenhouse Gases Jump to: navigation, search Name Global Research Alliance on Agricultural Greenhouse Gases Agency/Company /Organization United States Department of Agriculture Sector Land Focus Area Agriculture Topics GHG inventory, Policies/deployment programs Resource Type Guide/manual, Lessons learned/best practices Website http://globalresearchalliance. References Global Research Alliance on Agricultural Greenhouse Gases [1] Background "The Alliance is a bottom-up network, founded on the voluntary, collaborative efforts of countries. It will coordinate research on agricultural greenhouse gas emission reductions by linking up existing and new research efforts across a range of sub-sectors and work areas. It will

447

Semi-Continuous Detection of Mercury in Gases  

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

Continuous Detection of Mercury in Gases Continuous Detection of Mercury in Gases Opportunity Research is currently active on the patented technology "Semi-Continuous Detection of Mercury in Gases." The technology, which is a spinoff of the National Energy Technology Laboratory's (NETL) GP-254 Process (U.S. patent 6,576,092), is available for licensing and/or further collaborative research from the U.S. Department of Energy's NETL. Overview This invention discloses a method for the quantitative detection of heavy metals, especially mercury, in effluent gas streams. The method employs photo-deposition and an array of surface acoustic wave sensors where each sensor monitors a specific metal. The U.S. Environmental Protection Agency issued a national regulation for mercury removal from coal-derived flue and fuel gases in December 2011,

448

Method of producing pyrolysis gases from carbon-containing materials  

DOE Patents [OSTI]

A gasification process of improved efficiency is disclosed. A dual bed reactor system is used in which carbon-containing feedstock materials are first treated in a gasification reactor to form pyrolysis gases. The pyrolysis gases are then directed into a catalytic reactor for the destruction of residual tars/oils in the gases. Temperatures are maintained within the catalytic reactor at a level sufficient to crack the tars/oils in the gases, while avoiding thermal breakdown of the catalysts. In order to minimize problems associated with the deposition of carbon-containing materials on the catalysts during cracking, a gaseous oxidizing agent preferably consisting of air, oxygen, steam, and/or mixtures thereof is introduced into the catalytic reactor at a high flow rate in a direction perpendicular to the longitudinal axis of the reactor. This oxidizes any carbon deposits on the catalysts, which would normally cause catalyst deactivation.

Mudge, Lyle K. (Richland, WA); Brown, Michael D. (West Richland, WA); Wilcox, Wayne A. (Kennewick, WA); Baker, Eddie G. (Richland, WA)

1989-01-01T23:59:59.000Z

449

BIOSIGNATURE GASES IN H?-DOMINATED ATMOSPHERES ON ROCKY EXOPLANETS  

E-Print Network [OSTI]

Super-Earth exoplanets are being discovered with increasing frequency and some will be able to retain stable H2-dominated atmospheres. We study biosignature gases on exoplanets with thin H2 atmospheres and habitable surface ...

Seager, Sara

450

Spontaneous detonation of a mixture of two odd electron gases  

Science Journals Connector (OSTI)

Spontaneous detonation of a mixture of two odd electron gases ... Instructions for safe detonation of ClO2 and NO (the fastest known reaction between two stable molecules at room temperature). ...

Thomas S. Briggs

1991-01-01T23:59:59.000Z

451

Suitability of Non-Energy Greenhouse Gases for Emissions Trading  

Science Journals Connector (OSTI)

This paper assesses the suitability of different sources of non-energy greenhouse gases for emissions trading. Different forms of emissions trading are defined and criteria for determining whether a source is sui...

Erik Haites; Angelo Proestos

2000-01-01T23:59:59.000Z

452

Studying coherence in ultra-cold atomic gases  

E-Print Network [OSTI]

This thesis will discuss the study of coherence properties of ultra-cold atomic gases. The atomic systems investigated include a thermal cloud of atoms, a Bose-Einstein condensate and a fermion pair condensate. In each ...

Miller, Daniel E. (Daniel Edward)

2007-01-01T23:59:59.000Z

453

Liquefied Natural Gas  

Science Journals Connector (OSTI)

SCV systems are also commonly considered in the design of import terminals as shown in Figs. 3.30 and 3.31. Study has shown the operational history, low capital cost, simplicity in design and operational flexib...

G. G. Nasr; N. E. Connor

2014-01-01T23:59:59.000Z

454

Energy loss characteristics of heavy ions in nitrogen, carbon dioxide, argon, hydrocarbon gases and tradescantia tissue  

E-Print Network [OSTI]

Energy loss characteristics of heavy ions in nitrogen, carbon dioxide, argon, hydrocarbon gases and tradescantia tissue

Dennis, J A

1971-01-01T23:59:59.000Z

455

Superfund Record of Decision (EPA Region 7): Pester Refinery, Butler County, El Dorado, KS. (First remedial action), September 1992. Final report  

SciTech Connect (OSTI)

The 10-acre Pester Refinery site is a former petroleum refining facility located in El Dorado, Butler County, Kansas. Petroleum refining operations in the area began in 1917, and from 1958 to 1977, Fina Oil Company operated a petroleum refinery at this site. Process wastes, such as slop-oil emulsion solids, API separator sludge, and heat exchanger bundle cleaning sludge were sent through a pipe to a burn pond. Gaseous waste products were ignited at the end of the pipe, and whatever did not burn was discharged to the pond. The ROD provides a final remedy for the principal source of contamination at the site, the burn pit sludge. The primary contaminants of concern affecting the soil and sludge are VOCs, including ethylbenzene, toluene, and xylenes; other organics, including PAHs and phenols; and metals, including arsenic, chromium, and lead.

Not Available

1992-09-30T23:59:59.000Z

456

Fluid clathrate system for continuous removal of heavy noble gases from mixtures of lighter gases  

DOE Patents [OSTI]

An apparatus and method for separation of heavy noble gas in a gas volume. An apparatus and method have been devised which includes a reservoir containing an oil exhibiting a clathrate effect for heavy noble gases with a reservoir input port and the reservoir is designed to enable the input gas volume to bubble through the oil with the heavy noble gas being absorbed by the oil exhibiting a clathrate effect. The gas having reduced amounts of heavy noble gas is output from the oil reservoir, and the oil having absorbed heavy noble gas can be treated by mechanical agitation and/or heating to desorb the heavy noble gas for analysis and/or containment and allow recycling of the oil to the reservoir.

Gross, Kenneth C. (Bolingbrook, IL); Markun, Francis (Joliet, IL); Zawadzki, Mary T. (South Bend, IN)

1998-01-01T23:59:59.000Z

457

Fluid clathrate system for continuous removal of heavy noble gases from mixtures of lighter gases  

DOE Patents [OSTI]

An apparatus and method are disclosed for separation of heavy noble gas in a gas volume. An apparatus and method have been devised which includes a reservoir containing an oil exhibiting a clathrate effect for heavy noble gases with a reservoir input port and the reservoir is designed to enable the input gas volume to bubble through the oil with the heavy noble gas being absorbed by the oil exhibiting a clathrate effect. The gas having reduced amounts of heavy noble gas is output from the oil reservoir, and the oil having absorbed heavy noble gas can be treated by mechanical agitation and/or heating to desorb the heavy noble gas for analysis and/or containment and allow recycling of the oil to the reservoir. 6 figs.

Gross, K.C.; Markun, F.; Zawadzki, M.T.

1998-04-28T23:59:59.000Z

458

untitled  

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

Refinery Stocks of Crude Oil and Petroleum Products by PAD and Refining Districts, 2012 (Thousand Barrels) Commodity PAD District 1 - East Coast PAD District 2 - Midwest East Coast Appalachian No. 1 Total Indiana, Illinois, Kentucky Minnesota, Wisconsin, North and South Dakota Oklahoma, Kansas, Missouri Total Crude Oil ..................................................................... 6,647 398 7,045 8,842 1,644 1,917 12,403 Petroleum Products ................................................... 17,842 2,339 20,181 30,832 7,611 10,741 49,184 Pentanes Plus .......................................................... - - - 175 - 191 366 Liquefied Petroleum Gases ...................................... 769 34 803 2,779 493 1,377 4,649 Ethane/Ethylene ...................................................

459

TABLE16.CHP:Corel VENTURA  

Gasoline and Diesel Fuel Update (EIA)

6. 6. Refinery Input of Crude Oil and Petroleum Products by PAD and Refining Districts, January 1998 Crude Oil ................................................................... 44,047 2,783 46,830 70,320 12,891 21,794 105,005 Natural Gas Liquids ................................................. 252 0 252 2,613 131 1,076 3,820 Pentanes Plus ....................................................... 0 0 0 202 45 522 769 Liquefied Petroleum Gases ................................... 252 0 252 2,411 86 554 3,051 Ethane ............................................................... 0 0 0 0 0 0 0 Propane ............................................................. 0 0 0 0 0 0 0 Normal Butane .................................................. 162 0 162 1,792 76 435 2,303 Isobutane ..........................................................

460

Emissions Of Greenhouse Gases From Rice Agriculture  

SciTech Connect (OSTI)

This project produced detailed data on the processes that affect methane and nitrous oxide emissions from rice agriculture and their inter-relationships. It defines the shifting roles and potential future of these gases in causing global warming and the benefits and tradeoffs of reducing emissions. The major results include: 1). Mechanisms and Processes Leading to Methane Emissions are Delineated. Our experiments have tested the standard model of methane emissions from rice fields and found new results on the processes that control the flux. A mathematical mass balance model was used to unravel the production, oxidation and transport of methane from rice. The results suggested that when large amounts of organic matter are applied, the additional flux that is observed is due to both greater production and reduced oxidation of methane. 2). Methane Emissions From China Have Been Decreasing Over the Last Two Decades. We have calculated that methane emissions from rice fields have been falling in recent decades. This decrease is particularly large in China. While some of this is due to reduced area of rice agriculture, the bigger effect is from the reduction in the emission factor which is the annual amount of methane emitted per hectare of rice. The two most important changes that cause this decreasing emission from China are the reduced use of organic amendments which have been replaced by commercial nitrogen fertilizers, and the increased practice of intermittent flooding as greater demands are placed on water resources. 3). Global Methane Emissions Have Been Constant For More Than 20 Years. While the concentrations of methane in the atmosphere have been leveling off in recent years, our studies show that this is caused by a near constant total global source of methane for the last 20 years or more. This is probably because as some anthropogenic sources have increased, others, such as the rice agriculture source, have fallen. Changes in natural emissions appear small. 4). Nitrous Oxide Emissions From Rice Fields Increase as Methane Emissions Drop. Inundated conditions favor anaerobic methane production with high emission rates and de-nitrification resulting in modest nitrous oxide emissions. Under drier conditions such as intermittent flooding, methane emissions fall and nitrous oxide emissions increase. Increased nitrogen fertilizer use increases nitrous oxide emissions and is usually accompanied by reduced organic matter applications which decreases methane emissions. These mechanisms cause a generally inverse relationship between methane and nitrous oxide emissions. Reduction of methane from rice agriculture to control global warming comes with tradeoffs with increased nitrous oxide emissions. 5). High Spatial Resolution Maps of Emissions Produced. Maps of methane and nitrous oxide emissions at a resolution of 5 min × 5 min have been produced based on the composite results of this research. These maps are necessary for both scientific and policy uses.

M. Aslam K. Khalil

2009-07-16T23:59:59.000Z

Note: This page contains sample records for the topic "liquefied refinery gases" 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

North Carolina used motor oil re-refining program: site selection, permits, and environmental impact study. [Re-refinery  

SciTech Connect (OSTI)

The State of North Carolina has a used motor oil re-refining program that collects crankcase drainings from various sources, re-refines it in a plant purchased from the Phillips Petroleum Company, and distributes the product to State and other governmental garages. This report describes the steps between the initial decision to establish a used oil re-refining demonstration program and receipt of a final permit to operate a facility. The report covers in some detail those issues faced in obtaining approval to establish the program, select a site, gain permits for construction and operation, prepare an acceptable environmental impact statement, and start re-refining used motor oil. Many of the considerations made during this experience are germaine to other states and to private enterprise, although the details may vary. This is the first in what is expected to be a related series of reports; subsequent numbers will cover the economics of plant acquisition and start-up, technical considerations, and long term operations of the re-refinery.

Griffith, W.C.; Holland, G.M.; Taylor, A.; Taylor, S.

1981-12-01T23:59:59.000Z

462

Methanol production from eucalyptus wood chips. Attachment III. Florida's eucalyptus energy farm and methanol refinery: the background environment  

SciTech Connect (OSTI)

A wide array of general background information is presented on the Central Florida area in which the eucalyptus energy plantation and methanol refinery will be located. Five counties in Central Florida may be affected by the project, DeSoto, Hardee, Hillsborough, Manatee, and Polk. The human resources of the area are reviewed. Included are overviews of population demographic and economic trends. Land use patterns and the transportation are system described, and the region's archeological and recreational resources are evaluated. The region's air quality is emphasized. The overall climate is described along with noise and air shed properties. An analysis of the region's water resources is included. Ground water is discussed first followed by an analysis of surface water. Then the overall quality and water supply/demand balance for the area is evaluated. An overview of the region's biota is presented. Included here are discussions of the general ecosystems in Central Florida, and an analysis of areas with important biological significance. Finally, land resources are examined.

Fishkind, H.H.

1982-04-01T23:59:59.000Z

463

Finalize Historic National Program to Reduce Greenhouse Gases and Improve  

Open Energy Info (EERE)

Finalize Historic National Program to Reduce Greenhouse Gases and Improve Finalize Historic National Program to Reduce Greenhouse Gases and Improve Fuel Economy for Cars and Trucks Jump to: navigation, search Tool Summary LAUNCH TOOL Name: Finalize Historic National Program to Reduce Greenhouse Gases and Improve Fuel Economy for Cars and Trucks Agency/Company /Organization: EPA and NHTSA Focus Area: Standards - Incentives - Policies - Regulations Topics: Policy Impacts Resource Type: Reports, Journal Articles, & Tools Website: www.epa.gov/oms/climate/regulations/420f10014.pdf This document establish a national program consisting of new standards for model year 2012 through 2016 light-duty vehicles that will reduce greenhouse gas emissions and improve fuel economy. EPA is finalizing the first-ever national greenhouse gas (GHG) emissions standards under the

464

Voluntary Reporting of Greenhouse Gases Program - Electricity Factors  

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

Voluntary Reporting Program > Coefficients Voluntary Reporting Program > Coefficients Voluntary Reporting of Greenhouse Gases Program (Voluntary Reporting of Greenhouse Gases Program Fuel Carbon Dioxide Emission Coefficients) Voluntary Reporting of Greenhouse Gases Program Fuel Emission Coefficients Table 1: Carbon Dioxide Emission Factors for Stationary Combustion Table 2: Carbon Dioxide Emission Factors for Transportation Fuels Table 3: Generic Methane and Nitrous Oxide Emission Factors for Stationary Fuel Combustion Table 4: Specific Methane and Nitrous Oxide Emission Factors for Biogenic Fuel Sources Table 5: Methane and Nitrous Oxide Emissions Factors for Highway Vehicles Table 6: Methane and Nitrous Oxide Emission Factors for Alternative Fuel Vehicles Table 7: Methane and Nitrous Oxide Emission Factors for Non-Highway Mobile Combustion

465

Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation  

Open Energy Info (EERE)

Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation (GREET) Model Jump to: navigation, search Tool Summary LAUNCH TOOL Name: Greenhouse Gases, Regulated Emissions, and Energy Use in Transportation (GREET) Model Agency/Company /Organization: Argonne National Laboratory Focus Area: GHG Inventory Development Topics: Analysis Tools Website: greet.es.anl.gov/ This full life-cycle model evaluates the energy and emission impacts of advanced vehicle technologies and new transportation fuels. The model allows users to evaluate various vehicle and fuel combinations. How to Use This Tool This tool is most helpful when using these strategies: Shift - Change to low-carbon modes Improve - Enhance infrastructure & policies Learn more about the avoid, shift, improve framework for limiting air

466

Lattice vibrations of pure and doped GaSe  

SciTech Connect (OSTI)

The Bridgman method is used to grow especially undoped and doped single crystals of GaSe. Composition and impurity content of the grown crystals were determined using X-ray fluorescence (XRF) method. X-ray diffraction, Raman scattering, photoluminescence (PL), and IR transmission measurements were performed at room temperature. The long wavelength lattice vibrations of four modifications of GaSe were described in the framework of modified one-layer linear-chain model which also takes into consideration the interaction of the selenium (Se) atom with the second nearest neighbor gallium (Ga) atom in the same layer. The existence of an eight-layer modification of GaSe is suggested and the vibrational frequencies of this modification are explained in the framework of a lattice dynamical model considered in the present work. Frequencies and the type of vibrations (gap, local, or resonance) for the impurity atoms were calculated and compared with the experimental results.

Allakhverdiev, K. [Materials Institute, Marmara Research Center, TUBITAK, Gebze/Kocaeli 41470 (Turkey) and Institute of Physics, Azerbaijan National Academy of Sciences, Baku AZ1143 (Azerbaijan)]. E-mail: kerim.allahverdi@mam.gov.tr; Baykara, T. [Materials Institute, Marmara Research Center, TUBITAK, Gebze/Kocaeli 41470 (Turkey); Ellialtioglu, S. [Department of Physics, Middle East Technical University, Ankara 06531 (Turkey); Hashimzade, F. [Institute of Physics, Azerbaijan National Academy of Sciences, Baku AZ1143 (Azerbaijan); Huseinova, D. [Institute of Physics, Azerbaijan National Academy of Sciences, Baku AZ1143 (Azerbaijan); Kawamura, K. [Institute of Materials Science, University of Tsukuba 305-8573 (Japan); Kaya, A.A. [Materials Institute, Marmara Research Center, TUBITAK, Gebze/Kocaeli 41470 (Turkey); Kulibekov, A.M. [Department of Physics, Mugla University, Mugla 48000 (Turkey); Onari, S. [Institute of Materials Science, University of Tsukuba 305-8573 (Japan)

2006-04-13T23:59:59.000Z

467

Emissions of greenhouse gases in the United States 1997  

SciTech Connect (OSTI)

This is the sixth annual report on aggregate US national emissions of greenhouse gases. It covers emissions over the period 1990--1996, with preliminary estimates of emissions for 1997. Chapter one summarizes some background information about global climate change and the greenhouse effect. Important recent developments in global climate change activities are discussed, especially the third Conference of the Parties to the Framework Convention on Climate Change, which was held in December of 1997 in Kyoto, Japan. Chapters two through five cover emissions of carbon dioxide, methane, nitrous oxide, halocarbons and related gases, respectively. Chapter six describes potential sequestration and emissions of greenhouse gases as a result of land use changes. Six appendices are included in the report. 96 refs., 38 tabs.

NONE

1998-10-01T23:59:59.000Z

468

Other States Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic  

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

Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic Feet) Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic Feet) Other States Nonhydrocarbon Gases Removed from Natural Gas (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1996 - - - - - - - - - - - - 1997 513 491 515 539 557 534 541 579 574 585 558 573 1998 578 536 591 581 517 456 486 486 471 477 457 468 1999 466 438 489 495 499 510 547 557 544 555 541 579 2000 587 539 605 587 615 570 653 629 591 627 609 611 2001 658 591 677 690 718 694 692 679 686 697 688 700 2002 639 591 587 621 622 605 654 639 649 650 623 638 2003 689 624 649 676 702 691 733 732 704 734 719 748 2004 741 697 727 692 692 688 718 729 706 723 711 718

469

Assess Potential Agency Size Changes to Reduce Greenhouse Gases Using  

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

Assess Potential Agency Size Changes to Reduce Greenhouse Gases Assess Potential Agency Size Changes to Reduce Greenhouse Gases Using Renewable Energy in Buildings Assess Potential Agency Size Changes to Reduce Greenhouse Gases Using Renewable Energy in Buildings October 7, 2013 - 11:15am Addthis To support planning for using renewable energy to reduce greenhouse gas (GHG) emissions at the Federal agency or program-level, it is important to consider what changes to the agencies building or land-holding portfolio may have on opportunities for renewable energy. Changes to consider include: Addition of new buildings or sites to the agencies portfolio Major renovations to existing buildings Office moves into or out of agency-owned or leased space. As is the case with planning energy efficiency measures, planning for renewable energy in new construction can be more cost-effective than

470

Raman/FTIR spectroscopy of oil shale retort gases  

SciTech Connect (OSTI)

A Raman facility was assembled in order to aid in the evaluation of the feasibility of using Raman or FTIR spectroscopy for analyzing gas mixtures of interest in oil shale. Applications considered in oil shale research included both retort monitoring and laboratory kinetic studies. Both techniques gave limits of detection between 10 and 1000 ppM for ten representative pertinent gases. Both techniques are inferior as a general analytical technique for oil shale gas analysis in comparison with mass spectroscopy, which had detection limits between 1 and 50 ppM for the same gases. The conclusion of the feasibility study was to recommend that mass spectroscopic techniques be used for analyzing gases of interest to oil shale.

Richardson, J H; Monaco, S B; Sanborn, R H; Hirschfeld, T B; Taylor, J R

1982-08-01T23:59:59.000Z

471

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

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

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

472

Hazardous Gases VASILIS M. FTHENAKIS Department of Applied Science  

Office of Scientific and Technical Information (OSTI)

Mitigation Options for Mitigation Options for Accidental Releases of Hazardous Gases VASILIS M. FTHENAKIS Department of Applied Science Brookhaven National Laboratory Upton, N Y 11973 ABSTRACT The objective of this paper is to review and compare technologies available for mitigation of unconfined releases of toxic and flammable gases. These technologies indude: secondary confinement, de- inventory, vapor barriers, foam spraying, and water sprays/monitors. Guidelines for the design and/or operation of effective post-release mitigation systems and case studies involving actual industrial mitigation systems are also presented. 1. ACCIDENT PREVENTION & MITIGATION OPTIONS Accident prevention and mitigation in the process industries is based on the military concept of defense in

473

Dissipative dynamics of a Josephson junction in the Bose gases  

SciTech Connect (OSTI)

The dissipative dynamics of a Josephson junction in Bose gases is considered within the framework of the model of a tunneling Hamiltonian. The effective action that describes the dynamics of the phase difference across the junction is derived using the functional integration method. The dynamic equation obtained for the phase difference across the junction is analyzed for the finite temperatures in the low-frequency limit involving the radiation terms. The asymmetric case of the Bose gases with the different order parameters is calculated as well.

Barankov, R.A. [Department of Physics, Massachusetts Institute of Technology, Cambridge, Massachusetts 02139 (United States); Burmistrov, S.N. [RRC 'Kurchatov Institute', Kurchatov Sq.1, 123182 Moscow (Russian Federation)

2003-01-01T23:59:59.000Z

474

Carbonaceous adsorbent regeneration and halocarbon displacement by hydrocarbon gases  

DOE Patents [OSTI]

This invention describes a process for regeneration of halocarbon bearing carbonaceous adsorbents through which a carbonaceous adsorbent is contacted with hydrocarbon gases, preferably propane, butane and pentane at near room temperatures and at atmospheric pressure. As the hydrocarbon gases come in contact with the adsorbent, the hydrocarbons displace the halocarbons by physical adsorption. As a result of using this process, the halocarbon concentration and the hydrocarbon eluant is increased thereby allowing for an easier recovery of pure halocarbons. By using the process of this invention, carbonaceous adsorbents can be regenerated by an inexpensive process which also allows for subsequent re-use of the recovered halocarbons. 8 figures.

Senum, G.I.; Dietz, R.N.

1994-04-05T23:59:59.000Z

475

Carbonaceous adsorbent regeneration and halocarbon displacement by hydrocarbon gases  

DOE Patents [OSTI]

This invention describes a process for regeneration of halocarbon bearing carbonaceous adsorbents through which a carbonaceous adsorbent is contacted with hydrocarbon gases, preferably propane, butane and pentane at near room temperatures and at atmospheric pressure. As the hydrocarbon gases come in contact with the adsorbent, the hydrocarbons displace the halocarbons by physical adsorption. As a result of using this process, the halocarbon concentration and the hydrocarbon eluant is increased thereby allowing for an easier recovery of pure halocarbons. By using the process of this invention, carbonaceous adsorbents can be regenerated by an inexpensive process which also allows for subsequent re-use of the recovered halocarbons.

Senum, Gunnar I. (Patchogue, NY); Dietz, Russell N. (Patchogue, NY)

1994-01-01T23:59:59.000Z

476

Removal of sulfur and nitrogen containing pollutants from discharge gases  

DOE Patents [OSTI]

Oxides of sulfur and of nitrogen are removed from waste gases by reaction with an unsupported copper oxide powder to form copper sulfate. The resulting copper sulfate is dissolved in water to effect separation from insoluble mineral ash and dried to form solid copper sulfate pentahydrate. This solid sulfate is thermally decomposed to finely divided copper oxide powder with high specific surface area. The copper oxide powder is recycled into contact with the waste gases requiring cleanup. A reducing gas can be introduced to convert the oxide of nitrogen pollutants to nitrogen.

Joubert, James I. (Pittsburgh, PA)

1986-01-01T23:59:59.000Z

477

FIG15&16.CHP:Corel VENTURA  

Gasoline and Diesel Fuel Update (EIA)

5. Liquefied Petroleum Gases Supply and Disposition, Figure S16. Liquefied Petroleum Gases Ending Stocks, Jun Jul Aug Sep Oct Nov Dec Jan Feb Mar Apr May Jun Jul 2003 2004 Months 0...

478

Use of low temperature blowers for recirculation of hot gases  

DOE Patents [OSTI]

An apparatus is described for maintaining motors at low operating temperatures during recirculation of hot gases in fuel cell operations and chemical processes such as fluidized bed coal gasification. The apparatus includes a means for separating the hot process gas from the motor using a secondary lower temperature gas, thereby minimizing the temperature increase of the motor and associated accessories.

Maru, H.C.; Forooque, M.

1982-08-19T23:59:59.000Z

479

AER1301: KINETIC THEORY OF GASES Assignment #2  

E-Print Network [OSTI]

AER1301: KINETIC THEORY OF GASES Assignment #2 1. Using the formalism of the text book is as follows. Assume that the particle number density is a slowly varying function of the z coordinate #27; Ã? is a constant. 3. Show that if the potential function, U(r), varies as 1=r 4

Groth, Clinton P. T.

480

AER1301: KINETIC THEORY OF GASES Assignment #2  

E-Print Network [OSTI]

AER1301: KINETIC THEORY OF GASES Assignment #2 1. Using the formalism of the text book the particle number density and temperature are both slowly varying functions of the z coordinate of the previous problem is as follows. Assume that the particle number density is a slowly varying function

Groth, Clinton P. T.

Note: This page contains sample records for the topic "liquefied refinery gases" 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

OPTIONS FOR ABATING GREENHOUSE GASES FROM EXHAUST STREAMS.  

SciTech Connect (OSTI)

This report examines different alternatives for replacing, treating, and recycling greenhouse gases. It is concluded that treatment (abatement) is the only viable short-term option. Three options for abatement that were tested for use in semiconductor facilities are reviewed, and their performance and costs compared. This study shows that effective abatement options are available to the photovoltaic (PV) industry, at reasonable cost.

FTHENAKIS,V.

2001-12-01T23:59:59.000Z

482

THE GREENHOUSE EFFECT RISING GREENHOUSE GASES AND CLIMATE CHANGE  

E-Print Network [OSTI]

, methane, and nitrous oxides. The sun's energy passes through these gases, like light passing through risen by almost 40 percent. This is attributed primarily to the burning of fossil fuels (coal, oil, gasoline). Methane and nitrous oxides are also increasing rapidly, due in part to the expansion

483

Automatic Process Chromatographs for the Analysis of Corrosive Fluoride Gases  

Science Journals Connector (OSTI)

......hexaflu- oride matrix gas by a trapping procedure...the disadvantage of high cost and require skilled and...lacked reliability in gases of high halocarbon coolant...the uranium hexafluoride gas; impurities have a direct effect on production efficiency. Coolant-114......

J. G. Million; W. S. Pappas; C. W. Weber

1969-03-01T23:59:59.000Z

484

Optical Third-Harmonic Coefficients for Inert Gases  

Science Journals Connector (OSTI)

Optical third-harmonic coefficients ?zzzz(3?) for the inert gases have been calculated taking the LS coupling scheme for helium and Jj and jl coupling schemes for neon, argon, and krypton. Our calculated values agree reasonably well with the experimental values of set (i) of Ward and New.

B. P. Tripathi; R. K. Laloraya; S. L. Srivastava

1971-11-01T23:59:59.000Z

485

Mitigation options for accidental releases of hazardous gases  

SciTech Connect (OSTI)

The objective of this paper is to review and compare technologies available for mitigation of unconfined releases of toxic and flammable gases. These technologies include: secondary confinement, deinventory, vapor barriers, foam spraying, and water sprays/monitors. Guidelines for the design and/or operation of effective post-release mitigation systems and case studies involving actual industrial mitigation systems are also presented.

Fthenakis, V.M.

1995-05-01T23:59:59.000Z

486

SAFT Modeling of the Solubility of Gases in Perfluoroalkanes  

Science Journals Connector (OSTI)

SAFT Modeling of the Solubility of Gases in Perfluoroalkanes ... A molecular model within a SAFT context for quantitatively predicting the solubility of xenon and oxygen in n-perfluoroalkanes is presented and discussed here. ... Free-Volume Theory Coupled with Soft-SAFT for Viscosity Calculations: Comparison with Molecular Simulation and Experimental Data ...

Ana M. A. Dias; Josep C. Pàmies; João A. P. Coutinho; Isabel M. Marrucho; Lourdes F. Vega

2003-12-30T23:59:59.000Z

487

Total Energy - Data - U.S. Energy Information Administration (EIA)  

Gasoline and Diesel Fuel Update (EIA)

Petroleum Flow, (Million Barrels per Day) Petroleum Flow, (Million Barrels per Day) Petroleum Energy Flow diagram image Footnotes: 1 Unfinished oils, hydrogen/oxygenates/renewables/other hydrocarbons, and motor gasoline and aviation gasoline blending components. 2 Renewable fuels and oxygenate plant net production (0.972), net imports (1.164) and adjustments (0.122) minus stock change (0.019) and product supplied (0.001). 3 Finished petroleum products, liquefied petroleum gases, and pentanes plus. 4 Natural gas plant liquids. 5 Field production (2.183) and renewable fuels and oxygenate plant net production (-.019) minus refinery and blender net imputs (0.489). 6 Production minus refinery input. (s)= Less than 0.005. Notes: * Data are preliminary. * Values are derived from source data prior to rounding for publication.

488

Working and Net Available Shell Storage Capacity  

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

Net Available Shell Storage Capacity by PAD District as of September 30, 2013 Net Available Shell Storage Capacity by PAD District as of September 30, 2013 (Thousand Barrels) Commodity In Operation Idle 1 In Operation Idle 1 In Operation Idle 1 In Operation Idle 1 In Operation Idle 1 In Operation Idle 1 Refineries Crude Oil 17,334 831 21,870 1,721 86,629 3,468 4,655 174 39,839 1,230 170,327 7,424 Fuel Ethanol 174 - 175 1 289 - 134 - 92 - 864 1 Natural Gas Plant Liquids and Liquefied Refinery Gases 2 1,267 23 11,599 382 28,865 78 641 19 2,412 23 44,784 525 Propane/Propylene (dedicated)

489

Working and Net Available Shell Storage Capacity  

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

Working Storage Capacity by PAD District as of September 30, 2013 Working Storage Capacity by PAD District as of September 30, 2013 (Thousand Barrels) Commodity 1 2 3 4 5 U.S. Total Ending Stocks Utilization Rate 1 Refineries Crude Oil 15,154 17,952 72,858 4,109 35,324 145,397 90,778 62% Fuel Ethanol 151 142 257 114 79 743 482 65% Natural Gas Plant Liquids and Liquefied Refinery Gases 2 1,149 10,996 24,902 581 2,219 39,847 19,539 49% Propane/Propylene (dedicated) 3 405 3,710 3,886 54 199 8,254 4,104 NA Motor Gasoline (incl. Motor Gasoline Blending Components)

490

Fuel.vp  

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

3: Liquefied Petroleum Gases Price and Expenditure Estimates, 2012 State Prices Expenditures Residential Commercial Industrial Transportation Total Residential Commercial...

491

Strongly interacting Fermi gases : non-equilibrium dynamics and dimensional crossover  

E-Print Network [OSTI]

Experiments using ultracold atomic gases address fundamental problems in many-body physics. This thesis describes experiments on strongly-interacting gases of fermionic atoms, with a focus on non-equilibrium physics and ...

Sommer, Ariel T. (Ariel Tjodolv)

2013-01-01T23:59:59.000Z

492

Heat Transfer at Low Temperatures between Tube Walls and Gases in Turbulent Flow  

Science Journals Connector (OSTI)

...September 1947 research-article Heat Transfer at Low Temperatures between Tube...counter-flow system to study heat transfer between tube walls and gases at...Determinations on friction accompanying heat transfer with gases in turbulent flow at...

1947-01-01T23:59:59.000Z

493

Greenhouse Gases (GHG) Emissions from Gas Field Water in Southern Gas Field, Sichuan Basin, China  

Science Journals Connector (OSTI)

In order to assess correctly the gases emissions from oil/gas field water and its contributions to the source of greenhouse gases (GHG) at the atmospheric temperature and pressure, ... first developed to study th...

Guojun Chen; Wei Yang; Xuan Fang; Jiaai Zhong…

2014-03-01T23:59:59.000Z

494

Simultaneous Gas Chromatographic Determination of Four Toxic Gases Generally Present in Combustion Atmospheres  

Science Journals Connector (OSTI)

......determining these gases in mixtures...dioxide, nitrogen, water vapor, and...determining these gases in mixtures...dioxide, nitrogen, water vapor, and...to the solubility of A HCN in water, which was...thevariationin gas con- centrations......

Boyd R. Endecott; Donald C. Sanders; Arvind K. Chaturvedi

1996-01-01T23:59:59.000Z

495

E-Print Network 3.0 - atmospheric gases final Sample Search Results  

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

on Climate and Planets http:icp.giss.nasa.gov The Role of the Atmosphere and Greenhouse Effect in Summary: gases, and scenario 3 - an atmosphere and greenhouse gases. Use...

496

Conceptual design assessment for the co-firing of bio-refinery supplied lignin project. Quarterly report, June 23--July 1, 2000  

SciTech Connect (OSTI)

The Conceptual Design Assessment for the Co-Firing of Bio-Refinery Supplied Lignin Project was successfully kicked off on July 23, 2000 during a meeting at the TVA-PPI facility in Muscle Shoals, AL. An initial timeline for the study was distributed, issues of concern were identified and a priority actions list was developed. Next steps include meeting with NETL to discuss de-watering and lignin fuel testing, the development of the mass balance model and ethanol facility design criteria, providing TVA-Colbert with preliminary lignin fuel analysis and the procurement of representative feed materials for the pilot and bench scale testing of the hydrolysis process.

Berglund, T.; Ranney, J.T.; Babb, C.L.

2000-07-27T23:59:59.000Z

497

System for trapping and storing gases for subsequent chemical reduction to solids  

DOE Patents [OSTI]

A system for quantitatively reducing oxide gases. A pre-selected amount of zinc is provided in a vial. A tube is provided in the vial. The zinc and the tube are separated. A pre-selected amount of a catalyst is provided in the tube. Oxide gases are injected into the vial. The vial, tube, zinc, catalyst, and the oxide gases are cryogenically cooled. At least a portion of the vial, tube, zinc, catalyst, and oxide gases are heated.

Vogel, John S. (San Jose, CA); Ognibene, Ted J. (Oakland, CA); Bench, Graham S. (Livermore, CA); Peaslee, Graham F. (Holland, MI)

2009-11-03T23:59:59.000Z

498

E-Print Network 3.0 - atmospheric greenhouse gases Sample Search...  

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

to longwave radiation 12;Greenhouse Gases Polyatomic molecules... the greenhouse effect ... Source: Frierson, Dargan - Department of Atmospheric Sciences, University of...

499

What are greenhouse gases? Many chemical compounds in the atmosphere act as  

E-Print Network [OSTI]

back into space. However, greenhouse gases will not let all the infrared light pass throughWhat are greenhouse gases? Many chemical compounds in the atmosphere act as greenhouse gases the land and oceans. The warmed Earth releases this heat in the form of infrared light (longwave radiation

500

Modeling of LNG Pool Spreading and Vaporization  

E-Print Network [OSTI]

.............................................................................. 20 CHAPTER III PREVIOUS EXPERIMENTS ON LNG POOL SPREADING .............. 22 3.1. Summary of Experiments on liquefied gases ................................................... 22 CHAPTER IV CURRENT STATE OF THE ART... of liquefied gases into bunds .................................................................... 23 Table 7: Experimental setup for bund experiments.......................................................... 23 Table 8: Spills of liquefied gases onto water...

Basha, Omar 1988-

2012-11-20T23:59:59.000Z