Powered by Deep Web Technologies
Note: This page contains sample records for the topic "refinery bulk terminal" 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

Ohio Distillate Fuel Oil Stocks at Refineries, Bulk Terminals, and ...  

U.S. Energy Information Administration (EIA)

Ohio Distillate Fuel Oil Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

2

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

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

S1","MDGSXUS1","MRESXUS1","MPRSXUS1" "Date","U.S. Finished Motor Gasoline Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)","U.S. Reformulated Motor...

3

U.S. Refinery Grade Butane Stocks at Bulk Terminals (Thousand ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Grade Butane Stocks at Bulk Terminals (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; ...

4

U.S. Refinery Grade Butane Stocks at Bulk Terminals (Thousand ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Grade Butane Stocks at Bulk Terminals (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2005: 1,077: 999: 1,362: ...

5

Wisconsin Propane and Propylene Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

Wisconsin Propane and Propylene Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

6

Colorado Propane and Propylene Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

Colorado Propane and Propylene Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

7

Colorado Finished Motor Gasoline Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

Colorado Finished Motor Gasoline Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

8

Michigan Finished Motor Gasoline Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

Michigan Finished Motor Gasoline Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

9

South Dakota Distillate Fuel Oil Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

South Dakota Distillate Fuel Oil Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

10

South Dakota Propane and Propylene Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

South Dakota Propane and Propylene Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

11

,"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"

12

,"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"

13

Gulf Coast (PADD 3) Refinery Grade Butane Stocks at Bulk ...  

U.S. Energy Information Administration (EIA)

Gulf Coast (PADD 3) Refinery Grade Butane Stocks at Bulk Terminals (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2005: 935: ...

14

Motor Gasoline Blending Components Refinery, Bulk Terminal ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Distillate stocks ...

15

EIA-811 MONTHLY BULK TERMINAL REPORT INSTRUCTIONS  

U.S. Energy Information Administration (EIA)

EIA-811, Monthly Bulk Terminal Report Page 1 U.S. DEPARTMENT OF ENERGY ENERGY IN FORMATION ADMINISTRATION Washington, D.C. 20585 OMB No. 1905-0165

16

Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant  

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 U.S. 31,576 31,334 35,019 34,533 32,174 27,872 1993-2013 PAD District 1 2,286 2,947 3,296 3,722 3,755 2,837 1993-2013 Connecticut 1993-2005 Delaware 1993-2010 Florida 635 638 666 711 724 563 1993-2013 Georgia 179 213 239 277 244 191 1993-2013 Maine 126 263 324 270 310 112 1993-2013 Maryland 1993-2009 Massachusetts 7 6 7 5 8 7 1993-2013 New Hampshire 1993-2006 New Jersey 206 344 270 604 785 463 1993-2013 New York 325 455 535 508 465 521 1993-2013 North Carolina 251 387 522 535 457 320 1993-2013 Pennsylvania 116 165 232 202 234 178 1993-2013 Rhode Island 1993-2007 South Carolina 250 237 271 306 293 275 1993-2013 Vermont 20 30 19 15 24 19 1993-2013

17

Colorado Refinery, Bulk Terminal, and Natural Gas Plant Stocks ...  

U.S. Energy Information Administration (EIA)

456: 469: 693: 609: 461: 1993-2013: Conventional: 525: 456: 469: 693: 609: 461: 1993-2013: Motor Gasoline Blending Components: 663: 618: 638: 657: 682: 730: 2005-2013 ...

18

New Jersey Refinery, Bulk Terminal, and Natural Gas Plant ...  

U.S. Energy Information Administration (EIA)

Notes: Distillate stocks located in the Northeast Heating Oil Reserve are not included. Stocks are reported as of the last day of the month.

19

Iowa Refinery, Bulk Terminal, and Natural Gas Plant Stocks of ...  

U.S. Energy Information Administration (EIA)

Notes: Distillate stocks located in the Northeast Heating Oil Reserve are not included. Stocks are reported as of the last day of the month.

20

West Virginia Refinery, Bulk Terminal, and Natural Gas Plant ...  

U.S. Energy Information Administration (EIA)

Notes: Distillate stocks located in the Northeast Heating Oil Reserve are not included. Stocks are reported as of the last day of the month.

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Oregon Refinery, Bulk Terminal, and Natural Gas Plant Stocks ...  

U.S. Energy Information Administration (EIA)

Notes: Distillate stocks located in the Northeast Heating Oil Reserve are not included. Stocks are reported as of the last day of the month.

22

Kentucky Refinery, Bulk Terminal, and Natural Gas Plant Stocks ...  

U.S. Energy Information Administration (EIA)

Notes: Distillate stocks located in the Northeast Heating Oil Reserve are not included. Stocks are reported as of the last day of the month.

23

Ohio Refinery, Bulk Terminal, and Natural Gas Plant Stocks of ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Distillate stocks ...

24

Refinery Grade Butane Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

25

Michigan Refinery, Bulk Terminal, and Natural Gas Plant Stocks of ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Distillate stocks ...

26

Idaho Refinery, Bulk Terminal, and Natural Gas Plant Stocks of ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Distillate stocks ...

27

Finished Motor Gasoline Refinery, Bulk Terminal, and Natural Gas Plant  

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

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History U.S. 71,470 61,525 55,254 40,534 39,717 37,768 1993-2012 PAD District 1 19,732 16,074 10,858 3,913 3,741 3,513 1993-2012 Connecticut 1993-2004 Delaware 292 105 498 1993-2009 Florida 4,484 1,877 914 586 734 747 1993-2012 Georgia 2,141 1,724 800 374 251 220 1993-2012 Maine 889 374 130 152 1993-2012 Maryland 67 31 1993-2008 Massachusetts 2 4 3 1993-2012 New Hampshire 1993-2005 New Jersey 1,982 2,956 2,026 667 275 795 1993-2012 New York 1,768 1,469 273 194 628 483 1993-2012 North Carolina 1,977 1,724 1,470 591 389 317 1993-2012 Pennsylvania 3,731 3,595 3,421 697 782 188 1993-2012 Rhode Island 1993-2005 South Carolina 839 720 787 444 276 288 1993-2012

28

Stacker-reclaimer scheduling in a dry bulk terminal  

Science Conference Proceedings (OSTI)

A dry bulk terminal acts as a multi-modal interface for transhipping iron ores. Stacker-reclaimers are the dedicated equipments in storage yard for iron ore handling. Both unloading and loading processes are supported by stacker-reclaimers in most cases. ... Keywords: dry bulk terminal, genetic algorithm, lower bound, stacker-reclaimer scheduling

Dayong Hu; Zhenqiang Yao

2012-11-01T23:59:59.000Z

29

Washington, D. C. 20585 EIA-815 MONTHLY BULK TERMINAL AND ...  

U.S. Energy Information Administration (EIA)

instructions, please contact the Manager at Survey (202) 586-3536. PURPOSE . ... often blending of petroleum products and has total bulk shell

30

Distillate Fuel Oil Refinery, Bulk Terminal, and Natural Gas Plant Stocks  

Gasoline and Diesel Fuel Update (EIA)

May-13 Jun-13 Jul-13 Aug-13 Sep-13 Oct-13 View May-13 Jun-13 Jul-13 Aug-13 Sep-13 Oct-13 View History U.S. 91,312 93,175 97,872 97,384 98,180 87,471 1993-2013 PAD District 1 27,017 30,786 32,127 33,208 33,382 29,157 1993-2013 Connecticut 1,014 1,154 1,120 1,502 1,791 1,688 1993-2013 Delaware 560 578 385 599 686 319 1993-2013 District of Columbia 1993-2004 Florida 1,990 2,023 2,226 2,051 2,270 1,838 1993-2013 Georgia 1,192 1,278 1,161 1,174 1,257 1,003 1993-2013 Maine 1,180 1,147 1,033 969 1,076 1,200 1993-2013 Maryland 822 1,446 1,543 1,592 1,506 940 1993-2013 Massachusetts 1,258 1,358 1,615 1,490 1,827 2,066 1993-2013 New Hampshire 239 238 224 158 254 542 1993-2013 New Jersey 6,805 8,676 9,534 10,341 9,576 7,169 1993-2013 New York 2,734 3,650 3,433 4,141 3,783 3,601 1993-2013

31

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

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

Area: U.S. PAD District 1 Connecticut Delaware District of Columbia Florida Georgia Maine Maryland Massachusetts New Hampshire New Jersey New York North Carolina Pennsylvania Rhode Island South Carolina Vermont Virginia West Virginia PAD District 2 Illinois Indiana Iowa Kansas Kentucky Michigan Minnesota Missouri Nebraska North Dakota Ohio Oklahoma South Dakota Tennessee Wisconsin PAD District 3 Alabama Arkansas Louisiana Mississippi New Mexico Texas PAD District 4 Colorado Idaho Montana Utah Wyoming PAD District 5 Alaska Arizona California Hawaii Nevada Oregon Washington Period-Unit: Monthly-Thousand Barrels Annual-Thousand Barrels

32

Refinery Capacity Report  

U.S. Energy Information Administration (EIA)

Explanatory Notes Survey Methodology Description of Survey Form The Form EIA-820, “Annual Refinery Report,” is the primary source of data in the “Refinery ...

33

Texas facility treats, recycles refinery, petrochemical wastes  

Science Conference Proceedings (OSTI)

A US Gulf Coast environmental services company is treating refinery and petrochemical plant wastes to universal treatment standards (UTS). DuraTherm Inc.`s recycling center uses thermal desorption to treat a variety of refinery wastes and other hazardous materials. The plant is located in San Leon, Tex., near the major Houston/Texas City refining and petrochemical center. DuraTherm`s customers include major US refining companies, plus petrochemical, terminal, pipeline, transportation, and remediation companies. Examples of typical contaminant concentrations and treatment levels for refinery wastes are shown. The paper discusses thermal desorption, the process description and testing.

NONE

1996-09-16T23:59:59.000Z

34

Refinery Capacity Report 2007  

Reports and Publications (EIA)

Data series include fuel, electricity, and steam purchased for consumption at the refinery; refinery receipts of crude oil by method of transportation; current and projected capacities for atmospheric crude oil distillation, downstream charge, production, and storage 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.

Information Center

2007-06-29T23:59:59.000Z

35

Refinery Capacity Report 2009  

Reports and Publications (EIA)

Data series include fuel, electricity, and steam purchased for consumption at the refinery; refinery receipts of crude oil by method of transportation; current and projected capacities for atmospheric crude oil distillation, downstream charge, production, and storage 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.

Information Center

2009-06-25T23:59:59.000Z

36

Refinery Capacity Report 2008  

Reports and Publications (EIA)

Data series include fuel, electricity, and steam purchased for consumption at the refinery; refinery receipts of crude oil by method of transportation; current and projected capacities for atmospheric crude oil distillation, downstream charge, production, and storage 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.

Information Center

2008-06-20T23:59:59.000Z

37

Bulk Terminal Reports FAQ  

U.S. Energy Information Administration (EIA)

... to EIA as "distillate fuel oil 15 ppm sulfur and under" include fuel with sulfur content greater than 15 ppm but within test tolerance, ...

38

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.

39

Tables - Refinery Capacity Report  

U.S. Energy Information Administration (EIA)

Tables: 1: Number and Capacity of Operable Petroleum Refineries by PAD District and State as of January 1, 2009: PDF: 2: Production Capacity of Operable ...

40

Table 9. Refinery Receipts of Crude Oil by Method of ...  

U.S. Energy Information Administration (EIA)

Refinery Receipts of Crude Oil by Method of ... "Annual Refinery Report." 49 Energy Information Administration, Refinery Capacity 2011. Title: Refinery ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Oklahoma, Kansas, Missouri Refinery District API Gravity ...  

U.S. Energy Information Administration (EIA)

Oklahoma, Kansas, Missouri Refinery District API Gravity (Weighted Average) of Crude Oil Input to Refineries (Degree)

42

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

43

Status of Texas refineries, 1982  

Science Conference Proceedings (OSTI)

This report is a survey of current operations of the Texas refineries during the 1979-82 market slump using publicly available data from the US Department of Energy and the Texas Railroad Commission. The report looks at the small inland refineries, the large inland refineries, the small coastal refineries, the large coastal refineries in Texas, and the Louisiana coastal refineries. The report suggests that about 200 mb/d of inland capacity and 1.3 million b/d of coastal capacity has been permanently idled.

Langston, V.C.

1983-03-01T23:59:59.000Z

44

Texas Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Atmospheric Crude Oil Distillation Capacity : Operable ... Idle refineries represent refineries where distillation units were completely idle but not ...

45

Colorado Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Atmospheric Crude Oil Distillation Capacity : Operable ... Idle refineries represent refineries where distillation units were completely idle but not ...

46

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

47

Optimization of refinery hydrogen network  

Science Conference Proceedings (OSTI)

Tighter environmental regulations and more heavy-end upgrading in the petroleum industry lead to increased demand for hydrogen in oil refineries. In this paper, the method proposed to optimize the refinery hydrogen network is based upon mathematical ... Keywords: hydrogen management, optimization, refinery, superstructure

Yunqiang Jiao; Hongye Su

2010-09-01T23:59:59.000Z

48

U.S. Bulk Terminal  

U.S. Energy Information Administration (EIA)

930: 1,371: 602: 648: 717: 2005-2012: Other: 13,151: 12,460: 14,651: 11,798: 14,714: 17,885: 2005-2012: Finished Motor Gasoline: 48,549: 40,930: 37,645: 26,306 ...

49

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......................................

50

Texas Gulf Coast Refinery District API Gravity (Weighted ...  

U.S. Energy Information Administration (EIA)

Texas Gulf Coast Refinery District API Gravity (Weighted Average) of Crude Oil Input to Refineries (Degree)

51

Texas Gulf Coast Refinery District API Gravity (Weighted Average ...  

U.S. Energy Information Administration (EIA)

Texas Gulf Coast Refinery District API Gravity (Weighted Average) of Crude Oil Input to Refineries (Degree)

52

Appalachian No. 1 Refinery District Sulfur Content (Weighted ...  

U.S. Energy Information Administration (EIA)

Appalachian No. 1 Refinery District Sulfur Content (Weighted Average) of Crude Oil Input to Refineries (Percent)

53

EIA-820 ANNUAL REFINERY REPORT INSTRUCTIONS  

U.S. Energy Information Administration (EIA)

EIA-820, Annual Refinery Report Page 1 U.S. DEPARTMENT OF ENERGY ... production outside the refinery gate. Note: capacity should include base stocks and process oils

54

Indiana Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Notes: Idle refineries represent refineries where distillation units were completely idle but not permanently shutdown as of January 1 of the year.

55

Number of Idle Refineries - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Notes: Idle refineries represent refineries where distillation units were completely idle but not permanently shutdown as of January 1 of the year.

56

California Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Notes: Idle refineries represent refineries where distillation units were completely idle but not permanently shutdown as of January 1 of the year.

57

Refinery, petrochemical plant injuries decline  

Science Conference Proceedings (OSTI)

The National Petroleum Refiners Association (NPRA) reports a 7% reduction in workplace injury and illness incidence rates for refineries in 1993, and a 21% decrease for petrochemical plants. The report summarizes data from 135 of the 162 US member refineries, and 117 of the 172 US member petrochemical plants. This paper summarizes the report findings.

Not Available

1994-07-25T23:59:59.000Z

58

Puerto Rico Refinery Catalytic Reforming Downstream Charge ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Catalytic Reforming Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

59

Puerto Rico Refinery Desulfurization, Gasoline Downstream Charge ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Desulfurization, Gasoline Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

60

Mississippi Refinery Catalytic Reforming Downstream Charge ...  

U.S. Energy Information Administration (EIA)

Mississippi Refinery Catalytic Reforming Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Louisiana Refinery Catalytic Reforming Downstream Charge Capacity ...  

U.S. Energy Information Administration (EIA)

Louisiana Refinery Catalytic Reforming Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

62

Oklahoma Refinery Vacuum Distillation Downstream Charge Capacity ...  

U.S. Energy Information Administration (EIA)

Oklahoma Refinery Vacuum Distillation Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

63

Mississippi Refinery Vacuum Distillation Downstream Charge ...  

U.S. Energy Information Administration (EIA)

Mississippi Refinery Vacuum Distillation Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

64

Georgia Refinery Marketable Petroleum Coke Production Capacity ...  

U.S. Energy Information Administration (EIA)

Georgia Refinery Marketable Petroleum Coke Production Capacity as of January 1 (Barrels per Stream Day)

65

Minnesota Refinery Marketable Petroleum Coke Production ...  

U.S. Energy Information Administration (EIA)

Minnesota Refinery Marketable Petroleum Coke Production Capacity as of January 1 (Barrels per Stream Day)

66

Biological treatment of refinery wastes  

SciTech Connect

A detailed study of the treatment situation at a Thai refinery that used an API separator with no equalization tank, followed by an activated-sludge system, showed that only 42% of the total COD and 57% of the soluble COD was degradable. In a study of the possibility of additional treatments, an aerated lagoon showed promising results. The wastewater composition of the three main Thai refineries was surveyed.

Mahmud, Z.; Thanh, N.C.

1978-01-01T23:59:59.000Z

67

New Jersey Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Atmospheric Crude Oil Distillation Capacity : Operable ... Idle refineries represent refineries where distillation units were completely idle but not ...

68

Motiva Refinery | Department of Energy  

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

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

69

Refinery suppliers face tough times  

SciTech Connect

Despite a handful of bright spots in hydroprocessing and petrochemical sectors, economic woes plague much of the refinery and petrochemical catalysts business, as suppliers are feeling the impact of mature markets and refiners` ongoing cost cutting. Industry experts say the doldrums could spur further restructuring in the catalyst business, with suppliers scrambling for market share and jockeying for position in growing sectors. Expect further consolidation over the next several years, says Pierre Bonnifay, president of IFP Enterprises (New York). {open_quotes}There are still too many players for the mature [refinery catalyst] markets.{close_quotes} Others agree. {open_quotes}Only about seven [or] eight major suppliers will survive,{close_quotes} says Robert Allsmiller, v.p./refinery and petrochemical catalysts at United Catalysts Inc. (UCI; Louisville, KY). {open_quotes}Who they [will be] is still up in the air.{close_quotes}

Rotman, D.; Walsh, K.

1997-03-12T23:59:59.000Z

70

Refinery Capacity Report - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Respondents are operators of all operating and idle petroleum refineries ... Sources & Uses Petroleum Coal Natural Gas Renewable Nuclear Electricity Consumption

71

Louisiana Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

72

Delaware Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

73

Washington Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

74

Ohio Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

75

Mississippi Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

76

Utah Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

77

Number of Operating Refineries - Energy Information Administration  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

78

Montana Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

79

Oklahoma Refinery Catalytic Hydrotreating, Heavy Gas Oil ...  

U.S. Energy Information Administration (EIA)

Cat. Hydro. Heavy Gas Oil Downstream Charge Capacity (B/SD)y ; Oklahoma Downstream Charge Capacity of Operable Petroleum Refineries ...

80

Alaska Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Florida Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

82

Mississippi Refinery Catalytic Hydrotreating, Heavy Gas Oil ...  

U.S. Energy Information Administration (EIA)

Cat. Hydro. Heavy Gas Oil Downstream Charge Capacity (B/SD)y ; Mississippi Downstream Charge Capacity of Operable Petroleum Refineries ...

83

Nebraska Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

84

North Carolina Refinery Operable Atmospheric Crude Oil ...  

U.S. Energy Information Administration (EIA)

North Carolina Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

85

Michigan Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

86

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

87

Kansas refinery starts up coke gasification unit  

SciTech Connect

Texaco Refining and Marketing Inc. has started up a gasification unit at its El Dorado, Kan., refinery. The unit gasifies delayed coke and other refinery waste products. This is the first refinery to install a coke-fueled gasification unit for power generation. Start-up of the $80-million gasification-based power plant was completed in mid-June. The gasifier produces syngas which, along with natural gas, fuels a combustion turbine. The turbine produces virtually 100% of the refinery`s electricity needs and enough heat to generate 40% of its steam requirements.

Rhodes, A.K.

1996-08-05T23:59:59.000Z

88

California Propane and Propylene Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

456: 500: 619: 658: 659: 520: 1997: 283: 106: 204: 189: 307: 491: 580: 701: 737: 744: 844: 686: 1998: 403: 371: 278: 208: 293: 407: 529: 675: 775: 731: 696: 466: 1999 ...

89

Pennsylvania Distillate Fuel Oil Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

4,982: 4,744: 4,148: 3,926: 4,130: 4,332: 4,926: 4,971: 5,676: 5,851: 5,616: 5,552: 2006: 6,654: 5,231: 5,117: 5,523: 5,220: 4,623: 5,521: 6,339: 6,777: 6,919: 7,299 ...

90

Connecticut Distillate Fuel Oil Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

4,982: 2005: 3,001: 2,111: 2,114: 2,195: 3,100: 4,736: 5,955: 6,270: 6,002: 5,616: 5,152: 5,159: 2006: 5,590: 4,814: 4,284: 3,883: 4,145: 5,351: 5,844: 5,667: 5,938 ...

91

Indiana Reformulated Motor Gasoline Stocks at Refineries, Bulk ...  

U.S. Energy Information Administration (EIA)

241: 219: 111: 104: 124: 59: 2000: 155: 107: 66: 257: 359: 337: 443: 341: 213: 209: 81: 74: 2001: 416: 699: 131: 227: 419: 342: 396: 200: 273: 262: 253: 185: 2002 ...

92

Refinery and Blender Net Inputs  

Annual Energy Outlook 2012 (EIA)

Refinery and Blender Net Inputs Crude OIl ... 14.54 15.14 15.26 15.08 14.51 15.30 15.70 14.93 14.47 15.30 15.54 14.97 15.01...

93

Web based multilayered distributed SCADA/HMI system in refinery application  

Science Conference Proceedings (OSTI)

The paper describes system synthesis and architecture of a multilayered distributed SCADA/HMI system. The system is used for monitoring and control of refinery terminals for truck loading and oil products pipeline shipping. Network-centered, distributed ... Keywords: Data server, Fieldbuses, OPC protocols, Real time systems, SCADA/HMI

Adnan Salihbegovic; Vlatko Marinkovi?; Zoran Cico; Elvedin Karavdi?; Nina Delic

2009-03-01T23:59:59.000Z

94

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 of various techniques and approaches, dependent on the local environment and effectiveness of the Encon program. In this paper, we begin with the importance for stimulating personnel, note the essential ingredients required to motivate our people, and briefly review several techniques used for Encon motivation. Two examples of Encon motivation programs are presented before introducing the characteristics of a successful Encon motivation program. The paper concludes with a review of the needs and suggestions for maintaining a continuing program. Energy utilization efficiency in Esso Europe's refineries improved about 16% in the mid 70's, due primarily to Encon motivation. Experience has since demonstrated that additional improvements can be achieved through operational and maintenance practices.

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

1982-01-01T23:59:59.000Z

95

Table 12. Refinery Sales During 2010  

U.S. Energy Information Administration (EIA)

Former Corporation/Refiner Total Atmospheric Crude Oil Distillation Capacity (bbl/cd) New Corporation/Refiner Date of Sale Table 12. Refinery Sales During 2010

96

Opportunities for Biorenewables in Petroleum Refineries  

Science Conference Proceedings (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

97

Opportunities for Biorenewables in Petroleum Refineries  

SciTech Connect

A presentation by UOP based on collaborative work from FY05 using some results from PNNL for upgrading biomass pyrolysis oil to petroleum refinery feedstock

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

2007-02-01T23:59:59.000Z

98

Areas of Corrosion in the Refinery  

Science Conference Proceedings (OSTI)

...J.D. Poindexter, Corrosion Inhibitors for Crude Oil Refineries, Corrosion: Fundamentals, Testing, and Protection, Vol 13A, ASM Handbook, ASM International, 2003, p 887â??890...

99

Refinery Investments and Future Market Incentives  

U.S. Energy Information Administration (EIA)

Presentation given at the Annual NPRA Meeting that discusses factors affecting refinery investments. Refiners have plunged from a seeming “golden age” investment ...

100

Refinery Capacity Report - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Energy Information Administration (U.S. Dept. of Energy) ... Tables: 1: Number and Capacity of Operable Petroleum Refineries by PAD District and State as of ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

A Louisiana Refinery Success Story  

E-Print Network (OSTI)

"Refining 155,000 barrels of crude oil daily, a Louisiana plant markets oil products to gas stations in at least 26 states, including Washington, D.C. The plant uses 8,538 steam traps with 1,200-, 600-, 250-, 75-, 40- and 15-psi nominal pressures. Standardized with inverted bucket steam traps, the Louisiana refinery’s maintenance and energy coordinator was content with the results. The Spirax Sarco Inc (SSI) team demonstrated SSI’s Energy Service Group (ESG) capabilities and successes to the refinery 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 program, for example, the SSI team presented an ROI with less than six months payback. The ESG survey found that only 3,952 (46.3%) of the steam traps were operating correctly. The remaining steam traps experienced a variety of failures, including: 613 (7.2%) that failed open; 2,763 (32.4%) were cold; 1,012 (11.9%) that failed closed; 6 (0.0%) exhibited rapid cycling; and 192 (2.2%) were disconnected. The team also found performance and temperature issues with the HP sulfur reactors in the SRU units, largely due to the application of inverted bucket steam traps. Plus, as a result of excessive steam leaks, the sulfur reactors were creating a safety hazard. When these results were presented, management agreed that the sulfur reactors needed process improvement. The SSI team recommended replacing the inverted bucket steam traps with 1-1/2-in. strainers and 1-1/2-in. flanged float & thermostatic steam traps. They also suggested that the existing trap discharge piping should be removed and re-piped with globe-style bypass valves and gate-style isolation valves to reduce flow velocity. Once the SSI team began negotiations, it only took one survey for the Louisiana refinery to realize all the energy savings opportunities. In fact, the ESG survey uncovered more than $1.3 million in steam losses through failed steam traps and another $1 million in steam leak opportunities and production, process, safety and environmental improvements. Impressed with the survey results, the refinery approved the estimated $110,000 turnkey project, which offered a 5.3-month payback. Further negotiations netted the team annual steam trap surveys for the next three years, as well as an approved 2008 energy budget of $600,000. Additionally, the Louisiana refinery has indicated that upon successful completion of the ESG program, SSI’s annual energy budget will increase to $1,000,000."

Kacsur, D.

2009-05-01T23:59:59.000Z

102

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network (OSTI)

MTC. Marano, J.J. , 2003. Refinery Technology Profiles:Deep Desulfurization of Oil Refinery Streams: A Review. FuelSavings for Flying J Refinery. Oil & Gas Journal, December 2

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

103

Table 2. Production Capacity of Operable Petroleum Refineries by ...  

U.S. Energy Information Administration (EIA)

Includes hydrogen production capacity of hydrogen plants on refinery grounds. MMcfd = Million cubic feet per day. a ... (EIA), Form EIA-820, "Annual Refinery Report."

104

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network (OSTI)

fuels in the graph. Source: Petroleum Supply Annual, Energypetroleum products, refineries are still a substantial sourceadded produced by petroleum refineries. Source: U.S. Census,

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

105

Refinery receipts of crude oil by rail, truck, and barge ...  

U.S. Energy Information Administration (EIA)

While refinery receipts of crude by truck, rail, and barge remain a small percentage of total receipts, EIA's recently released Refinery Capacity ...

106

Petroleum refineries vary by level of complexity - Today in Energy ...  

U.S. Energy Information Administration (EIA)

A refinery is an industrial complex that manufactures petroleum products, such as gasoline, from crude oil and other feedstocks. Many different types of refineries ...

107

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network (OSTI)

Aspropyrgos Refinery Combined Cycle Cogeneration System.refineries operate combined cycles with higher efficiencies.in an Integrated Gasifier Combined Cycle (IGCC). In this

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

108

EIA-800 WEEKLY REFINERY AND FRACTIONATOR REPORT INSTRUCTIONS  

U.S. Energy Information Administration (EIA)

EIA-800, Weekly Refinery and Fractionator Report Page 3 Crude Oil (Code 050) Report all refinery input of domestic and foreign crude oil (including ...

109

PAD District 4 Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

Notes: Idle refineries represent refineries where distillation units were completely idle but not permanently shutdown as of January 1 of the year.

110

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

111

Refinery burner simulation design architecture summary.  

SciTech Connect

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

112

Take an integrated approach to refinery automation  

Science Conference Proceedings (OSTI)

An integrated approach to designing refinery automation systems is essential to guaranteeing systems compatibility and maximizing benefits. Several aspects of implementing integrated refinery automation should be considered early in the project. Many refineries have major parts of their business automated, starting from corporate planning at the higher level, down to DCS and field instrumentation. A typical refinery automation system architecture of the mid-eighties is shown. Automation systems help refineries improve their business through: Rationalization of man power; Increased throughputs; Reduced give-away; Reduced energy consumption; Better response to market demands and changes; Effective use of offsite areas through scheduling and automatic line-up systems; Reduced losses; and Decision support systems.

Wadi, I. (Abu Dhabi National Oil Co. (United Arab Emirates))

1993-09-01T23:59:59.000Z

113

Kerosene Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

114

Gulf Coast (PADD 3) Bulk Terminal  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

115

EIA-801 WEEKLY BULK TERMINAL REPORT INSTRUCTIONS  

U.S. Energy Information Administration (EIA)

the context of emergency response planning and actual emergencies. SANCTIONS The timely submission of Form EIA-801 by those required to

116

Documentation: The automated ORAD (Oil Refinery and Distribution Model) to RYMs (Refinery Yield Model) linked system  

SciTech Connect

The Refinery Evaluation Modeling System (REMS) is an analytic tool used by the Energy Information Administration (EIA) to provide insight into the domestic operations of United States refineries. REMS can be used to determine the potential impacts of changes in demands for petroleum products, crude and feedstock qualities, refinery processing capacities, foreign and domestic crude availabilities, transportation modes and costs, and government regulations. REMS is a set of linear programming models that solve for a partial equilibrium in the US refinery market by equating supply and demand while maximizing profits for US refiners. REMS consists of two models: the Refinery Yield Model (RYM), and the Oil Refinery and Distribution Model (ORAD). RYMs consists of nine separate regional models that represent the contiguous US refinery system. These nine regions are aggregates of the 13 Bureau of Mines (BOM) refinery districts. ORAD integrates the results from the individual RYMs into a transportation network which represents the US refinery market. ORAD uses the extreme point refinery representation from RYMs to solve for the optimal product prices in ORAD.

Sanders, R.P.; Kydes, A.S.

1987-01-01T23:59:59.000Z

117

Colorado Refinery Marketable Petroleum Coke Production Capacity as ...  

U.S. Energy Information Administration (EIA)

Colorado Refinery Marketable Petroleum Coke Production Capacity as of January 1 (Barrels per Stream Day)

118

Midwest (PADD 2) Refinery and Blender Net Production of ...  

U.S. Energy Information Administration (EIA)

Midwest (PADD 2) Refinery and Blender Net Production of Finished Motor Gasoline (Thousand Barrels per Day)

119

Guam Refinery Operable Atmospheric Crude Oil Distillation Capacity ...  

U.S. Energy Information Administration (EIA)

Guam Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

120

Rocky Mountains (PADD 4) Gross Inputs to Refineries (Thousand ...  

U.S. Energy Information Administration (EIA)

Gross Input to Atmospheric Crude Oil Distillation Units ; PAD District 4 Refinery Utilization and Capacity ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

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:

122

Wastewater reuse and recycle in petroleum refineries  

SciTech Connect

The objectives of this study were to identify feasible reuse and recycle techniques that can be successful in reducing wastewater discharge and to estimate their associated costs. Wastewater reduction is a fundamental aspect of the US EPA's proposed regulations for the petroleum refining industry. EPA undertook this study to confirm the cost estimates used in the proposed guidelines, to identify specific technologies, and to accurately assess their costs. Fifteen refineries were chosen to represent the range of refinery characteristics including crude capacity, process employed, and wastewater generation. Significant wastewater reductions were found possible at 12 refineries studied.

Langer, B.S.

1983-05-01T23:59:59.000Z

123

Former Soviet refineries face modernization, restructuring  

Science Conference Proceedings (OSTI)

A massive modernization and restructuring program is under way in the refining sector of Russia and other former Soviet republics. Economic reforms and resulting economic dislocation following the collapse of the Soviet Union has left refineries in the region grappling with a steep decline and changes in product demand. At the same time, rising oil prices and an aging, dilapidated infrastructure promise a massive shakeout. Even as many refineries in the former Soviet Union (FSU) face possible closure because they are running at a fraction of capacity, a host of revamps, expansions, and grass roots refineries are planned or under way. The paper discusses plans.

Not Available

1993-11-29T23:59:59.000Z

124

A Texas Refinery Success Story  

E-Print Network (OSTI)

"Common knowledge rules that maintenance is the key to long-lasting machinery performance. Yet steam traps are often left to their own devices, to fail or succeed alone. And without steam trap programs, plants are certain to experience a high failure rate. An oil refinery in Texas was continuously experiencing a high failure rate on its 4,790-steam trap system. Finally, the steam losses were judged to be too high, and plant management called on Spirax Sarco Inc. (SSI) to reduce costs. The SSI team noticed symptoms of subpar efficiency within the steam system. Steam traps were improperly installed, water hammer problems were evident and the condensate recovery system was damaged."

Kacsur, D.

2009-05-01T23:59:59.000Z

125

Inbicon Biomass Refinery Cellulosic Ethanol Technology Platforms  

U.S. Energy Information Administration (EIA)

for biogas production Inbicon Biomass Refinery Energy integrated solutions Wheat Straw 50 t/h (at 86 % dm) C5 molasses Power The Lignin and biogas are used in power

126

Motiva Enterprises Refinery Expansion Groundbreaking | Department...  

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

it. When this expansion is complete this facility which is now one of the preeminent refineries on the Gulf Coast will become the largest in the United States and one of the...

127

Refinery siting workbook: appendices A and B  

Science Conference Proceedings (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

128

Retrofitting analysis of integrated bio-refineries  

E-Print Network (OSTI)

A bio-refinery is a processing facility that produces liquid transportation fuels and/or value-added chemicals and other products. Because of the dwindling resources and escalating prices of fossil fuels, there are emerging situations in which the economic performance of fossil-based facilities can be enhanced by retrofitting and incorporation of bio-mass feedstocks. These systems can be regarded as bio-refineries or integrated fossilbio- refineries. This work presents a retrofitting analysis to integrated bio-refineries. Focus is given to the problem of process modification to an existing plant by considering capacity expansion and material substitution with biomass feedstocks. Process integration studies were conducted to determine cost-effective strategies for enhancing production and for incorporating biomass into the process. Energy and mass integration approaches were used to induce synergism and to reduce cost by exchanging heat, material utilities, and by sharing equipment. Cost-benefit analysis was used to guide the decision-making process and to compare various production routes. Ethanol production from two routes was used as a case study to illustrate the applicability of the proposed approach and the results were bio-refinery has become more attractive then fossil-refinery.

Cormier, Benjamin R.

2005-12-01T23:59:59.000Z

129

Refinery analytical techniques optimize unit performance  

Science Conference Proceedings (OSTI)

Refinery process engineers need to consider benefits of laboratory analytical techniques when evaluating unit performance. Refinery heavy-oil laboratory analytical techniques use both old and new technologies. Knowing how to use available laboratory analytical techniques within their limitations are critical to obtain correct refinery optimization decisions. Better refinery stream distillation and contaminant data ultimately improves the accuracy of various refinery decision-making tools. These laboratory analytical techniques are covered: high-temperature simulated distillation (HTSD); true boiling point (TBP) distillation--ASTM D2892; vacuum distillation--ASTM D5236; continuous-flash vaporizers; wiped-film evaporators; inductively coupled plasma atomic-emission spectroscopy (ICP-AES); Conradson--ASTM D189/Microcarbon residue--ASTM D4530; and asphaltene IP-143, ASTM D3279, ASTM D4124. Analysis of atmospheric crude, vacuum crude and delayed coker units highlight these laboratory techniques to identify potential yield and product quality benefits. Physical distillation or wiped-film evaporation in conjunction with HTSD, ICP-AES, microcarbon residue and asphaltened data will better characterize a feedstock as well as determine the source of contaminants. Economics are refinery specific, therefore, these examples focus on applying laboratory techniques as opposed to discussing specifics of unit improvement. These are discussed qualitatively.

Golden, S.W. [Process Consulting Services Inc., Grapevine, TX (United States); Craft, S. [Chempro, Inc., LaPorte, TX (United States); Villalanti, D.C. [Triton Analytics Corp., Houston, TX (United States)

1995-11-01T23:59:59.000Z

130

Complexity index indicates refinery capability, value  

Science Conference Proceedings (OSTI)

Refinery size usually is measured in terms of distillation capacity. Relative size, however, can be measured using refinery complexity--a concept developed by W.L. Nelson in the 1960s. Nelson developed the complexity index to quantify the relative cost of components that make up a refinery. It is a pure cost index that provides a relative measure of the construction costs of a particular refinery based on its crude and upgrading capacity. The Nelson index compares the costs of various upgrading units--such as a fluid catalytic cracking (FCC) unit or a catalytic reformer--to the cost of a crude distillation unit. Computation of the index is an attempt to quantify the relative cost of a refinery based on the added cost of various upgrading units and the relative upgrading capacity. A review of complexity calculations, and an explanation of how indices have changed, provide a simple means of determining the complexity of single refineries or refining regions. The impact of complexity on product slate is also examined in this paper.

Johnston, D. [Daniel Johnston and Co. Inc., Dallas, TX (United States)

1996-03-18T23:59:59.000Z

131

OMB No. 1905-0165 Version No.:xxxx.xx FORM EIA-820 ANNUAL REFINERY ...  

U.S. Energy Information Administration (EIA)

the comparable capacity numbers reported on the Form EIA-810, "Monthly Refinery Report," filed for January 2014. ... ANNUAL REFINERY REPORT.

132

U.S. Exports of Natural Gas Liquids and Liquid Refinery Gases ...  

U.S. Energy Information Administration (EIA)

Natural Gas Plant Liquids and Liquefied Refinery Gases Exports; Natural Gas Plant Liquids and Liquefied Refinery Gases Supply and Disposition;

133

Kyrgyzstan starts up its first refinery  

Science Conference Proceedings (OSTI)

The Central Asian republic of Kyrgyzstan started up its first oil refinery in October 1996. The 10,000 b/d plant is designed to produce gasoline, diesel, and mazut (heavy fuel oil) from local Kyrgyz crude. Before construction of the Jalalabad refinery, all finished petroleum products were imported from neighboring countries. Kyrgyzstan`s demand for finished products is about 40,000 b/d. The new refinery was designed and constructed by Petrofac of Tyler, Texas, on behalf of Kyrgoil Corp., Calgary. Kyrgoil is a partner with the Kyrgyz state oil company, Kyrgyzsneft, in a venture called Kyrzgyz Petroleum Co. (KPC). KPC has undertaken restoration and continued development of the oil fields in Kyrgyzstan`s Fergana basin, in addition to the refinery project. The company also has marketing rights for finished products within Kyrgyzstan. The refinery comprises: a hydroskimming (atmospheric distillation) section, diesel steam stripping, gasoline blending, and utilities and off-sites, including steam generation, power generation, tank farm, truck and rail tank-car loading and unloading facilities, crude inlet pipeline, high-voltage power line, substation, air compression, laboratory, and maintenance facilities.

McLeod, G. [Petrofac LLC, Tyler, TX (United States)

1997-05-05T23:59:59.000Z

134

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

135

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

136

Indiana, Illinois, Kentucky Refinery District Gross Inputs to ...  

U.S. Energy Information Administration (EIA)

Indiana, Illinois, Kentucky Refinery District Gross Inputs to Refineries (Thousand Barrels per Day) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1985: 1,739 ...

137

Texas City Refinery Update: The Price of Safety Complacency  

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

Texas City Refinery Update: The Price of Safety Complacency DOEEH-0699 2006-01 January 2006 ES&H Safety Bulletin 2005-09 (July 2005) discussed the Texas City Refinery accident in...

138

Improved oil refinery operations and cheaper crude oil to help...  

Annual Energy Outlook 2012 (EIA)

Improved oil refinery operations and cheaper crude oil to help reduce gasoline prices U.S. gasoline prices are expected to fall as more oil refineries come back on line and crude...

139

Flare Gas Recovery in Shell Canada Refineries  

E-Print Network (OSTI)

Two of Shell Canada's refineries have logged about six years total operating experience with modern flare gas recovery facilities. The flare gas recovery systems were designed to recover the normal continuous flare gas flow for use in the refinery fuel gas system. The system consists of liquid knock-out, compression, and liquid seal facilities. Now that the debugging-stage challenges have been dealt with, Shell Canada is more than satisfied with the system performance. A well-thought-out installation can today be safe, trouble-free, and attractive from an economic and environmental viewpoint. This paper highlights general guidelines for the sizing, design and operation of a refinery flare gas recovery facility.

Allen, G. D.; Wey, R. E.; Chan, H. H.

1983-01-01T23:59:59.000Z

140

How refinery fuel indexes have varied  

Science Conference Proceedings (OSTI)

Refinery fuels costs have endured a steady incline since 1993, except for a period in 1993. As shown in the accompanying table, these increases in cost have occurred for residual fuel oil costs in three of the five PADD districts. The cost for natural gas for refinery usage also dropped steadily during the 3-year study. These conclusions are based on costs of an average refinery fuel consisting of 1 bbl each of PADD Districts 1--5 and an average US cost of 4.4 MMscf natural gas (a 1 bbl equivalent on a BTU content basis). Raw residual fuel oil and natural gas prices come from publications put out by the US Department of Labor.

Farrar, G.

1997-01-06T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

U.S. Refinery Thermal Cracking, Visbreaking Downstream Charge ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Thermal Cracking, Visbreaking Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

142

Guam Refinery Thermal Cracking/Visbreaking Downstream Charge ...  

U.S. Energy Information Administration (EIA)

Guam Refinery Thermal Cracking/Visbreaking Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

143

Guam Refinery Thermal Cracking/Other (including Gas Oil ...  

U.S. Energy Information Administration (EIA)

Guam Refinery Thermal Cracking/Other (including Gas Oil) Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

144

U.S. Refinery Thermal Cracking, Fluid Coking Downstream Charge ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Thermal Cracking, Fluid Coking Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

145

Market Assessment of Refinery Outages Planned for October 2009 ...  

U.S. Energy Information Administration (EIA)

January fuel demand with availability of the refinery process units for distillate and gasoline production net of outages.

146

Virgin Islands Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

147

Midwest (PADD 2) Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

148

Puerto Rico Number and Capacity of Petroleum Refineries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Idle refineries ...

149

Refineries are also indirectly exposed to forced processing rate ...  

U.S. Energy Information Administration (EIA)

Refineries receive crude oil from two sources: waterborne deliveries by ship and domestic production from California crude oil producing fields.

150

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

U.S. Energy Information Administration (EIA)

receipt of crude oil at idled refineries require considerable modification before they can be used to receive products. Moreover, ...

151

Michigan Refinery Catalytic Hydrotreating, Kerosene/Jet Fuel ...  

U.S. Energy Information Administration (EIA)

Cat. Hydro.. Kerosene/Jet Fuel Downstream Charge Capacity (B/SD) Michigan Downstream Charge Capacity of Operable Petroleum Refineries ...

152

Colorado Refinery Catalytic Hydrotreating, Other/Residual Fuel Oil ...  

U.S. Energy Information Administration (EIA)

Colorado Refinery Catalytic Hydrotreating, Other/Residual Fuel Oil Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

153

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

154

Puerto Rico Refinery Thermal Cracking/Visbreaking Downstream ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Thermal Cracking/Visbreaking Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

155

Puerto Rico Refinery Catalytic Hydrotreating, Kerosene/Jet Fuel ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Catalytic Hydrotreating, Kerosene/Jet Fuel Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

156

Puerto Rico Refinery Catalytic Hydrocracking, Gas Oil Downstream ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Catalytic Hydrocracking, Gas Oil Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

157

Refining District Oklahoma-Kansas-Missouri Refinery and ...  

U.S. Energy Information Administration (EIA)

Refining District Oklahoma-Kansas-Missouri Refinery and Blender Net Input of Fuel Ethanol (Thousand Barrels per Day)

158

New Jersey Refinery Catalytic Reforming/High Pressure Downstream ...  

U.S. Energy Information Administration (EIA)

New Jersey Refinery Catalytic Reforming/High Pressure Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

159

Arkansas Refinery Catalytic Reforming/High Pressure Downstream ...  

U.S. Energy Information Administration (EIA)

Arkansas Refinery Catalytic Reforming/High Pressure Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

160

U.S. Refinery Catalytic Hydrotreating, Heavy Gas Oil ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Catalytic Hydrotreating, Heavy Gas Oil Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

Note: This page contains sample records for the topic "refinery bulk terminal" 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

East Coast (PADD 1) Refinery Operable Atmospheric Crude Oil ...  

U.S. Energy Information Administration (EIA)

East Coast (PADD 1) Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

162

East Coast (PADD 1) Refinery Vacuum Distillation Downstream Charge ...  

U.S. Energy Information Administration (EIA)

East Coast (PADD 1) Refinery Vacuum Distillation Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

163

West Coast (PADD 5) Refinery Operable Atmospheric Crude Oil ...  

U.S. Energy Information Administration (EIA)

West Coast (PADD 5) Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

164

Puerto Rico Refinery Operable Atmospheric Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

Puerto Rico Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

165

Rocky Mountain (PADD 4) Refinery Operable Atmospheric Crude Oil ...  

U.S. Energy Information Administration (EIA)

Rocky Mountain (PADD 4) Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

166

Gulf Coast (PADD 3) Refinery Operable Atmospheric Crude Oil ...  

U.S. Energy Information Administration (EIA)

Gulf Coast (PADD 3) Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

167

U.S. Refinery Operating Atmospheric Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Operating Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

168

U.S. Refinery Operable Atmospheric Crude Oil Distillation Capacity ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Calendar Day)

169

U.S. Refinery Operable Atmospheric Crude Oil Distillation Capacity ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Operable Atmospheric Crude Oil Distillation Capacity as of January 1 (Barrels per Stream Day)

170

U.S. Refinery Marketable Petroleum Coke Production Capacity as ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Marketable Petroleum Coke Production Capacity as of January 1 (Barrels per Stream Day)

171

Structural, energy and environmental aspects in Iranian oil refineries  

Science Conference Proceedings (OSTI)

Petroleum refineries extract and upgrade the valuable components of crude oil to produce a variety of marketable petroleum products. However Iranian refineries are old and their efficiency and structure do not satisfy demand of the country in which their ... Keywords: Iran, demand, energy, refinery

Sourena Sattari; Akram Avami

2008-02-01T23:59:59.000Z

172

Exxon reduces production at U. S. refineries  

SciTech Connect

This paper reports that Exxon Co. U.S.A. has trimmed output of its U.S. refineries by a combined 15% because of depressed margins on products markets. The company made the announcement last week as it began increasing crude runs at its 396,000 b/cd refinery at Baytown, Tex., on the Houston Ship Channel. Exxon trimmed Baytown crude runs late last month to manage feedstock inventories after a barge was rammed and sunk in the ship channel, briefly halting traffic. Most feedstock is delivered to the Baytown plant by water.

Not Available

1993-01-11T23:59:59.000Z

173

Monitoring and Management of Refinery Energy Consumption  

E-Print Network (OSTI)

Since 1972, the U.S. refining industry has made much progress in reducing energy consumption. Lately, falling energy prices have de-emphasized the need to appropriate new capital for additional energy conservation projects. One area neglected in most refineries is the need to monitor and manage the daily use of energy. Setting up an energy auditing system will tell management how well each unit in the refinery is being operated and can be used as a valuable tool in reducing energy costs. An example of an energy monitorirg and management system is discussed and illustrated with examples.

Pelham, R. O.; Moriarty, R. D.; Hudgens, P. D.

1986-06-01T23:59:59.000Z

174

U.S. Refinery Net Production  

U.S. Energy Information Administration (EIA)

Liquefied Refinery Gases: 11,903: 12,936: 13,591: 20,226: 24,599: 26,928: 2005-2013: ... Asphalt and Road Oil: 10,230: 9,328: 8,595: 9,973: 9,494: 9,914: 2005-2013 ...

175

Refinery siting workbook: appendices C to O  

Science Conference Proceedings (OSTI)

Applicable laws and permits available for the selection and building of petroleum refineries are enclosed. A glossary of pertinent terms is also included. References related to the National Environmental Policy Act, the Clean Air Act, the Federal Water Pollution Control Act, Resource Conservation and Recovery Act, Toxic Substance Control Act, and Wetlands and Coastal Zone are included. Permit information is also presented. (DC)

Not Available

1980-07-01T23:59:59.000Z

176

Refinery Investments and Future Market Incentives  

Reports and Publications (EIA)

Presentation given at the Annual NPRA Meeting that discusses factors affecting refinery investments. Refiners have plunged from a seeming "golden age" investment environment to a world with excess capacity, flat to declining demand, and weak margins. What is happening to refining investments in this turbulent and uncertain situation?

Information Center

2009-03-25T23:59:59.000Z

177

Firing Excess Refinery Butane in Peaking Gas Turbines  

E-Print Network (OSTI)

New environmentally-driven regulations for motor gasoline volatility will significantly alter refinery light ends supply/demand balancing. This, in turn, will impact refinery economics. This paper presumes that one outcome will be excess refinery normal butane production, which will reduce refinery normal butane value and price. Explored is an opportunity for a new use for excess refinery normal butane- as a fuel for utility peaking gas turbines which currently fire kerosene and #2 oil. Our paper identifies the fundamental driving forces which are changing refinery butane economics, examines how these forces influence refinery production, and evaluates the potential for using normal butanes as peaking utility gas turbine fuel, especially on the US East Coast.

Pavone, A.; Schreiber, H.; Zwillenberg, M.

1989-09-01T23:59:59.000Z

178

Opportunities for Biorenewables in Oil Refineries  

Science Conference Proceedings (OSTI)

Abstract: The purpose of this study was to evaluate the potential for using biorenewable feedstocks in oil refineries. Economic analyses were conducted, with support from process modeling and proof of principle experiments, to assess a variety of potential processes and configurations. The study considered two primary alternatives: the production of biodiesel and green diesel from vegetable oils and greases and opportunities for utilization of pyrolysis oil. The study identified a number of promising opportunities for biorenewables in existing or new refining operations.

Marker, T.L.

2005-12-19T23:59:59.000Z

179

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.

180

GreenHunter Biodiesel Refinery Grand Opening | Department of Energy  

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

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

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Economic impact analysis for the petroleum refineries NESHAP. Final report  

Science Conference Proceedings (OSTI)

An economic analysis of the industries affected by the Petroleum Refineries National Emmissions Standard for Hazardous Air Pollutants (NESHAP) was completed in support of this standard. The industry for which economic impacts was computed was the petroleum refinery industry. Affected refineries must reduce HAP emissions by the level of control required in the standard. Several types of economic impacts, among them price product changes, output changes, job impacts, and effects on foriegn trade, were computed for the selected regulatory alternative.

NONE

1995-08-01T23:59:59.000Z

182

U.S. Refinery Thermal Cracking, Other (including Gas Oil ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Thermal Cracking, Other (including Gas Oil) Downstream Charge Capacity as of January 1 (Barrels per Stream Day)

183

Summary of Market Assessment of Planned Refinery Outages  

U.S. Energy Information Administration (EIA)

Home > Petroleum > Analysis > Summary of Market Assessment of Planned Refinery ... As required under Section 804 of the Energy Independence and Security Act of 2007 ...

184

U.S. refineries and blenders produced record amounts of ...  

U.S. Energy Information Administration (EIA)

Because of its chemical composition, crude oil run through a refinery typically yields roughly twice as much motor gasoline as distillate fuels.

185

Directory of Operable Petroleum Refineries on Tables 38 and 39  

U.S. Energy Information Administration (EIA)

Directory of Operable Petroleum Refineries on Tables 38 and 39 Refiner State(s)aRefiner State(s)a.....Age Refining Inc ...

186

Environmentally advanced refinery nears start-up in Germany  

SciTech Connect

Mitteldeutsche Erdoel-Raffinerie GmbH (Mider), is building a 170,000 b/d, grassroots refinery in Leuna, Germany. The refinery is scheduled to start up in third quarter of this year. At the heart of the new refinery is a new technology called progressive distillation. Other major units include: vacuum distillation, catalytic reforming, alkylation, visbreaking, fluid catalytic cracking (FCC), and hydrodesulfurization (HDS). In addition, an existing partial oxidation (POX)/methanol production unit will be integrated with the new refinery. The paper describes the plant and its major processes.

Rhodes, A.K.

1997-03-17T23:59:59.000Z

187

Energy efficiency improvement and cost saving opportunities for petroleum refineries  

E-Print Network (OSTI)

are also listed. The Energy Guide draws upon the experiencesmanagement programs. This Energy Guide describes researchpetroleum refineries. This Energy Guide introduces energy

Worrell, Ernst; Galitsky, Christina

2005-01-01T23:59:59.000Z

188

EIA Energy Kids - Carson Refinery - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Hydrogen. Recent Statistics ... and then distributed to gas stations all over Los Angeles and Southern ... you are probably filling up with gas from the Carson refinery.

189

U.S. Refinery Operable Capacity is Updated  

U.S. Energy Information Administration (EIA)

Released: March 28, 2012 Notice: Reported refinery operable capacity data shown in the Weekly Petroleum Status Report (WPSR) for the week-ended March 23, 2012, has ...

190

U.S. Refinery Catalytic Hydrotreating, Kerosene/Jet Fuel ...  

U.S. Energy Information Administration (EIA)

Cat. Hydro.. Kerosene/Jet Fuel Downstream Charge Capacity (B/SD) U.S. Downstream Charge Capacity of Operable Petroleum Refineries ...

191

Market Assessment of Refinery Outages Planned for March 2010 ...  

U.S. Energy Information Administration (EIA)

DOE/EIA-0641(2010)/1 Market Assessment of Refinery Outages Planned for March 2010 through June 2010 March 2010 Energy Information Administration

192

When was the last refinery built in the United States? - FAQ ...  

U.S. Energy Information Administration (EIA)

When was the last refinery built in the United States? There were a total of 143 operable petroleum refineries in the United States as of January 1, 2013.

193

Bulk Metallic Glasses XI  

Science Conference Proceedings (OSTI)

Jul 15, 2013 ... A Bulk Metallic Glass with Record-breaking Damage Tolerance ... Oxidation on the Surface Characteristics of Zr-based Bulk Metallic Glasses.

194

Poland petroleum refinery sludge lagoon demonstration project  

SciTech Connect

The US Department of Energy and the Institute for Ecology of Industrial Area have been working together to develop mutually beneficial, cost-effective environmental remediation technologies such as the demonstration of bioremediation techniques for the clean up of acidic petroleum sludge impacted soils at an oil refinery in southern Poland. After an expedited site characterization, treatability study, and a risk assessment study, a remediation strategy was devised. The waste material was composed primarily of high molecular weight paraffinic and polynuclear aromatic hydrocarbons. A biopile design which employed a combination of passive and active aeration in conjunction with nutrient and surfactant application as used to increase the biodegradation of the contaminants of concern.

Altman, D.J.

2000-05-05T23:59:59.000Z

195

Upgrade Your Refinery for Energy Conservation  

E-Print Network (OSTI)

Upgrading existing refineries for efficient energy utilization imposes strict restraints upon design engineers. Present and future production requirements must be defined. Reliable operating data must be obtained from historical records and test runs to accurately define actual performance of each piece of equipment. A complete simulation model of the facility is developed and tested. Future operations are evaluated using the model to define heat and material balance requirements for all projected operations. Energy conservation projects are evaluated with the model to define energy savings over the life of each project. A discounted cash flow analysis is formulated and an optimum set of projects yielding maximum rates of return are selected for implementation.

Johnnie, D. H., Jr.; Klooster, H. J.

1983-01-01T23:59:59.000Z

196

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.

197

Flare-gas recovery success at Canadian refineries  

SciTech Connect

It appears that some North American refining companies still cling to an old philosophy that flare gas recovery systems are unsafe, unreliable, uneconomic, or unnecessary. Shell Canada's recent experience with two modern systems has proven otherwise. Two of Shell Canada's refineries, at Sarnia, Ont., and Montreal East, Que., have now logged about 6 years' total operating experience with modern flare gas recovery units. The compression facilities in each utilize a two-stage reciprocating machine, one liquid seal drum per flare stack, and an automated load control strategy. The purpose was to recover the normal continuous flow of refinery flare gas for treatment and use in the refinery fuel gas system.

Allen, G.D.; Chan, H.H.; Wey, R.E.

1983-06-01T23:59:59.000Z

198

Master development plan for the Cartagena Refinery. Export trade information  

Science Conference Proceedings (OSTI)

This study, conducted by the M.W. Kellogg Company, was funded by the U.S. Trade and Development Agency on behalf of ECOPETROL, Colombia`s national oil company. The objective of the study was to investigate technical, economic, and environmental issues that challenge the Cartagena Refinery. The study also recommends the most attractive options for the refinery to improve profitability. The document is divided into the following sections: (1) Executive Summary; (2) Market Survey; (3) Refinery Configuration; (4) Economic Evaluation; (5) Other Technical/Strategic Considerations; (6) Appendix.

NONE

1996-09-01T23:59:59.000Z

199

Application of Pinch Technology in Refinery Retrofits  

E-Print Network (OSTI)

This paper reviews the application of pinch technology in the identification of the most attractive retrofit prospects in typical refineries. In the first part of the paper, methodology is described to identify attractive inter-unit heat integration opportunities as well as attractive process-utility system integration (co-generation). An example of an atmospheric pipestill-alkylation unit integration evaluation is given using both composite stream and Grand composite stream methods. In the second part of the paper, the application of pinch technology in a typical intra-unit heat integration problem is given. It is explained how inefficiencies in an APS crude preheat train are identified, and a typical small retrofit project is described.

Thomas, W. R.; Siegell, J. H.; Sideropoulos, T.; Robertson, J. L.; Papoulias, S. A.

1987-09-01T23:59:59.000Z

200

Bulk Metallic Glasses X  

Science Conference Proceedings (OSTI)

Jul 31, 2012 ... Aerospace and Spacecraft Applications for Bulk Metallic Glasses and Matrix Composites · Air Oxidation of a Binary Cu64.5Zr35.5 Bulk Metallic ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Motiva Enterprises Refinery Expansion Groundbreaking | Department of Energy  

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

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

202

Secretary Bodman Tours Refinery and Calls for More Domestic Refining  

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

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

203

U.S. Percent Utilization of Refinery Operable Capacity (Percent)  

U.S. Energy Information Administration (EIA)

Annual : Download Data (XLS File) U.S. Percent Utilization of Refinery Operable Capacity (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1985: 74.0 ...

204

Rocky Mountain (PADD 4) Refinery and Blender Net Production of ...  

U.S. Energy Information Administration (EIA)

Rocky Mountain (PADD 4) Refinery and Blender Net Production of Normal Butane (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8

205

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

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

,,"(202) 586-8800",,,"7242013 11:46:42 PM" "Back to Contents","Data 1: U.S. Refinery Crude Oil Input Qualities" "Sourcekey","MCRS1US2","MCRAPUS2" "Date","U.S. Sulfur...

206

Coal Use in Petroleum Refineries -- Opportunities and Issues  

Science Conference Proceedings (OSTI)

This report is a brief review of the technologies and key issues involved in considering the use of coal as a replacement, supplemental, or additional fuel in petroleum refineries.

2002-10-21T23:59:59.000Z

207

World Energy Projection System Plus Model Documentation: Refinery Model  

Reports and Publications (EIA)

This report documents the objectives, analytical approach and development of the World Energy Projection System Plus (WEPS+) Refinery Model. It also catalogues and describes critical assumptions, computational methodology, parameter estimation techniques, and model source code.

Adrian Geagla

2011-10-04T23:59:59.000Z

208

Rocky Mountain (PADD 4) Foreign Crude Oil Refinery Receipts by ...  

U.S. Energy Information Administration (EIA)

Rocky Mountain (PADD 4) Foreign Crude Oil Refinery Receipts by Tank Cars (Rail) (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8

209

U.S. Petroleum Coke Consumed at Refineries (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Petroleum Coke Consumed at Refineries (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's: ...

210

U.S. Petroleum Coke Stocks at Refineries (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Petroleum Coke Stocks at Refineries (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: 10,747: 11,072: 11,444: ...

211

Rotary bulk solids divider  

DOE Patents (OSTI)

An apparatus for the disbursement of a bulk solid sample comprising, a gravity hopper having a top open end and a bottom discharge end, a feeder positioned beneath the gravity hopper so as to receive a bulk solid sample flowing from the bottom discharge end, and a conveyor receiving the bulk solid sample from the feeder and rotating on an axis that allows the bulk solid sample to disperse the sample to a collection station.

Maronde, Carl P. (McMurray, PA); Killmeyer, Jr., Richard P. (Pittsburgh, PA)

1992-01-01T23:59:59.000Z

212

Flexible hydrogen plant utilizing multiple refinery hydrocarbon streams  

Science Conference Proceedings (OSTI)

Numerous processes are available to produce hydrogen, however, steam reforming is still the dominant and currently preferred process because it can economically process a variety of refinery feedstocks into hydrogen. This paper discusses the Air Products 88 MMSCFD hydrogen plant built by KTI, adjacent to Shell`s Martinez refinery, which utilizes up to eight separate refinery hydrocarbon streams as feed and fuel for the production of hydrogen in the steam reforming unit. The integration of refinery hydrocarbon purge streams, normally sent to fuel, allows greater flexibility in refinery operations and increases the overall refinery fuel efficiencies. The hydrogen plant also incorporates a number of process control design features to enhance reliability, such as two out of three voting systems, in-line sparing, and reduced bed PSA operation. The final section of the paper describes the environmental features of the plant required for operation in the Bay Area Air Quality Management District (BAAQMD). Air Products and KTI designed BACT features into the hydrogen plant to minimize emissions from the facility.

Kramer, K.A.; Patel, N.M. [Air Products and Chemicals Inc., Allentown, PA (United States); Sekhri, S. [Kinetics Technology International Corp., San Dimas, CA (United States); Brown, M.G. [Shell Oil Products Co., Martinez, CA (United States)

1996-12-01T23:59:59.000Z

213

Engineering firm has designed refinery of the future  

SciTech Connect

Four years ago, JGC Corp. organized a project team called ``Refinery Engineering for the Future in the Twenty-First Century,`` or REF-21. The purpose of the team was to forecast the environment facing the refining industry in Japan, long-range energy supply and demand, population and economic growth, traffic system trends, and technology and science progress through the middle of the twenty-first century. The REF-21 team also was charged with developing a conceptual design for the future refinery. The team proposed four types of configurations for the so-called new-generation refineries. These schemes included some new technologies that it deemed commercializable by 2000. JGC evaluated these new-generation refinery schemes in terms of overall yields, energy efficiencies, emissions, and economics, as compared with existing refineries. JGC also has developed an amenity design program (ADP), and is applying it to a refinery in Japan to produce a new-concept operation center. Through amenity design, JGC intends to improve the operating environment for employees in order to enhance overall productivity.

Inomata, Makoto; Sato, Kyohei; Yamada, Yu; Sasaki, Hajime [JGC Corp., Yokohama (Japan)

1997-04-28T23:59:59.000Z

214

Bulk Hydrogen Storage - Strategic Directions for Hydrogen Delivery Workshop  

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

Hydrogen Hydrogen Storage Strategic Directions for Hydrogen Delivery Workshop May 7-8, 2003 Crystal City, Virginia Breakout Session - Bulk Hydrogen Storage Main Themes/Caveats Bulk Storage = Anything not on the vehicle 10's of Tons -- End use point 50-100 Tons - Terminals/City Gates 1000's Tons - Between Production Facility and Terminal/City Gate Bulk storage requirements less restrictive and different from on-board storage Uncertainty about evolution of infrastructure requires multiple pathways to be considered Bulk storage is an economic solution to address supply/demand imbalance Breakout Session - Bulk Hydrogen Storage Targets/Objectives Hard to quantify - scenario & end-use dependent Storage Materials (solid state) and container require different targets

215

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

216

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

217

U.S. Kerosene Stocks at Bulk Terminals (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

1,954: 1,760: 1,941: 2,174: 2,631: 2,627: 2,637: 2,157: 2010: 2,651: 2,126: 1,992: 2,006: 2,003: 2,170: 2,092: 2,106: 2,494: 2,762: 2,220: 1,733: ...

218

Isobutane/Butylene Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

219

EIA-805 WEEKLY BULK TERMINAL AND BLENDER REPORT INSTRUCTIONS  

U.S. Energy Information Administration (EIA)

component of the Department of Energy (DOE); ... violations which may result in a temporary restraining order or a preliminary or permanent injunction without bond.

220

Conventional Gasoline Blended Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Residual Fuel Oil Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

Stock Type: Download Series History: Definitions, Sources & Notes: Show Data By: Product: Stock Type: Area: Jan-13 Feb-13 Mar-13 Apr-13 May-13 Jun-13 View History; U ...

222

Asphalt and Road Oil Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

223

Crude Oil and Petroleum Products Bulk Terminal Stocks by Type  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Crude oil stocks in the ...

224

Environmental Regulation and Productivity: Evidence from Oil Refineries  

E-Print Network (OSTI)

Abstract: We examine the effect of air quality regulation on the productivity of some of the most heavily regulated manufacturing plants in the United States, the oil refineries of the Los Angeles (South Coast) Air Basin. We use direct measures of local air pollution regulation in this region to estimate their effects on abatement investment. Refineries not subject to these local environmental regulations are used as a comparison group. We study the period of increased regulation between 1979 and 1992. On average, each regulation cost $3M per plant on compliance dates and a further $5M per plant on dates of increased stringency. We also construct measures of total factor productivity using plant level data which allow us to observe physical quantities of inputs and outputs for the entire population of refineries. Despite the high costs associated with the local regulations, productivity in the Los Angeles Air Basin refineries rose sharply during the 1987-92 period, a period of decreased refinery productivity in other regions. We conclude that measures of the cost of environmental regulation may be significantly overstated. The gross costs may be far greater than the net cost, as abatement may be productive.

Eli Berman; Linda T. M. Bui

1998-01-01T23:59:59.000Z

225

Assessment of coal liquids as refinery feedstocks  

Science Conference Proceedings (OSTI)

The R D of direct coal liquefaction has reached such a stage that current two-stage processes can produce coal liquids with high yields and improved quality at a reasonable cost. To fully realize the potential value, these coal liquids should be refined into high-value liquid transportation fuels. The purpose of this study is to assess coal liquids as feedstocks to be processed by modern petroleum refining technologies. After the introduction, Section 2.0 summarizes ASTM specifications for major transportation fuels: gasoline, jet fuel, and diesel fuel, which serve as a target for coal-liquid refining. A concise description of modern refining processes follows with an emphasis on the requirements for the raw materials. These provide criteria to judge the quality of coal liquids as a refinery feedstock for the production of marketable liquid fuels. Section 3.0 surveys the properties of coal liquids produced by various liquefaction processes. Compared with typical petroleum oils, the current two-stage coal liquids are: Light in boiling range and free of resids and metals; very low in sulfur but relatively high in oxygen; relatively low in hydrogen and high in cyclics content; and essentially toxicologically inactive when end point is lower than 650[degrees]F, particularly after hydroprocessing. Despite these characteristics, the coal liquids are basically similar to petroleum. The modern refining technology is capable of processing coal liquids into transportation fuels meeting all specifications, and hydroprocessinq is obviously the major tool. The important point is the determination of a reasonable product slate and an appropriate refining scheme.

Zhou, P.

1992-02-01T23:59:59.000Z

226

Assessment of coal liquids as refinery feedstocks  

Science Conference Proceedings (OSTI)

The R&D of direct coal liquefaction has reached such a stage that current two-stage processes can produce coal liquids with high yields and improved quality at a reasonable cost. To fully realize the potential value, these coal liquids should be refined into high-value liquid transportation fuels. The purpose of this study is to assess coal liquids as feedstocks to be processed by modern petroleum refining technologies. After the introduction, Section 2.0 summarizes ASTM specifications for major transportation fuels: gasoline, jet fuel, and diesel fuel, which serve as a target for coal-liquid refining. A concise description of modern refining processes follows with an emphasis on the requirements for the raw materials. These provide criteria to judge the quality of coal liquids as a refinery feedstock for the production of marketable liquid fuels. Section 3.0 surveys the properties of coal liquids produced by various liquefaction processes. Compared with typical petroleum oils, the current two-stage coal liquids are: Light in boiling range and free of resids and metals; very low in sulfur but relatively high in oxygen; relatively low in hydrogen and high in cyclics content; and essentially toxicologically inactive when end point is lower than 650{degrees}F, particularly after hydroprocessing. Despite these characteristics, the coal liquids are basically similar to petroleum. The modern refining technology is capable of processing coal liquids into transportation fuels meeting all specifications, and hydroprocessinq is obviously the major tool. The important point is the determination of a reasonable product slate and an appropriate refining scheme.

Zhou, P.

1992-02-01T23:59:59.000Z

227

2013 Short Course Analytical Techniques: Quality Control, Process Control, and Refinery Optimization  

Science Conference Proceedings (OSTI)

Analytical Techniques: Quality Control, Process Control, and Refinery Optimization held at the 104th AOCS Annual Meeting and Expo. 2013 Short Course Analytical Techniques: Quality Control, Process Control, and Refinery Optimization Analytical Techn

228

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

229

Alternative multimedia regulatory programs for next-generation refineries  

Science Conference Proceedings (OSTI)

The 25-year-old command-and-control environmental regulatory structure in the US has resulted in significant environmental improvements. Recently, however, its limitations (e.g., rigid application regardless of site-specific conditions, disregard of cross-media and multimedia impacts, limited incentives for new technology development and use) have become increasingly apparent. New regulatory approaches that recognize current and anticipated economic constraints, new knowledge of environmental processes and impacts, and the benefits of new technologies are needed. Such approaches could be especially important for the US petroleum refining industry. This industry operates under thin profit margins, releases chemicals that can produce adverse health and environmental impacts, and must meet the technological challenges of producing more highly refined fuels from poorer quality feedstocks. Under a grant from the Environmental Technology Initiative (ETI), Argonne National Laboratory and its subcontractor, Analytical Services, Inc. developed two alternative environmental regulatory programs for next-generation petroleum refineries. (In this report, next-generation refineries refers to the refineries of today as they operate in the next 20 or more years rather than to fully reengineered future refineries.) The objective of the ETI refinery project was to develop future-oriented regulatory programs for next-generation refineries that will expand the use of innovative technologies, encourage pollution prevention, demonstrate environmental responsibility, and maintain refinery economic performance. Rather than suggesting targeted, short-term modifications to existing media-specific command-and-control regulations, the ETI project suggests the use of new approaches that are broader and more flexible. It recognizes that giving refineries flexibility in meeting environmental protection goals can stimulate new technology development and use. Unlike most US Environmental Protection Agency (EPA) reinvention efforts, which seek results in 12 to 18 months, this ETI effort assumes a time frame of 20 years or more. It also assumes that existing laws and regulations can be changed. An iterative and interactive process was used by the project team to develop the alternative approaches. Information and stakeholder input were integrated to provide for constant revision and improvement. First, guidelines and principles were established to bound the study and set parameters for developing the approaches. Next, existing and projected environmental laws and regulations affecting petroleum refineries were examined to identify areas needing change. Then, to understand future challenges and opportunities, the projected refinery operating environment was described in terms of feedstock, product, technology, and economics. Finally several goals and indicators for assessing and comparing the alternatives were identified. On the basis of this background information, more than 60 options that could efficiently and effectively protect human health and the environment were identified. These options ranged from fundamental changes in program philosophy to procedural improvements. After the options were evaluated against the goals and indicators, many of them were integrated into two separate thematic paradigms: a risk-based paradigm and a goal-based paradigm. Elements common to both approaches include the following: (1) Establish the baseline--In establishing the baseline, the refinery and the regulator jointly identify residuals for which release limits must be established; (2) Set residual release limits--The refinery and the regulator jointly specify release limits on a facility-wide rather than a source-specific basis. A facility-wide permit documents the release limits; and (3) Assure compliance--Incentives provide the basis for assuring compliance, and flexibility in the compliance method is encouraged. Penalties apply if releases exceed the limits, and reporting requirements are streamlined relative to current practices.

Elcock, D.; Gasper, J.; Arguerro, R.; Emerson, D.

2000-06-22T23:59:59.000Z

230

Mazheikiai refinery modernization study. Executive summary. Export trade information  

Science Conference Proceedings (OSTI)

The study, conducted by Foster Wheeler Corporation, was funded by the U.S. Trade and Development Agency on behalf of Lithuania's Ministry of Energy. The Mazheikiai Oil Refinery is the only one in the Baltic Region and serves the needs of Lithuania, Latvia, Estonia, and Kaliningrad. Before Lithuania's independence in 1990, the refinery was assured of crude supplies from Russia. However, since then the need has arisen to secure alternate sources of crude oil and the ability to process them. The purpose of the report is to provide recommendations to the Ministry of Energy for process improvements, environmental control measures, physical rehabilitation and energy conservation plans for the Mazheikiai Oil Refinery. The volume contains the Executive Summary.

Not Available

1994-01-01T23:59:59.000Z

231

Monitoring near refineries or airborne chemicals on the SARA Title 3 section 313 list  

Science Conference Proceedings (OSTI)

In this volume, detailed procedures recommended for the measurement of selected petroleum refinery emissions in ambient air are presented.

Not Available

1988-01-01T23:59:59.000Z

232

Monitoring near refineries for airborne chemicals on the SARA Title 3 Section 313 list  

SciTech Connect

This study provides an ambient air concentration perspective to the engineering estimates of petroleum refinery emissions required under SARA Title III Section 313. It presents and discusses ambient air concentrations of 25 selected target chemicals measured at and near the perimeter (fenceline) of three refineries. Measurements were made over three consecutive 24-hour sampling periods at each refinery. The extent to which the concentrations of the target chemicals were due to fugitive emissions from the refineries is estimated.

Not Available

1989-01-01T23:59:59.000Z

233

Monitoring near refineries or airborne chemicals on the SARA Title 3 Section 313 list  

Science Conference Proceedings (OSTI)

This volume identifies publications and databases that address ambient air concentrations measured near petroleum refineries for the selected target chemicals.

Not Available

1988-01-01T23:59:59.000Z

234

Lyondell, Citgo join for heavy oil upgrade project at Houston refinery  

Science Conference Proceedings (OSTI)

Lyondell-Citgo Refining Co. Ltd. is beginning an $800-million upgrade and expansion of its Houston refinery. The project will enable the refinery. The project will enable the refinery to produce clean fuels while processing about 80% heavy, high-sulfur Venezuelan crude oil. The paper describes the Houston refinery, the expansion project, the technologies to be used, operational changes, environmental impacts, and construction.

Rhodes, A.K.

1994-03-21T23:59:59.000Z

235

Distillate yields at U.S. refineries are rising - Today in ...  

U.S. Energy Information Administration (EIA)

Refinery processing gain results from some refining processes, such as fluid catalytic cracking and hydrocracking, where volumes can increase when ...

236

Fuzzy possibilistic modeling and sensitivity analysis for optimal fuel gas scheduling in refinery  

Science Conference Proceedings (OSTI)

In refinery, fuel gas which is continuously generated during the production process is one of the most important energy sources. Optimal scheduling of fuel gas system helps the refinery to achieve energy cost reduction and cleaner production. However, ... Keywords: Fuel gas, Fuzzy possibilistic programming, Marginal value analysis, Refinery, Scheduling, Sensitivity analysis

J. D. Zhang; G. Rong

2010-04-01T23:59:59.000Z

237

Hanford ETR Bulk Vitrification System - Demonstration Bulk Vitrification  

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

Bulk Vitrification System - Demonstration Bulk Bulk Vitrification System - Demonstration Bulk Vitrification System (DBVS) Review Report Hanford ETR Bulk Vitrification System - Demonstration Bulk Vitrification System (DBVS) Review Report Full Document and Summary Versions are available for download Hanford ETR Bulk Vitrification System - Demonstration Bulk Vitrification System (DBVS) Review Report Summary - Demonstration Bulk Vitrification System (DBVS) for Low-Actvity Waste at Hanford More Documents & Publications Independent Oversight Activity Report, Hanford Waste Treatment and Immobilization Plant - November 2013 SRS Tank 48H Waste Treatment Project Technology Readiness Assessment External Technical Review for Evaluation of System Level Modeling and Simulation Tools in Support of Hanford Site Liquid Waste Process

238

Utah Distillate Fuel Oil, Greater than 15 to 500 ppm Sulfur Stocks ...  

U.S. Energy Information Administration (EIA)

Utah Distillate Fuel Oil, Greater than 15 to 500 ppm Sulfur Stocks at Refineries, Bulk Terminals, and Natural Gas Plants (Thousand Barrels)

239

Accuracy of Petroleum Supply Data - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

The greater length of time allows more in-depth review of the data by the respondents and EIA. ... fuel oil from refineries, bulk terminals, and pipel ...

240

Large area bulk superconductors  

DOE Patents (OSTI)

A bulk superconductor having a thickness of not less than about 100 microns is carried by a polycrystalline textured substrate having misorientation angles at the surface thereof not greater than about 15.degree.; the bulk superconductor may have a thickness of not less than about 100 microns and a surface area of not less than about 50 cm.sup.2. The textured substrate may have a thickness not less than about 10 microns and misorientation angles at the surface thereof not greater than about 15.degree.. Also disclosed is a process of manufacturing the bulk superconductor and the polycrystalline biaxially textured substrate material.

Miller, Dean J. (Darien, IL); Field, Michael B. (Jersey City, NJ)

2002-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Universal battery terminal connector  

SciTech Connect

This patent describes a universal battery terminal connector for connecting either a top post battery terminal or a side post battery terminal to a battery cable. The connector comprises an elongated electrically conductive body having: (a) first means for connection to a top post battery terminal; (b) second means for connection to a side post battery terminal, and (c) third means for receiving one end of a battery cable and providing an electrical connection therewith.

Norris, R.W.

1987-01-13T23:59:59.000Z

242

Bulk Metallic Glasses VII  

Science Conference Proceedings (OSTI)

Sponsorship, The Minerals, Metals and Materials Society ... Air-Oxidation of a ( Zr55Cu30Al10Ni5)98Er2 Bulk Metallic Glass at 350-500oc · Anelastic ...

243

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":""}]}

244

Obstacles and Opportunity: Turbine Motorization in Refineries Today  

E-Print Network (OSTI)

Steam turbines have been widely used in oil refineries for driving pumps, compressors and other rotary machines. However, in recent years, the authors of this paper have seen substantial turbine motorization projects completed or being planned in the refineries. This paper discusses the key aspects that should be considered in evaluating the feasibility of motorization projects. Based on the literature review and a refinery survey conducted by the authors, the key factors include the critical level of the related equipment, the potential energy savings and capital cost, the steam and power balance in the related area, and the reliability in the refinery's power supply. Based on the authors' experience, the utilities' energy efficiency incentive programs in California also influence the decision-making process for turbine motorization projects. Therefore, this paper includes a description of the utilities' guidelines for fuel substitution projects. In particular, the utilities' three-prong requirements on net source-BTU energy savings, cost effectiveness, and avoidance of adverse impacts to the environment are discussed. Two real life case studies are presented to demonstrate how the above criteria should be applied for determining if a motorization opportunity is economically viable. A discussion on suggested features is also included for prescreening turbine motorization project candidates for better energy and environment economics such as venting of exhaust steam from a back pressure turbine and oversized design of the existing turbine and pump.

Feng, Hua; Liu, Jinghing; Liu, Xiang; Ahmad, Mushtaq; Deng, Alan

2012-01-01T23:59:59.000Z

245

Refinery Outages: Description and Potential Impact on Petroleum Product Prices  

Reports and Publications (EIA)

This report responds to a July 13, 2006 request from Chairman Jeff Bingaman of the Senate Committee on Energy and Natural Resources requested that EIA conduct a study of the impact that refinery shutdowns have had on the price of oil and gasoline.

Joanne Shore

2007-03-27T23:59:59.000Z

246

U.S. LPG's Consumed at Refineries (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. LPG's Consumed at Refineries (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's: 8,966: 8,021: 9,466: 11,962 ...

247

U.S. Refinery Yield of Petroleum Coke (Percent)  

U.S. Energy Information Administration (EIA)

U.S. Refinery Yield of Petroleum Coke (Percent) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1990's: 4.3: 4.3: 4.3: ...

248

U.S. Refinery Yield of Petroleum Coke (Percent)  

U.S. Energy Information Administration (EIA)

U.S. Refinery Yield of Petroleum Coke (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: 4.4: 4.6: 4.5: 4.3: 4.1: 4.2: 4.4: 4.3: ...

249

Energy efficiency improvement and cost saving opportunities forpetroleum refineries  

Science Conference Proceedings (OSTI)

The petroleum refining industry in the United States is the largest in the world, providing inputs to virtually any economic sector,including the transport sector and the chemical industry. The industry operates 146 refineries (as of January 2004) around the country,employing over 65,000 employees. The refining industry produces a mix of products with a total value exceeding $151 billion. Refineries spend typically 50 percent of cash operating costs (i.e., excluding capital costs and depreciation) on energy, making energy a major cost factor and also an important opportunity for cost reduction. Energy use is also a major source of emissions in the refinery industry making energy efficiency improvement an attractive opportunity to reduce emissions and operating costs. Voluntary government programs aim to assist industry to improve competitiveness through increased energy efficiency and reduced environmental impact. ENERGY STAR (R), a voluntary program managed by the U.S. Environmental Protection Agency, stresses the need for strong and strategic corporate energy management programs. ENERGY STAR provides energy management tools and strategies for successful corporate energy management programs. This Energy Guide describes research conducted to support ENERGY STAR and its work with the petroleum refining industry.This research provides information on potential energy efficiency opportunities for petroleum refineries. This Energy Guide introduces energy efficiency opportunities available for petroleum refineries. It begins with descriptions of the trends, structure, and production of the refining industry and the energy used in the refining and conversion processes. Specific energy savings for each energy efficiency measure based on case studies of plants and references to technical literature are provided. If available, typical payback periods are also listed. The Energy Guide draws upon the experiences with energy efficiency measures of petroleum refineries worldwide. The findings suggest that given available resources and technology, there are opportunities to reduce energy consumption cost-effectively in the petroleum refining industry while maintaining the quality of the products manufactured. Further research on the economics of the measures, as well as the applicability of these to individual refineries, is needed to assess the feasibility of implementation of selected technologies at individual plants.

Worrell, Ernst; Galitsky, Christina

2005-02-15T23:59:59.000Z

250

Market survey on products from the Tema Oil Refinery carried out as part of the feasibility study on the Tema Oil Refinery expansion project. Export trade information  

SciTech Connect

The Tema Oil Refinery (TOR), which was commissioned in 1963, is a simple hydroskimming plant which processes crude oil into LPG, gasoline, kerosene, gasoil, and fuel oil. It is the only petroleum refinery in Ghana. Over the years some of the equipment in the refinery has deteriorated or become obsolete necessitating major rehabilitation. A feasibility study is investigating the modernization and expansion of the refinery to meet projected market demands until the year 2005. The report presents the results of a market survey done on products from TOR.

Not Available

1991-10-01T23:59:59.000Z

251

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

NLE Websites -- All DOE Office Websites (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

252

Approximating Buy-at-Bulk k-Steiner trees  

E-Print Network (OSTI)

In the buy-at-bulk $k$-Steiner tree (or rent-or-buy$k$-Steiner tree) problem we are given a graph $G(V,E)$ with a setof terminals $T\\subseteq V$ including a particular vertex $s$ calledthe root, and an integer $k\\leq |T|$. ...

Hajiaghayi, MohammadTaghi

2005-11-15T23:59:59.000Z

253

Alternative future environmental regulatory approaches for petroleum refineries.  

Science Conference Proceedings (OSTI)

Recently, many industrial, regulatory, and community leaders have expressed concern that the current environmental regulatory structure disregards multimedia environmental impacts, provides few incentives to develop and use new technologies, and fails to consider site-specific conditions. For the US petroleum refining industry, faced with the need to produce higher-quality fuels from poorer-quality feedstocks, such criticisms are expected to increase. This article offers two alternative environmental regulatory approaches for existing petroleum refineries to use in the future. These alternative approaches are multimedia in scope, provide for new technology development and use, and allow flexibility in the means for meeting environmental goals. They have been reviewed and critiqued by various stakeholders, including industry representatives, regulators, and local and national community and environmental organizations. The integration of stakeholder comments and findings of ongoing national and international regulatory reinvention efforts in the development of these approaches positions them for potential use by other industries in addition to petroleum refineries.

Elcock, D.; Gasper, J.; Moses, D. O.; Emerson, D.; Arguerro, R.; Environmental Assessment; DOE; Analytical Services, Inc.

2000-01-01T23:59:59.000Z

254

New process effectively recovers oil from refinery waste streams  

Science Conference Proceedings (OSTI)

A new process uses chemically assisted, thermal flashing to break difficult emulsions and recover oil for reprocessing. The process is best suited for refinery waste management and slop oil systems, where it can process streams with high oil content to recover high-quality oil. Recent testing of a full-scale, commercial prototype unit on slop oil emulsions at a major Gulf Coast refinery resulted in: 97.9% recovery of oil with 99.3--99.6% purity; 99.5% recovery of water with 99+% purity; and a centrifuge cake containing 49-60% solids, 23--30 oil, and 17--22% water. The paper discusses background of the process, then gives a process description as well as results of field studies and cost.

Rhodes, A.

1994-08-15T23:59:59.000Z

255

Pemex to acquire interest in Shell Texas refinery  

Science Conference Proceedings (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

256

Martinez Refinery Completes Plant-Wide Energy Assessment  

SciTech Connect

This OIT BestPractices Case Study describes how the Equilon Enterprises oil refinery in Martinez, California undertook a plant-wide energy assessment that focused on three key areas: waste minimization, process debottlenecking, and operations optimization. The assessment yielded recommendations, which, if implemented, can save more than 6,000,000 MMBtu per year and an estimated $52,000,000 per year, plus improve process control and reduce waste.

Not Available

2002-11-01T23:59:59.000Z

257

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

SciTech Connect

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

258

Petroleum complex of Russia. Reconstruction of petroleum refineries: Means for accomplishing the task  

SciTech Connect

This report describes the refining industry in Russia with respect to production and economic factors. The modernization and reconstruction of the refineries is also discussed.

Rykunova, T.

1994-11-01T23:59:59.000Z

259

New desorption process treats refinery K and F wastes in demo trial  

SciTech Connect

A new desorption process for treating refinery wastes has been proven in pilot demonstrations at Amoco Oil Co.'s Texas City, Tex., refinery. The process -- Waste-Tech Services Inc.'s desorption and recovery unit (DRU) -- treats petroleum-contaminated refinery wastes and recovers oil and water suitable for recycling to the refinery. The DRU meets Resource Conservation and Recovery Act (RCRA) recycle exemptions and produces solids that satisfy US Environmental Protection Agency (EPA) land disposal restrictions (LDRs). This paper discusses RCRA wastes, the process, the demonstration unit, operating conditions, and analyses of semivolatiles, volatiles, leachable metals, and recovered oil and water.

Rasmussen, G.P. (Waste-Tech Services Inc., Golden, CO (United States))

1994-01-10T23:59:59.000Z

260

Economic forces push down selling prices of U.S. refineries  

Science Conference Proceedings (OSTI)

Recent data on US refinery sales reveal that selling prices have continued to decline in the 1990s. Reasons for this decrease include increased plant investments to meet regulatory requirements, excess refining capacity, increased imports of refined products, and reduced margins. While these expenditures enable a refinery to continue operating, they do not make the refinery more profitable or valuable. Other factors contributing to reduced selling prices of US refineries are: declining local crude production; unstable crude costs; increased energy conservation; growing competition from alternative fuels.

NONE

1996-03-25T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

The Revival of Onahama Smelter & Refinery from the Disaster by the ...  

Science Conference Proceedings (OSTI)

Presentation Title, The Revival of Onahama Smelter & Refinery from the ... Study of Modified Semi-Coke on the Advanced Treatment of Coking Wastewater's Oil.

262

Aspects of Holly Corporation's Acquisition of Sunoco Inc.'s Tulsa, Oklahoma Refinery  

Reports and Publications (EIA)

The Energy Information Administration has produced a review of aspects of the Holly's acquisition of Sunoco's 85,000-barrels-per-day Tulsa refinery

Neal Davis

2009-04-22T23:59:59.000Z

263

The Heliospheric Termination Shock  

E-Print Network (OSTI)

The heliospheric Termination Shock is the largest (by dimension) shock in the heliosphere. It is believed that it is also the strongest shock and is responsible for the generation of the Anomalous Cosmic Ray component in the heliosphere. This chapter review the gross properties and observations of the Termination Shock. It is structured as follows: 1. The heliosphere, providing the heliospheric stage for Termination Shock formation, 2. The argument for a heliospheric Termination Shock, 3. The global heliospheric system, 4. Termination Shock properties, 5. Observations: the Voyager passages, radio observations, plasma waves and electron beams, traces of plasma and magnetic field, energetic particles, galactic cosmic rays, Termination Shock particles, the anomalous cosmic ray component, 6. Conclusions.

R. A. Treumann; C. H. Jaroschek

2008-07-25T23:59:59.000Z

264

Terminal automation system maintenance  

SciTech Connect

Nothing has improved petroleum product loading in recent years more than terminal automation systems. The presence of terminal automation systems (TAS) at loading racks has increased operational efficiency and safety and enhanced their accounting and management capabilities. However, like all finite systems, they occasionally malfunction or fail. Proper servicing and maintenance can minimize this. And in the unlikely event a TAS breakdown does occur, prompt and effective troubleshooting can reduce its impact on terminal productivity. To accommodate around-the-clock loading at racks, increasingly unattended by terminal personnel, TAS maintenance, servicing and troubleshooting has become increasingly demanding. It has also become increasingly important. After 15 years of trial and error at petroleum and petrochemical storage and transfer terminals, a number of successful troubleshooting programs have been developed. These include 24-hour {open_quotes}help hotlines,{close_quotes} internal (terminal company) and external (supplier) support staff, and {open_quotes}layered{close_quotes} support. These programs are described.

Coffelt, D.; Hewitt, J. [Engineered Systems Inc., Tempe, AZ (United States)

1997-01-01T23:59:59.000Z

265

Status Company Terminal Term  

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

Status of Short-Term Applications to Export Previously Imported LNG (as of March 5, 2013) Status Company Terminal Term (Years) Authorized Volume (Equivalent Bcf in natural gas)...

266

Superconducting Cable Termination  

SciTech Connect

Disclosed is a termination that connects high temperature superconducting (HTS) cable immersed in pressurized liquid nitrogen to high voltage and neutral (shield) external bushings at ambient temperature and pressure. The termination consists of a splice between the HTS power (inner) and shield (outer) conductors and concentric copper pipes which are the conductors in the termination. There is also a transition from the dielectric tape insulator used in the HTS cable to the insulators used between and around the copper pipe conductors in the termination. At the warm end of the termination the copper pipes are connected via copper braided straps to the conventional warm external bushings which have low thermal stresses. This termination allows for a natural temperature gradient in the copper pipe conductors inside the termination which enables the controlled flashing of the pressurized liquid coolant (nitrogen) to the gaseous state. Thus the entire termination is near the coolant supply pressure and the high voltage and shield cold bushings, a highly stressed component used in most HTS cables, are eliminated. A sliding seal allows for cable contraction as it is cooled from room temperature to ˜72-82 K. Seals, static vacuum, and multi-layer superinsulation minimize radial heat leak to the environment.

Sinha, Uday K. (Carrollton, GA); Tolbert, Jerry (Newnan, GA)

2005-08-30T23:59:59.000Z

267

Clean air amendments put big burden on refinery planners  

SciTech Connect

The Clean Air Act Amendments of 1990 will not only require the production of reformulated gasoline but also have significant impact on other refinery-related construction. This must be considered when developing sound planning strategy. The three titles of the Clean Air Act Amendments that will have the greatest effect on refining are: Title I: Nonattainment; Title III: Air toxics; Title V: Permitting. To understand the ramifications of these amendments, it is necessary to review the interactions of new requirements with the permitting and construction schedule shown.

Scherr, R.C.; Smalley, G.A. Jr.; Norman, M.E. (ENSR Consulting and Engineering, Houston, TX (US))

1991-06-10T23:59:59.000Z

268

Feasibility study report for the Imperial Valley Ethanol Refinery: a 14. 9-million-gallon-per-year ethanol synfuel refinery utilizing geothermal energy  

DOE Green Energy (OSTI)

The construction and operation of a 14,980,000 gallon per year fuel ethanol from grain refinery in the Imperial Valley of California is proposed. The Imperial Valley Ethanol Refinery (refinery) will use hot geothermal fluid from geothermal resources at the East Mesa area as the source of process energy. In order to evaluate the economic viability of the proposed Project, exhaustive engineering, cost analysis, and financial studies have been undertaken. This report presents the results of feasibility studies undertaken in geothermal resource, engineering, marketing financing, management, environment, and permits and approvals. The conclusion of these studies is that the Project is economically viable. US Alcohol Fuels is proceeding with its plans to construct and operate the Refinery.

Not Available

1981-03-01T23:59:59.000Z

269

Dark energy from bulk matter  

SciTech Connect

We consider the possibility of getting accelerated expansion and w=-1 crossing in the context of a braneworld cosmological setup, endowed with a bulk energy-momentum tensor. For a given ansatz of the bulk content, we demonstrate that the bulk pressures dominate the dynamics at late times and can lead to accelerated expansion. We also analyze the constraints under which we can get a realistic profile for the effective equation of state and conclude that matter in the bulk has the effect of dark energy on the brane. Furthermore, we show that it is possible to simulate the behavior to a Chaplygin gas using nonexotic bulk matter.

Bogdanos, C.; Dimitriadis, A.; Tamvakis, K. [Physics Department, University of Ioannina, Ioannina GR451 10 (Greece)

2007-04-15T23:59:59.000Z

270

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

Science Conference Proceedings (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

271

Implementing an Energy Management Strategy for a Houston Refinery  

E-Print Network (OSTI)

Intense competition and environmental regulation of industries utilizing combustion equipment have motivated many owners and operators to seek ways to reduce costs, improve performance, and minimize emissions. Energy management programs are being implemented throughout industry to improve equipment operating efficiencies, profitability, extend equipment life, prevent forced shutdowns, generate substantial fuel savings, track valuable information, and enhance compliance margins. A well designed and maintained energy management program translates to PROFIT added directly to the BOTTOM LINE. Woodward-Clyde Consultants (WCC) recently implemented and energy management program at the Lyondell-Citgo Refinery in Houston, Texas. The basis of the program is the 80/20 rule where 80% of the total potential savings are derived from optimizing the energy utilization from 20% of the combustion equipment. In this case, 11 out of 55 heaters were targeted for inclusion in the program. The fuel savings potential alone exceeded $1,250,000. In addition to the fuel savings, there were reduced costs from improved operation, as well as reduction in maintenance requirements and forced shutdowns. The remainder of this paper discusses the technical approach, the benefits, and the results of the program implemented at the Lyondell-Citgo Refinery.

Wood, S. C.; Agrawal, R. K.; Canon, D.

1996-04-01T23:59:59.000Z

272

Creating bulk nanocrystalline metal.  

Science Conference Proceedings (OSTI)

Nanocrystalline and nanostructured materials offer unique microstructure-dependent properties that are superior to coarse-grained materials. These materials have been shown to have very high hardness, strength, and wear resistance. However, most current methods of producing nanostructured materials in weapons-relevant materials create powdered metal that must be consolidated into bulk form to be useful. Conventional consolidation methods are not appropriate due to the need to maintain the nanocrystalline structure. This research investigated new ways of creating nanocrystalline material, new methods of consolidating nanocrystalline material, and an analysis of these different methods of creation and consolidation to evaluate their applicability to mesoscale weapons applications where part features are often under 100 {micro}m wide and the material's microstructure must be very small to give homogeneous properties across the feature.

Fredenburg, D. Anthony (Georgia Institute of Technology, Atlanta, GA); Saldana, Christopher J. (Purdue University, West Lafayette, IN); Gill, David D.; Hall, Aaron Christopher; Roemer, Timothy John (Ktech Corporation, Albuquerque, NM); Vogler, Tracy John; Yang, Pin

2008-10-01T23:59:59.000Z

273

Auxiliary battery charging terminal  

SciTech Connect

In accordance with the present invention there is provided an auxiliary battery charging terminal that may selectively engage battery charging circuitry inside a portable radio pager. There is provided a current conducting cap having a downwardly and outwardly flared rim that deforms to lock under the crimped edge an insulating seal ring of a standard rechargeable cell by application of a compressive axial force. The auxiliary battery charging terminal is further provided with a central tip axially projecting upwardly from the cap. The auxiliary terminal may be further provided with a cap of reduced diameter to circumferentially engage the raised battery cathode terminal on the battery cell. A mating recess in a remote battery charging receptacle may receive the tip to captivate the battery cell against lateral displacement. The tip may be further provided with a rounded apex to relieve localized frictional forces upon insertion and removal of the battery cell from the remote battery charging receptacle.

Field, H.; Richter, R. E.

1985-04-23T23:59:59.000Z

274

Cirrus Crystal Terminal Velocities  

Science Conference Proceedings (OSTI)

Cirrus crystal terminal velocities are of primary importance in determining the rate of transport of condensate from upper- to middle-tropospheric levels and profoundly influence the earth’s radiation balance through their effect on the rate of ...

Andrew J. Heymsfield; Jean Iaquinta

2000-04-01T23:59:59.000Z

275

SECURITY TERMINATION STATEMENT | Department of Energy  

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

SECURITY TERMINATION STATEMENT SECURITY TERMINATION STATEMENT Form provides an individual's statement in connection with the termination of access authorization (security...

276

Hydrotreating Pyrolytic Lignin to Produce a Refinery Feedstock (Poster)  

Science Conference Proceedings (OSTI)

Fast pyrolysis of biomass followed by water separation to produce pyrolytic lignin and hydrotreating of the lignin could be used to produce a stable volatile low-oxygen intermediate liquid. Such a liquid could be converted into a finished motor-fuel in a refinery, taking advantage of the existing infrastructure and economies of scale of refineries. Hydrotreating just the lignin would consume less hydrogen while preserving about half of the energy of the original oil. The aqueous by-products could be reformed to produce the needed hydrogen and would contain much of the unwanted acids and unstable oxygenates. To assess such intermediate liquids, several pyrolytic lignins were prepared by mixing pyrolysis oil with water at 1:1 and 3:1 ratios. The carboxylic acidity in the pyrolytic lignin was reduced to 24 and 10 mg-KOH/g-lignin compared to 81 in the whole oil. These lignins were hydrotreated using Ni-Mo(S)/alumina, Pt/char, or Pd/C(activated) in a semi-batch 1 L stirred autoclave. The oil was stabilized under hydrogen at 150-280 degrees C, then water and light organics were removed by partial depressurization. Hydrodeoxygenation was then performed at 340-400 degrees C. Total pressure was controlled at 70 or 170 bar with hydrogen gas. Organic liquid yields of 39-56% were obtained. For many experiments the organic oxygen content was oil, the volatility was greater than or equal to 94% and, on a carbon basis, the total yield of organic products miscible in hydrocarbons at a 1:10 ratio was over 50%. These properties are probably acceptable to a refinery.The residual liquids left in the reactor at the end of the experiment comprised 60-85% of the organic-phase product while the rest was condensate. 13C-NMR of the residual liquids showed that they were 50-80% aliphatic. 13C-NMR coupled with GC-MS identified phenolic compounds as the main oxygenates in most residual liquids.

French, R. J.

2013-09-01T23:59:59.000Z

277

Hydrotreating Pyrolytic Lignin to Produce a Refinery Feedstock (Poster)  

DOE Green Energy (OSTI)

Fast pyrolysis of biomass followed by water separation to produce pyrolytic lignin and hydrotreating of the lignin could be used to produce a stable volatile low-oxygen intermediate liquid. Such a liquid could be converted into a finished motor-fuel in a refinery, taking advantage of the existing infrastructure and economies of scale of refineries. Hydrotreating just the lignin would consume less hydrogen while preserving about half of the energy of the original oil. The aqueous by-products could be reformed to produce the needed hydrogen and would contain much of the unwanted acids and unstable oxygenates. To assess such intermediate liquids, several pyrolytic lignins were prepared by mixing pyrolysis oil with water at 1:1 and 3:1 ratios. The carboxylic acidity in the pyrolytic lignin was reduced to 24 and 10 mg-KOH/g-lignin compared to 81 in the whole oil. These lignins were hydrotreated using Ni-Mo(S)/alumina, Pt/char, or Pd/C(activated) in a semi-batch 1 L stirred autoclave. The oil was stabilized under hydrogen at 150-280 degrees C, then water and light organics were removed by partial depressurization. Hydrodeoxygenation was then performed at 340-400 degrees C. Total pressure was controlled at 70 or 170 bar with hydrogen gas. Organic liquid yields of 39-56% were obtained. For many experiments the organic oxygen content was <7%, acidity was < 7 mg-KOH/g-oil, the volatility was greater than or equal to 94% and, on a carbon basis, the total yield of organic products miscible in hydrocarbons at a 1:10 ratio was over 50%. These properties are probably acceptable to a refinery.The residual liquids left in the reactor at the end of the experiment comprised 60-85% of the organic-phase product while the rest was condensate. 13C-NMR of the residual liquids showed that they were 50-80% aliphatic. 13C-NMR coupled with GC-MS identified phenolic compounds as the main oxygenates in most residual liquids.

French, R. J.

2013-09-01T23:59:59.000Z

278

,"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"

279

,"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"

280

,"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"

Note: This page contains sample records for the topic "refinery bulk terminal" 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

,"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"

282

Market Assessment of Planned Refinery Outages March Â… 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.

283

Optimization of Steam Network in Tehran Oil Refinery  

E-Print Network (OSTI)

Dominated energy crisis in the world dictates to reduce energy consumption and identify energy saving opportunities in large and complex industries especially in oil refining industry. In this paper, Tehran oil refinery is considered as a proper case study and its steam network is analyzed. At the first step, using STAR software, the steam network is simulated and then optimized, which determines the optimum conditions. In this regard, energy saving potential was identified and total operating costs (TOC) in two states of fixed fuel fraction and changeable fuel fraction was calculated. In addition, different scenarios were proposed like using HRSG instead of two boilers. The results showed that amount of total operating cost has been reduced, as the result the best scenario regarding TOC is selected.

Khodaie, H.; Nasr, M. R. J.

2008-01-01T23:59:59.000Z

284

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 and Refining Sectors Advisory Committee as streams with a temperature below 400 degrees F. Their waste energy streams were also characterized as to state, flow rate, heat content, source and temperature. These criteria were then used to identify potential candidates of waste heat recovery technologies that might have an application in these industries. Four technologies that met the criteria of the Advisory Committee included: organic rankine cycle (ORC), absorption refrigeration and chilling, Kalina cycle, and fuel cell technologies. This paper characterizes each of these technologies, technical specifications, limitations, potential costs/ payback and commercialization status as was discussed in the Technology Forum held in Houston, TX in May 2012 (TXIOF 2012).

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

2013-01-01T23:59:59.000Z

285

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

286

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

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

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

287

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 /

288

Appendix D Short-Term Analysis of Refinery Costs and Supply  

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

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-

289

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

E-Print Network (OSTI)

Integrating gas turbines with refinery furnaces can be a cost effective means of reducing NOx emissions while also generating electricity at an attractive heat rate. Design considerations and system costs are presented.

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

1985-05-01T23:59:59.000Z

290

U.S. Refinery and Blender Net Production of Normal Butane ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery and Blender Net Production of Normal Butane (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993-884: 268: 4,851: 6,387: 6,489 ...

291

Valero: Houston Refinery Uses Plant-Wide Assessment to Develop an Energy Optimization and Management System  

SciTech Connect

This Industrial Technologies Program case study describes an energy assessment team's recommendations for saving $5 million in energy, water, and other costs at an oil refinery in Houston, Texas.

Not Available

2005-08-01T23:59:59.000Z

292

U.S. Refinery Hydrogen Production Capacity as of January 1 ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Hydrogen Production Capacity as of January 1 (Million Cubic Feet per Day) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 ...

293

U.S. Refinery Normal Butane/Butylene Shell Storage Capacity as ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Normal Butane/Butylene Shell Storage Capacity as of January 1 (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 ...

294

Models and algorithms for a multilevel control system of primary oil refinery installations  

Science Conference Proceedings (OSTI)

Algorithms and mathematical models for the technological process of primary oil refinery operating in the uncertain conditions are developed; the solution of the optimal control problem in the form of stochastic programming with probabilistic characteristics ...

I. A. Guseinov; E. A. Melikov; N. A. Khanbutaeva; I. R. Efendiev

2012-02-01T23:59:59.000Z

295

West Coast (PADD 5) Foreign Crude Oil Refinery Receipts by Tank ...  

U.S. Energy Information Administration (EIA)

West Coast (PADD 5) Foreign Crude Oil Refinery Receipts by Tank Cars (Rail) (Thousand Barrels) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 ...

296

Welding electric terminals ultrasonically  

SciTech Connect

Ultrasonic welding has been investigated for use on foil conductor terminations. Equipment and tooling have been improved; material considerations and combinations have been evaluated to determine their effects on the process; and special configurations and techniques have been studied to extend the applicability of the ultrasonic welding process.

Darner, G.S.

1976-09-01T23:59:59.000Z

297

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

SciTech Connect

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

298

Bulk Power Transmission Study  

E-Print Network (OSTI)

"Texans now have a choice. We can become more efficient and maintain our standard of living, or we can continue business as usual and watch our standard of living erode from competition from other regions. In the past, except for improving reliability, there was no need for a strong transmission system. When Texas generation was primarily gas fueled, the extensive natural gas pipeline network moved energy easily within the state. In recent years two things have changed: 1. Electric utilities have made extensive investment in lignite, coal, and nuclear plants and, 2. Improvements in gas turbine technology and the removal of institutional barriers has encouraged cogeneration at many of our energy intensive process industries. This energy diversity means that there are now significant differences in energy costs between units. The variable costs of generation of power can vary between units by a ratio of 2 or 3 to 1 and this difference will be accentuated when energy costs rise (and they will; it’s a question of when, not if). The potential for costs savings by optional dispatching of the entire interconnected system are greater than ever before as demonstrated by the PUC's Bulk Power Transmission Study. And the potential can be enhanced with added transmission system investment. Cogeneration and small power production has proven to be the most cost effective way for Texas to add additional generating capacity needed to supply an economy that is starting to rebound and to replace old, obsolete power plants. The freedom to locate these facilities at the fuel source or at the site of large thermal demand makes real economic and environmental sense. The use of renewable or waste fuels allows something that would otherwise be wasted to contribute to our economy. Fossil fuels that are displaced can be redirected to another use or consumed for future benefit. By integrating a gas turbine generator with a. process plant, the natural gas required for producing electricity can be reduced by 40% below that required for a combined cycle. The heat rejected from a gas turbine, combined cycle, or steam plant can be redirected to a process use that contributes to our economy by producing something of value to world markets. By contrast a conventional power plant is paid for by the rate payers and consumes Texas natural resources and therefore is a burden rather than an enhancement to our economy. The optimal location of facilities are possible only if there is an adequate transmission system. Utility, consumer and industry must cooperate to improve our transmission system for the benefit of all Texas. The Texas Public Utilities Commission has taken the lead in promoting efficiency by requiring transmission wheeling between qualifying facilities and electric utilities. Several cogeneration facilities have been constructed as a result. In order to encourage small power production, the rule needs to be expanded to include projects interconnected with distribution systems. Most renewable resource projects are relatively small and cannot afford the cost of a high voltage interconnect, and yet their characteristics match a baseload need. The ability to wheel power to a utility that needs base load power from a distribution level interconnection is essential to development of these smaller projects."

John, T.

1988-09-01T23:59:59.000Z

299

bulk power | OpenEI  

Open Energy Info (EERE)

bulk power bulk power Dataset Summary Description The Form EIA-411, "Coordinated Bulk Power Supply Program Report," collects information from the Nation's power system planners about the electricity supply, both capacity and energy, that is needed to serve current demand and for future growth. Source Energy Information Administration (EIA) Date Released December 03rd, 2010 (3 years ago) Date Updated December 03rd, 2010 (3 years ago) Keywords bulk power EIA Electricity Generation Data application/vnd.ms-excel icon Net Energy for Load - Historic, Actual and Projected Five-Years (xls, 26.1 KiB) application/vnd.ms-excel icon Noncoincident Peak Load - Historic, Actual and Projected Five-Years (xls, 25.6 KiB) application/vnd.ms-excel icon Noncoincident Peak Load - Historic, Actual and Projected Five-Years (xls, 0 bytes)

300

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

Note: This page contains sample records for the topic "refinery bulk terminal" 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

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

302

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

303

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

304

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

305

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

SciTech Connect

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

306

Ductility of Bulk Nanostructured Materials - Programmaster.org  

Science Conference Proceedings (OSTI)

Geometry Dependence of the Strain-driven Self-rolling of Semiconductor Nanotubes · Gold Nano-Engineered Mercury Sensor for Alumina Refineries.

307

Bulk Functional Materials Obtained by Shock Waves Compaction of ...  

Science Conference Proceedings (OSTI)

Geometry Dependence of the Strain-driven Self-rolling of Semiconductor Nanotubes · Gold Nano-Engineered Mercury Sensor for Alumina Refineries.

308

Robbins Corn & Bulk Services | Open Energy Information  

Open Energy Info (EERE)

Robbins Corn & Bulk Services Jump to: navigation, search Name Robbins Corn & Bulk Services Place Sackets Harbor, NY Information About Partnership with NREL Partnership with NREL...

309

A Case Study of Steam System Evaluation in a Petroleum Refinery  

E-Print Network (OSTI)

ASI conducted a steam system evaluation study at a multinational petroleum Refinery located in the Eastern UK during June-July, 1999. At this refinery, Steam, Fuel and Electricity systems are inter-connected. Steam is generated from direct fuel fired boilers as well from Furnace and Kiln waste heat. Steam is also supplied from the CHP waste heat boilers. Steam generation averages 1,500,000 lbs/hr and does not change significantly between winter and summer since steam needs for process and power generation dominates way above comfort heating. To generate steam, the refinery spends about £28 million per year ($46 million). The system evaluation study identified 31 Energy & steam system cost savings measures (ECM) to save fuel, steam and condensate in the areas of: Steam generation, Steam distribution, Steam Utilization, Condensate recovery, and Combustion optimization in kilns. By implementing all the above 31 ECMs, the refinery is estimated to save $3.5 million annually. Based on our preliminary investment estimate the average payback would be within 2 years. The refinery also would reduce 5600 metric tons Carbon emission to environment. Some of the opportunities address the installation defects of the steam system components that would improve the system reliability and longevity.

Venkatesan, V. V.; Iordanova, N.

2003-05-01T23:59:59.000Z

310

FEASIBILITY STUDY FOR A PETROLEUM REFINERY FOR THE JICARILLA APACHE TRIBE  

Science Conference Proceedings (OSTI)

A feasibility study for a proposed petroleum refinery for the Jicarilla Apache Indian Reservation was performed. The available crude oil production was identified and characterized. There is 6,000 barrels per day of crude oil production available for processing in the proposed refinery. The proposed refinery will utilize a lower temperature, smaller crude fractionation unit. It will have a Naphtha Hydrodesulfurizer and Reformer to produce high octane gasoline. The surplus hydrogen from the reformer will be used in a specialized hydrocracker to convert the heavier crude oil fractions to ultra low sulfur gasoline and diesel fuel products. The proposed refinery will produce gasoline, jet fuel, diesel fuel, and a minimal amount of lube oil. The refinery will require about $86,700,000 to construct. It will have net annual pre-tax profit of about $17,000,000. The estimated return on investment is 20%. The feasibility is positive subject to confirmation of long term crude supply. The study also identified procedures for evaluating processing options as a means for American Indian Tribes and Native American Corporations to maximize the value of their crude oil production.

John D. Jones

2004-10-01T23:59:59.000Z

311

,"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"

312

,"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"

313

Petroleum Refinery Catalytic Reforming -- Cutting High Energy Costs  

E-Print Network (OSTI)

Hydrocarbon reforming involves a variety of chemical reactions at high temperatures and pressures in the presence of suitable catalysts. The conversion of naptha to high octane aromatics requires high energy to initiate and sustain the reaction at temperatures of 850-950oF. Hydrogen - rich off - gases are fired in combinations of process furnaces. Heat is transferred to hydrocarbon fluids by radiation, principally. Feed or return stream temperatures determine the need for convection sections. It is essential that the operation and maintenance of these furnaces be optimized to minimize production costs. This paper describes the performance testing and evaluation of a set of ten refinery furnaces used to thermally drive several reforming reactors and to regenerate catalysts. Firing rates provide an input of 216.2 x 106 Btu/hr. to the furnaces, at $1.90 per 106 Btu. The units are fitted with multiple natural draft burners. There is insufficient turbulence and swirl in the burners. Operators manually set up the burners with excessive airflows for normal, full-load firing. These furnaces represent production limits. Products of combustion exhaust at high thermal levels - the range is from 985-1700oF. The mixed gases flow through a "waste heat" boiler, or they bypass the boiler and enter a single stack. Steam generation at 150 psig averages 38,200 lb/hr. Heat is wasted via the bypass at a rate of 41.1x106 Btu /hr. at 1240oF. When airflows are reduced (to 15% excess air) the loss will be 18.7x106 Btu/hr. at 1180oF. Installation of a second, parallel waste heat boiler will result in a saving of l3.4x106 Btu/hr. Energy savings at this furnace complex will be equivalent to $628,700 per year. Investment costs were estimated to be less than $250,000 for the proposed heat trap addition.

Viar, W. L.

1979-01-01T23:59:59.000Z

314

Bulk separation of carbon dioxide from natural gas  

SciTech Connect

In the bulk separation of carbon dioxide from feedstocks containing same in admixture with relatively nonsorbable gases using a zeolitic molecular sieve to adsorb selectively the carbon dioxide, higher product purity is attained by terminating the adsorption stroke using the feedstock while the bed still has capacity to adsorb more carbon dioxide at the same conditions, then purging the void space hydrocarbons from the bed using product carbon dioxide at a high partial pressure, and finally desorbing the bed by pressure reduction. (3 claims)

Collins, J.J.

1973-08-14T23:59:59.000Z

315

,"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"

316

Mazheikiai refinery modernization study. Final report. Volume 1. Export trade information  

SciTech Connect

The study, conducted by Foster Wheeler Corporation, was funded by the U.S. Trade and Development Agency on behalf of Lithuania's Ministry of Energy. The Mazheikiai Oil Refinery is the only one in the Baltic Region and serves the needs of Lithuania, Latvia, Estonia, and Kaliningrad. Before Lithuania's independence in 1990, the refinery was assured of crude supplies from Russia. However, since then the need has arisen to secure alternate sources of crude oil and the ability to process them. The purpose of the report is to provide recommendations to the Ministry of Energy for process improvements, environmental control measures, physical rehabilitation and energy conservation plans for the Mazheikiai Oil Refinery. This is Volume 1 of the study.

Not Available

1994-01-01T23:59:59.000Z

317

Mazheikiai refinery modernization study. Final report. Volume 3. Export trade information  

Science Conference Proceedings (OSTI)

The study, conducted by Foster Wheeler Corporation, was funded by the U.S. Trade and Development Agency on behalf of Lithuania's Ministry of Energy. The Mazheikiai Oil Refinery is the only one in the Baltic Region and serves the needs of Lithuania, Latvia, Estonia, and Kaliningrad. Before Lithuania's independence in 1990, the refinery was assured of crude supplies from Russia. However, since then the need has arisen to secure alternate sources of crude oil and the ability to process them. The purpose of the report is to provide recommendations to the Ministry of Energy for process improvements, environmental control measures, physical rehabilitation and energy conservation plans for the Mazheikiai Oil Refinery. This is Volume 3 of the study.

Not Available

1994-01-01T23:59:59.000Z

318

Mazheikiai refinery modernization study. Final report. Volume 2. Export trade information  

Science Conference Proceedings (OSTI)

The study, conducted by Foster Wheeler Corporation, was funded by the U.S. Trade and Development Agency on behalf of Lithuania's Ministry of Energy. The Mazheikiai Oil Refinery is the only one in the Baltic Region and serves the needs of Lithuania, Latvia, Estonia, and Kaliningrad. Before Lithuania's independence in 1990, the refinery was assured of crude supplies from Russia. However, since then the need has arisen to secure alternate sources of crude oil and the ability to process them. The purpose of the report is to provide recommendations to the Ministry of Energy for process improvements, environmental control measures, physical rehabilitation and energy conservation plans for the Mazheikiai Oil Refinery. This is Volume 2 of the study.

Not Available

1994-01-01T23:59:59.000Z

319

Potentials for fuel cells in refineries and chlor-alkali plants  

DOE Green Energy (OSTI)

The market potentials for fuel cell cogeneration systems in petroleum refineries and chlor-alkali plants were evaluated. the most promising application appears to be in chlor-alkali plants where the production process is electricity intensive. Future anticipated changes in the production process are favorable to the use of fuel cells. The energy use in refineries is steam intensive with the required steam pressures ranging from approximately 15 to 650 psig. The near-term use of fuel cell cogeneration in refineries is not as attractive as in chlor-alkali plants. The phosphoric acid fuel cell is the most developed and the most competitive, but its use is limited by its being able to produce only low-pressure steam. Over the longer term, the molten carbonate and the solid oxide fuel cell both of which operate at significantly higher temperatures, are technically very attractive. However, they do not appear to be cost competitive with conventional systems.

Altseimer, J.H.; Roach, F.

1986-01-01T23:59:59.000Z

320

Increasing Distillate Production at U.S. Refineries Â… 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

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Short-Term Schedulability Analysis of Crude Oil Operations in Refinery With Oil Residency Time Constraint Using Petri Nets  

Science Conference Proceedings (OSTI)

A short-term schedule for oil refinery should arrange all the activities in every detail for the whole scheduling horizon, leading to a complex problem. There lacks efficient techniques and software tools for its solution applicable to industrial oil ... Keywords: Automated manufacturing system, Petri net (PN), hybrid Petri net, oil refinery, scheduling, short-term scheduling

NaiQi Wu; Feng Chu; Chengbin Chu; MengChu Zhou

2008-11-01T23:59:59.000Z

322

Modeling and Conflict Detection of Crude Oil Operations for Refinery Process Based on Controlled Colored Timed Petri Net  

Science Conference Proceedings (OSTI)

Recently, there has been a great interest in the modeling and analysis of process industry, and various models are proposed for different uses. It is meaningful to have a model to serve as an analytical aid tool in short-term scheduling for oil refinery ... Keywords: Hybrid systems, petri net, refinery process, system modeling

Naiqi Wu; Liping Bai; Chengbin Chu

2007-07-01T23:59:59.000Z

323

CTR/ANL, July 2010 1 Updated Estimation of Energy Efficiencies of U.S. Petroleum Refineries  

E-Print Network (OSTI)

for emissions associated with hydrogen production. Hydrogen is generated in a refinery's catalytic reformer-process distillate material into commercial diesel and jet fuel. From this perspective catalytic reforming transfers refinery operations, most notably catalytic reforming. References Bredeson, L., Quiceno-Gonzalez, R., Riera

Argonne National Laboratory

324

,"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"

325

,"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"

326

Bulk Hauling Equipment for CHG  

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

BULK HAULING EQUIPMENT FOR CHG BULK HAULING EQUIPMENT FOR CHG Don Baldwin Director of Product Development - Hexagon Lincoln HEXAGON LINCOLN TITAN(tm) Module System Compressed Hydrogen Gas * Capacity 250 bar - 616 kg 350 bar - 809 kg 540 bar - 1155 kg * Gross Vehicle Weight (with prime mover) 250 bar - 28 450 kg 350 bar - 30 820 kg 540 bar - 39 440 kg * Purchase Cost 250 bar - $510,000 350 bar - $633,750 540 bar - $1,100,000 Compressed Natural Gas * Capacity (250 bar at 15 C) - 7412 kg * GVW (With prime mover) - 35 250 kg * Purchase Cost (+/- 5%) - $510,000 HEXAGON LINCOLN TITAN(tm) V Magnum Trailer System Compressed Hydrogen Gas * Capacity 250 bar - 800 kg 350 bar - 1050 kg 540 bar - 1500 kg * Gross Vehicle Weight (with prime mover) 250 bar - 31 000 kg 350 bar - 34 200 kg 540 bar - 45 700 kg * Purchase Cost (+/-

327

Allocation of energy use in petroleum refineries to petroleum products : implications for life-cycle energy use and emission inventory of petroleum transportation fuels.  

Science Conference Proceedings (OSTI)

Studies to evaluate the energy and emission impacts of vehicle/fuel systems have to address allocation of the energy use and emissions associated with petroleum refineries to various petroleum products because refineries produce multiple products. The allocation is needed in evaluating energy and emission effects of individual transportation fuels. Allocation methods used so far for petroleum-based fuels (e.g., gasoline, diesel, and liquefied petroleum gas [LPG]) are based primarily on mass, energy content, or market value shares of individual fuels from a given refinery. The aggregate approach at the refinery level is unable to account for the energy use and emission differences associated with producing individual fuels at the next sub-level: individual refining processes within a refinery. The approach ignores the fact that different refinery products go through different processes within a refinery. Allocation at the subprocess level (i.e., the refining process level) instead of at the aggregate process level (i.e., the refinery level) is advocated by the International Standard Organization. In this study, we seek a means of allocating total refinery energy use among various refinery products at the level of individual refinery processes. We present a petroleum refinery-process-based approach to allocating energy use in a petroleum refinery to petroleum refinery products according to mass, energy content, and market value share of final and intermediate petroleum products as they flow through refining processes within a refinery. The results from this study reveal that product-specific energy use based on the refinery process-level allocation differs considerably from that based on the refinery-level allocation. We calculated well-to-pump total energy use and greenhouse gas (GHG) emissions for gasoline, diesel, LPG, and naphtha with the refinery process-based allocation approach. For gasoline, the efficiency estimated from the refinery-level allocation underestimates gasoline energy use, relative to the process-level based gasoline efficiency. For diesel fuel, the well-to-pump energy use for the process-level allocations with the mass- and energy-content-based weighting factors is smaller than that predicted with the refinery-level allocations. However, the process-level allocation with the market-value-based weighting factors has results very close to those obtained by using the refinery-level allocations. For LPG, the refinery-level allocation significantly overestimates LPG energy use. For naphtha, the refinery-level allocation overestimates naphtha energy use. The GHG emission patterns for each of the fuels are similar to those of energy use.We presented a refining-process-level-based method that can be used to allocate energy use of individual refining processes to refinery products. The process-level-based method captures process-dependent characteristics of fuel production within a petroleum refinery. The method starts with the mass and energy flow chart of a refinery, tracks energy use by individual refining processes, and distributes energy use of a given refining process to products from the process. In allocating energy use to refinery products, the allocation method could rely on product mass, product energy contents, or product market values as weighting factors. While the mass- and energy-content-based allocation methods provide an engineering perspective of energy allocation within a refinery, the market-value-ased allocation method provides an economic perspective. The results from this study show that energy allocations at the aggregate refinery level and at the refining process level could make a difference in evaluating the energy use and emissions associated with individual petroleum products. Furthermore, for the refining-process-level allocation method, use of mass -- energy content- or market value share-based weighting factors could lead to different results for diesel fuels, LPG, and naphtha. We suggest that, when possible, energy use allocations should be made at the lowest subprocess level

Wang, M.; Lee, H.; Molburg, J.

2004-01-01T23:59:59.000Z

328

Markovian bulk-arrival and bulk-service queues with state-dependent control  

Science Conference Proceedings (OSTI)

We study a modified Markovian bulk-arrival and bulk-service queue incorporating state-dependent control. The stopped bulk-arrival and bulk-service queue is first investigated and the relationship with our queueing model is examined and exploited. Equilibrium ... Keywords: 60J27, 60J80, Bulk-arrival and bulk-service queues, Busy period distributions, Equilibrium distribution, Hitting times, Queue length distributions, State-dependent control, Transient behaviour

Anyue Chen; Phil Pollett; Junping Li; Hanjun Zhang

2010-03-01T23:59:59.000Z

329

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

E-Print Network (OSTI)

for the first time. Bioelectrochemical treatability was evaluated relative to oxygen demand. MECs were-oiled refinery wastewater sample from one site (DOW1) produced the best results, with 2.1 ± 0.2 A/m2 (maximum current density), 79% chemical oxygen demand removal, and 82% headspace biological oxygen demand removal

330

U.S. Gross Inputs to Refineries (Thousand Barrels per Day)  

U.S. Energy Information Administration (EIA)

U.S. Gross Inputs to Refineries (Thousand Barrels per Day) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1985: 11,583: 11,485: 11,484: 11,969: 12,269: 12,422 ...

331

CO2 Reduction through Optimization of Steam Network in Petroleum Refineries: Evaluation of New Scenario  

E-Print Network (OSTI)

Steam network of petroleum refinery is energy intensive, and consequently contribute significantly to the greenhouse gases emissions. A simple model for the estimation of CO2 emissions associated with operation of steam network as encountered in refineries is introduced. In conjunction with a shortcut model this model has been used to calculate of the steam network of an existing refinery aiming at minimization total annualized cost with considering emissions. In this paper, the case study is steam network of southern Tehran refinery. Simulation of this case has been performed in STAR software that licensed by energy system laboratory at K.N. Toosi University of Technology. Mathematical linear programming method has been applied to optimization of steam network. In addition, the short cut model of CO2 production has been provided for evaluation of steam network with considering CO2 production taxes and other economic effects in total annualized cost. Meanwhile, in this research, new scenario has been defined and evaluated. Results shows new scenario have 45 % less TAOC rather than base scenario in optimal condition.

Manesh, M. H. K; Khodaie, H.; Amidpour, M.

2008-01-01T23:59:59.000Z

332

U.S. Refinery Net Production of Normal Butane-Butylene (Thousand ...  

U.S. Energy Information Administration (EIA)

U.S. Refinery Net Production of Normal Butane-Butylene (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2005-4,241-2,244: 2,431: 7,319: 7,538 ...

333

THE NEW GASIFICATION PROJECT AT ENI SANNAZZARO REFINERY AND ITS INTEGRATION WITH A  

E-Print Network (OSTI)

Following the new regulation introduced in Europe in the last years, defining more stringent limits for the emissions to the atmosphere, the necessity to find an alternative use for the fuel oil has created a new challenge for the refineries. At the same time the need to improve the Italian power production has pushed Eni, the Italian energy company, to enter the electricity market.

Mwe Power Plant; Guido Collodi; Dario Camozzi; Snamprogetti Italy

2004-01-01T23:59:59.000Z

334

U.S. Kerosene-Type Jet Fuel Stocks at Refineries (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Kerosene-Type Jet Fuel Stocks at Refineries (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: 13,255: 14,640: 14,907: 15,583: 14,878 ...

335

Table 4b. U.S. Petroleum Refinery Balance (Million Barrels per Day ...  

U.S. Energy Information Administration (EIA)

Refinery Distillation Utilization Factor ..... 0.86 0.90 0.90 0.89 0.83 0.89 0.91 0.87 0.83 0.88 0.90 0.87 0.89 0.88 0.87 - = no data available Table 4b. U.S ...

336

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

337

Feasibility study on the modernization and expansion of the Tema Oil Refinery. Executive Summary. Export trade information  

Science Conference Proceedings (OSTI)

The Tema Oil Refinery (TOR), which was commissioned in 1963, is a simple hydro-skimming plant which processes crude oil into LPG, gasoline, kerosene, gasoil, and fuel oil. It is the only petroleum refinery in Ghana. Over the years some of the equipment in the refinery has deteriorated or become obsolete necessitating major rehabilitation. A study of the refinery expansion project takes into consideration earlier studies and, equally important, recognizes the extensive work done by TOR in rehabilitating the refinery. The program, carried out in phases because of funding limitations, has addressed the critical repairs and replacements in the process units and utilities necessary to prolong the life of the refinery and assure reliability and safe operation. It undertook the task of investigating the feasibility of modernizing and expanding the refinery at Tema, Ghana to meet projected market demands until the year 2005. A process planning study was conducted to select the optimal process and utility configuration which would result in economic benefits to Ghana.

Not Available

1992-04-01T23:59:59.000Z

338

Test plan, the Czechowice Oil Refinery bioremediation demonstration of a process waste lagoon. Revision 1  

SciTech Connect

The overall objective of the bioremediation project is to provide a cost effective bioremediation demonstration of petroleum contaminated soil at the Czechowice Oil Refinery. Additional objectives include training of personnel, and transfer of this technology by example to Poland, and the Risk Abatement Center for Central and Eastern Europe (RACE). The goal of the remediation is to reduce the risk of PAH compounds in soil and provide a green zone (grassy area) adjacent to the site boundary. Initial project discussions with the Czechowice Oil Refinery resulted in helping the refinery find an immediate cost effective solution for the dense organic sludge in the lagoons. They found that when mixed with other waste materials, the sludge could be sold as a fuel source to local cement kilns. Thus the waste was incinerated and provided a revenue stream for the refinery to cleanup the lagoon. This allowed the bioremediation project to focus on remediation of contaminated soil that unusable as fuel, less recalcitrant and easier to handle and remediate. The assessment identified 19 compounds at the refinery that represented significant risk and would require remediation. These compounds consisted of metals, PAH`s, and BTEX. The contaminated soil to be remediated in the bioremediation demonstration contains only PAH (BTEX and metals are not significantly above background concentrations). The final biopile design consists of (1) dewatering and clearing lagoon A to clean clay, (2) adding a 20 cm layer of dolomite with pipes for drainage, leachate collection, air injection, and pH adjustment, (3) adding a 1.1 m layer of contaminated soil mixed with wood chips to improve permeability, and (4) completing the surface with 20 cm of top soil planted with grass.

Altman, D.J.; Hazen, T.C.; Tien, A.J. [Westinghouse Savannah River Co., Aiken, SC (United States). Savannah River Technology Center; Worsztynowicz, A.; Ulfig, K. [Inst. for Ecology of Industrial Areas, Katowice (Poland)

1997-05-10T23:59:59.000Z

339

Comparison of the response of bacterial luminescence and mitochondrial respiration to the effluent of an oil refinery  

Science Conference Proceedings (OSTI)

The effects of oil refinery effluents on rat mitochondrial respiration and on the luminescence of the bacterium Photobacterium phosphoreum were compared. Mitochondria from male Wistar rat livers were exposed to different concentrations of refinery effluents in a semiclosed 3-ml reaction vessel. Respiration was measured polarographically with an oxygen electrode. Effects on P. phosphoreum were measured by the standard test developed by Microbics. The mitochondrial method showed EC50s in the range from 1 to 7.5%, while Microtox gave EC50 in the range from 30 to 42%. The higher sensitivity of mitochondria may be exploited in the development of a sensitive biosensor for toxicity of oil refinery effluents.

Riisberg, M.; Bratlie, E.; Stenersen, J. [Univ. of Oslo (Norway)

1996-04-01T23:59:59.000Z

340

West Coast (PADD 5) Bulk Terminal - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

Area: Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History; Crude Oil and Petroleum Products: 27,704: ... 51: 202: 1993-2013: Liquefied Petroleum Gases: 1,368 ...

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Numerical Simulation of an Industrial Cumulus Affected by Heat, Moisture, and CCN Released from an Oil Refinery  

Science Conference Proceedings (OSTI)

Large oil refineries emit heat, vapor, and cloud condensation nuclei (CCN), all of which can affect the formation of cloud and precipitation. This study quantities the relative contributions of the three factors on cloud development in calm wind ...

S. Guan; G. W. Reuter

1996-08-01T23:59:59.000Z

342

Three-dimensional terminal toric flips  

E-Print Network (OSTI)

We describe three-dimensional terminal toric flips. We obtain the complete local description of three-dimensional terminal toric flips.

Fujino, Osamu; Takano, Yukishige; Uehara, Hokuto

2008-01-01T23:59:59.000Z

343

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

E-Print Network (OSTI)

A first-of-its-kind Waste Heat Ammonia Absorption Refrigeration Plant (WHAARP™) was installed by Planetec Utility Services Co., Inc. in partnership with Energy Concepts Co. at Ultramar Diamond Shamrock's 30,000 barrel per day refinery in Denver, Colorado. The refrigeration unit is designed to provide refrigeration for two process units at the refinery while utilizing waste heat as the energy source. The added refrigeration capacity benefits the refinery by recovering salable products, debottlenecking process units, avoiding additional electrical demand, and reducing the refinery Energy Intensity Index. In addition, the WHAARP unit lowers air pollutant emissions by reducing excess fuel gas that is combusted in the refinery flare. A comprehensive utility and process efficiency Master Plan developed for the Denver refinery by Planetec provided the necessary platform for implementing this distinctive project. The $2.3 million WHAARP system was paid for in part by a $760,000 grant from the U.S. Department of Energy, as part of their "Industry of the Future Program". Total combined benefits are projected to be approximately $1 million/year with a 1.6 year simple payback including the grant funding.

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

1998-04-01T23:59:59.000Z

344

Refinery IGCC plants are exceeding 90% capacity factor after 3 years  

SciTech Connect

Steep learning curves for commercial IGCC plants in Italy show annual capacity factors of 55-60% in the first year of service and improvement to over 90% after the third year. The article reviews the success of three IGCC projects in Italy - those of ISAB Energy, Sarlux Saras and Api Energy. EniPower is commissioning a 250 MW IGCC plant that will burn syngas produced by gasification of residues at an adjacent Eni Sannazzaro refinery in north central Italy. The article lists 14 commercially operating IGCC plants worldwide that together provide close to 3900 MW of generating capacity. These use a variety of feedstock-coals, petroleum coke and refinery residues and biomass. Experience with commercial scale plants in Europe demonstrates that IGCC plants can operate at capacity factors comparable to if not better than conventional coal plants. 2 figs., 1 photo.

Jaeger, H.

2006-01-15T23:59:59.000Z

345

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 operations goes beyond energy conservation housekeeping measures and investments, and uses a comprehensive method to measure energy efficiency rather than energy consumption per barrel. It uses the Exxon Research and Engineering developed energy guideline factors, which are based on energy efficient designs and criteria, to (1) Evaluate the energy efficiency performance of refineries of different complexity in a consistent manner. (2) Compensate for changes in individual process unit throughputs and in unit operating intensity/severity. (3) Identify and quantify areas of energy inefficiency. (4) Regularly monitor and steward energy efficiency performance. Effective conservation also requires the analysis of energy performance and setting goals for future improvement. The paper explains how this can be done.

Libbers, D. D.

1980-01-01T23:59:59.000Z

346

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 leakage, corbel damage, flue gas obstruction and dirty tubes. Efficiency impact is greatest in the convection section since conventional repairs only permit accessing from the outside, thus only hot spots and some air leakage are repaired. Exxon USA's Baton Rouge refinery has adopted a restoration procedure, using the technique of ceramic fiber lined panels, which corrects all the problem areas and returns the heater to new condition. Restorations have been successfully completed on convection sections as well as total heaters. All restorations have been within a normal turnaround period. Efficiency increases greater than 3% have been realized, as well as improvements in the heater's operation.

Sento, H. D.

1981-01-01T23:59:59.000Z

347

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

Science Conference Proceedings (OSTI)

This report summarizes the accomplishments toward project goals during the first twelve 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

2004-09-17T23:59:59.000Z

348

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

Science Conference Proceedings (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

349

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

SciTech Connect

This report summarizes the accomplishments toward project goals during the first six months of the second year 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; Gareth Mitchell

2005-05-18T23:59:59.000Z

350

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

Science Conference Proceedings (OSTI)

This report summarizes the accomplishments toward project goals during the first six months of the second year 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. Evaluations to assess the quality of coal based fuel oil are reported. 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; Gareth Mitchell

2005-11-17T23:59:59.000Z

351

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

Science Conference Proceedings (OSTI)

This report summarizes the accomplishments toward project goals during the first six months of the third year 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. Characterization of the gasoline fuel indicates a dominance of single ring alkylcycloalkanes that have a low octane rating; however, blends containing these compounds do not have a negative effect upon gasoline when blended in refinery gasoline streams. Characterization of the diesel fuel indicates a dominance of 3-ring aromatics that have a low cetane value; however, these compounds do not have a negative effect upon diesel when blended in refinery diesel streams. 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. Combustion and characterization of fuel oil indicates that the fuel is somewhere in between a No. 4 and a No. 6 fuel oil. Emission testing indicates the fuel burns similarly to these two fuels, but trace metals for the coal-based material are different than petroleum-based fuel oils. Co-coking studies using cleaned coal are highly reproducible in the pilot-scale delayed coker. Evaluation of the coke by Alcoa, Inc. indicated that while the coke produced is of very good quality, the metals content of the carbon is still high in iron and silica. Coke is being evaluated for other possible uses. Methods to reduce metal content are being evaluated.

Caroline E. Burgess Clifford; Andre Boehman; Chunshan Song; Bruce Miller; Gareth Mitchell

2006-05-17T23:59:59.000Z

352

Who lives near coke plants and oil refineries An exploration of the environmental inequity hypothesis  

SciTech Connect

Facility-specific information on pollution was obtained for 36 coke plants and 46 oil refineries in the US and matched with information on populations surrounding these 82 facilities. These data were analyzed to determine whether environmental inequities were present, whether they were more economic or racial in nature, and whether the racial composition of nearby communities has changed significantly since plants began operations. The Census tracts near coke plants have a disproportionate share of poor and nonwhite residents. Multivariate analyses suggest that existing inequities are primarily economic in nature. The findings for oil refineries are not strongly supportive of the environmental inequity hypothesis. Rank ordering of facilities by race, poverty, and pollution produces limited (although not consistent) evidence that the more risky facilities tend to be operating in communities with above-median proportions of nonwhite residents (near coke plants) and Hispanic residents (near oil refineries). Over time, the radical makeup of many communities near facilities has changed significantly, particularly in the case of coke plants sited in the early 1900s. Further risk-oriented studies of multiple manufacturing facilities in various industrial sectors of the economy are recommended.

Graham, J.D.; Beaulieu, N.D.; Sussman, D.; Sadowitz, M.; Li, Y.C. (Harvard Center for Risk Analysis, Boston, MA (United States))

1999-04-01T23:59:59.000Z

353

The Use of Oil Refinery Wastes as a Dust Suppression Surfactant for Use in Mining  

Science Conference Proceedings (OSTI)

In this research, the suitability of a selection of petroleum refinery wastes as a dust suppressant were examined. Dust is a significant problem in surface and underground mining mainly because of its adverse effects on human health and machinery. Hence, dust control and suppression is a vital part of mine planning for mining engineers. Water is the oldest and the cheapest suppressant in dealing with the mine dusts. However, surfactant use has recently been used for a wider range of applications in the mining industry. In order to carry out laboratory experiments, a dust chamber was designed and manufactured. The chamber has an inlet for coal dust entrance and a nozzle for spraying water and the oil refinery wastes. Water and the surfactants were mixed at various ratios and then sprayed onto the coal dusts within the cell. Dust concentration was measured systematically to determine the effects of surfactant containing solution on the coal dust and the data obtained by the measurements were analyzed. The results showed that the oil refinery wastes could be used as a dust suppressant, which may create an economical utilization for the wastes concerned.

Dixon-Hardy, D.W.; Beyhan, S.; Ediz, I.G.; Erarslan, K. [University of Leeds, Leeds (United Kingdom)

2008-10-15T23:59:59.000Z

354

Production of ethanol from refinery waste gases. Phase 2, technology development, annual report  

DOE Green Energy (OSTI)

Oil refineries discharge large volumes of H{sub 2}, CO, and CO{sub 2} from cracking, coking, and hydrotreating operations. This program seeks to develop a biological process for converting these waste gases into ethanol, which can be blended with gasoline to reduce emissions. Production of ethanol from all 194 US refineries would save 450 billion BTU annually, would reduce crude oil imports by 110 million barrels/year and emissions by 19 million tons/year. Phase II efforts has yielded at least 3 cultures (Clostridium ljungdahlii, Isolate O-52, Isolate C-01) which are able to produce commercially viable concentrations of ethanol from CO, CO{sub 2}, and H{sub 2} in petroleum waste gas. Single continuous stirred tank reactor studies have shown that 15-20 g/L of ethanol can be produced, with less than 5 g/L acetic acid byproduct. Culture and reactor optimization in Phase III should yield even higher ethanol concentrations and minimal acetic acid. Product recovery studies showed that ethanol is best recovered in a multi-step process involving solvent extraction/distillation to azeotrope/azeotropic distillation or pervaporation, or direct distillation to the azeotrope/azeotropic distillation or pervaporation. Projections show that the ethanol facility for a typical refinery would require an investment of about $30 million, which would be returned in less than 2 years.

Arora, D.; Basu, R.; Phillips, J.R.; Wikstrom, C.V.; Clausen, E.C.; Gaddy, J.L.

1995-07-01T23:59:59.000Z

355

Potentials for Fuel Cells in Refineries and Chlor-Alkali Plants  

E-Print Network (OSTI)

The market potentials for fuel cell cogeneration systems in petroleum refineries and chlor-alkali plants were evaluated. Costs of the total energy consumed (power plus steam) were calculated and compared with those for more conventional cogeneration systems. Questionnaires were sent to major plants in both industries to determine technical requirements and data required for the assessment of the market potential. The most promising application appears to be in chlor-alkali plants where the production process is electricity intensive. Future anticipated changes in the production process are favorable to the use of fuel cells. The energy use in refineries is steam intensive with the required steam pressures ranging from approximately 15 to 650 psig. The near-term use of fuel cell cogeneration in refineries is not as attractive as in chlor-alkali plants. The phosphoric acid fuel cell is the most developed and the most cost competitive, but its use is limited by its being able to produce only low-pressure steam. Over the longer term, the molten carbonate and the solid oxide fuel cell, both of which operate at significantly higher temperatures, are technically very attractive. However, they do not appear to be cost competitive with conventional systems.

Altseimer, J. H.; Roach, F.

1986-06-01T23:59:59.000Z

356

Inorganic Nanocrystal Bulk Heterojunctions - Energy Innovation ...  

Schematic illustration of a nanocrystal bulk heterojunction solar cell with an active layer in which the concentration of n-type and p-type nanocrystals is graded ...

357

Mechanical Behavior of Bulk Nanocrystalline Copper Alloys ...  

Science Conference Proceedings (OSTI)

Presentation Title, Mechanical Behavior of Bulk Nanocrystalline Copper Alloys Produced by High Energy Ball Milling. Author(s), Hamed Bahmanpour, Khaled M.

358

Bulk Metallic Glasses VIII - Programmaster.org  

Science Conference Proceedings (OSTI)

Aug 2, 2010 ... Sponsorship, The Minerals, Metals and Materials Society .... The Oxidation Behavior of an FeCo-Based Bulk Metallic Glass at 600 - 700C.

359

Two terminal line voltage thermostat  

Science Conference Proceedings (OSTI)

A two terminal line voltage thermostat includes a switch which effectively connects line voltage to a heater load. The entire process is controlled by an integrated circuit microcontroller which is powered by a rectified voltage from a transformer secondary connected to a primary which is in series with the heater load. Backup battery power is provided to maintain limited functions of the microcontroller in the event of overall power loss. The microcontroller is programmed to meet the temperature sensing and control requirements specific to a two terminal electric baseboard heating installation. 7 figs.

Stalsberg, K.J.; Ingalls, J.E.; Hoglund, S.R.

1995-10-10T23:59:59.000Z

360

INTERNATIONAL CONSULTANTS REQUIRED FOR DEVELOPMENT OF COAL PORT/TERMINAL  

E-Print Network (OSTI)

PIDC intends to develop complete infrastructure facilities (Coal Port/Terminal) for the handling & transportation of imported coal at a greenfield site in the coastal area of Pakistan to facilitate setting up coal based industries in an adjoining industrial zone and supply to other users. International consultants, having experience and expertise of developing coal handling facilities of international standard for off-loading, storage and transportation of imported coal in bulk volume are invited to apply preferably in association with reputed local consultants for preparation of Feasibility Study of the project covering all relevant aspects including: 1. Market study to ascertain potential local demand for imported coal by power, cement and steel plants and other major users for the next 15 years. 2. Develop master plan and design of the infrastructure facilities (Coal Port/Terminal) for handling imported coal in bulk quantity at the location to be identified in the study. 3. Development of industrial zone for coal based industry. 4. Financial and technical aspects / viability of the project. 5. Implementation plan and strategy to develop and operate the project. Interested parties may collect the TOR for the feasibility study from the under mentioned office during working hours or download it from Ministry of Industries, Production & Special Initiatives, Government of Pakistan’s web site www.moip.gov.pk. Detailed proposal for carrying out the feasibility study alongwith financial bid and the background information of the consultants, should be submitted latest by May 17, 2007 at the address given below. PIDC

For Imported; Coal In Pakistan

2007-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Bulk heating cleans paraffinic bottoms from crude tanks  

SciTech Connect

It is often challenging to remove from service crude oil tanks that have been in use for many years. Bulk heating, as opposed to localized heating, has been used to successfully liquefy heavy paraffinic or asphaltic bases in crude oil tanks. The process provides economical product recovery, while minimizing waste production and reducing human exposure to hazardous working conditions. Statia Terminals Point Tupper Inc., Point Tupper, N.S., used bulk heating to remove 2 ft of weathered, paraffinic tank bottoms from six 450,000 bbl tanks that held Cabinda crude from West Africa. Immersion tube heaters were installed through the tank manholes and a diluent was added. Two 10-million BTU/hr propane burners supplied heat, and tank mixers operated continuously to aid in heat transfer. The tank contents were heated to 135 F and the temperature was held constant for 3 days. The resulting hot liquid was a pumpable and recoverable product. About 10 days were required to clean each tank. The paper describes the heating and cleaning operation as well as the economics of the Statia project.

Badrock, J. (Cooperheat Inc., Houston, TX (United States)); Coutu, R. (Cooperheat Inc., Mississauga, Ontario (Canada)); Johnson, N. (Statia Terminals N.V. St. Eustatius (Netherlands)); Martin, A. (Chicago Bridge and Iron Co., Oak Brook, IL (United States))

1995-02-20T23:59:59.000Z

362

Bulk Higgs with 4D Gauge Interactions  

E-Print Network (OSTI)

We consider a model with an extra compact dimension in which the Higgs is a bulk field while all other Standard Model fields are confined on a brane. We find that four-dimensional gauge invariance can still be achieved by appropriate modification of the brane action. This changes accordingly the Higgs propagator so that, the Higgs, in all its interactions with Standard Model fields, behaves as an ordinary 4D field, although it has a bulk kinetic term and bulk self-interactions. In addition, it cannot propagate from the brane to the bulk and, thus, no charge can escape into the bulk but it remains confined on the brane. Moreover, the photon remains massless, while the dependence of the Higgs vacuum on the extra dimension induces a mixing between the graviphoton and the Z-boson. This results in a modification of the sensitive \\rho-parameter.

Alex Kehagias; Kyriakos Tamvakis

2005-07-14T23:59:59.000Z

363

Bulk viscosity of N=2* plasma  

E-Print Network (OSTI)

We use gauge theory/string theory correspondence to study the bulk viscosity of strongly coupled, mass deformed SU(N_c) N=4 supersymmetric Yang-Mills plasma, also known as N=2^* gauge theory. For a wide range of masses we confirm the bulk viscosity bound proposed in arXiv:0708.3459. For a certain choice of masses, the theory undergoes a phase transition with divergent specific heat c_V ~ |1-T_c/T|^(-1/2). We show that, although bulk viscosity rapidly grows as T -> T_c, it remains finite in the vicinity of the critical point.

Alex Buchel; Chris Pagnutti

2008-12-18T23:59:59.000Z

364

The Bulk Viscosity of a Pion Gas  

E-Print Network (OSTI)

We compute the bulk viscosity of a gas of pions at temperatures below the QCD crossover temperature, for the physical value of pion mass, to lowest order in chiral perturbation theory. Bulk viscosity is controlled by number-changing processes which become exponentially slow at low temperatures when the pions become exponentially dilute, leading to an exponentially large bulk viscosity zeta ~ (F_0^8/m_\\pi^5) exp(2m_\\pi/T), where F_0 = 93 MeV is the pion decay constant.

Egang Lu; Guy D. Moore

2011-01-31T23:59:59.000Z

365

DOE Terminated Federal Advisory Committees  

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

TERMINATED FEDERAL ADVISORY COMMITTEES Date Committee Name/Web Site Terminated Federal Energy Management Advisory Committee 06/08/07 Web Site: (Environmental Management Site-Specific Advisory Board) Fernald 09/30/06 Web Site: (Environmental Management Site-Specific Advisory Board) Rocky Flats 09/30/06 Web Site: Secretary of Energy Advisory Board 05/20/06 Web Site: http://www.seab.energy.gov/ Electricity Advisory Board 02/10/06 Web Site: http://www.eab.doe.gov/ American Statistical Association Advisory Committee on Energy Statistics 03/24/05 Web Site: Workers' Compensation Assistance Advisory Committee 06/29/04 Web Site: National Nuclear Security Administration Advisory Committee 06/25/03 Web Site: Commission on Fire Safety and Preparedness 01/09/03

366

Standard practice for evaluating and qualifying oil field and refinery corrosion inhibitors using rotating cage  

E-Print Network (OSTI)

1.1 This practice covers a generally accepted procedure to use the rotating cage (RC) for evaluating corrosion inhibitors for oil field and refinery applications. 1.2 The values stated in SI units are to be regarded as the standard. The values given in parentheses are for information only. 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 limitations prior to use.

American Society for Testing and Materials. Philadelphia

2006-01-01T23:59:59.000Z

367

Simulation analysis of marine terminal investments  

Science Conference Proceedings (OSTI)

A common problem in the oil industry is the optimization of terminal facilities to minimize delays in servicing incoming tankers. In Exxon Corporation, simulation has been successfully applied to marine terminal studies since the early nineteen sixties. ...

David W. Graff

1973-01-01T23:59:59.000Z

368

Definition: Bulk Electric System | Open Energy Information  

Open Energy Info (EERE)

Bulk Electric System Bulk Electric System Jump to: navigation, search Dictionary.png Bulk Electric System As defined by the Regional Reliability Organization, the electrical generation resources, transmission lines, interconnections with neighboring systems, and associated equipment, generally operated at voltages of 100 kV or higher. Radial transmission facilities serving only load with one transmission source are generally not included in this definition.[1] Related Terms Regional Reliability Organization, transmission lines, transmission line References ↑ Glossary of Terms Used in Reliability Standards An in LikeLike UnlikeLike You like this.Sign Up to see what your friends like. line Glossary Definition Retrieved from "http://en.openei.org/w/index.php?title=Definition:Bulk_Electric_System&oldid=48030

369

INVESTIGATION OF BULK POWER ERCOT (Texas)  

E-Print Network (OSTI)

INVESTIGATION OF BULK POWER MARKETS ERCOT (Texas) November 1, 2000 The analyses and conclusions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-2 A. Electric Reliability Council of Texas (ERCOT) . . . . . . . . . . . . . . . . . . . . . . . . 4-2 B. The 1995 Texas Electricity Restructuring Statute

Laughlin, Robert B.

370

Sulfur recovery in U.S. refineries is at an all-time high  

SciTech Connect

Environmental pressures are reducing allowable sulfur emissions and tightening fuel sulfur specifications on a global basis. Combined with an increasingly sour crude slate, this means that ever-greater quantities of sulfur are recovered each year. Sulfur is produced through three main routes: Frasch mining, recovery from pyrites, and recovery from crude oil and natural gas. Sulfur recovery from US refineries reached an all-time high in 1995: 13,753 metric tons/calendar day (mt/cd). Frasch mining has lost its place as the primary source of elemental sulfur. Current demand patterns for sulfur are expected to continue through the next decade. About half of world sulfur production will be used to produce phosphatic fertilizers. The other half will be used in some 30 chemically oriented industries. The data reported in this article were collected by the US Bureau of Mines/US Geological Survey, unless otherwise noted. The paper discusses sulfur from natural gas, sulfur from refineries, sulfur prices, imports and exports.

Swain, E.J. [Swain (Edward J.), Houston, TX (United States)

1997-04-21T23:59:59.000Z

371

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

Science Conference Proceedings (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 (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

372

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

E-Print Network (OSTI)

The design of a low temperature Rankine cycle system using R-113 working fluid for recovery and conversion of process waste heat is described for typical applications in oil refineries and chemical plants. The system is designed to produce electric power from waste heat available in a temperature range from 180oF to 400oF. The design of a new ORC turbo generator uniquely adapted to applications of this type is presented. The unit has been designed for power outputs from 3/4 to 2 1/2 MW and turbine inlet temperatures from 170 to 260oF. The machine design has eliminated the need for shaft seals, shaft couplings and the usual lube oil console normally required for turbine-generator units. Results of prototype tests of a 1 MW unit are presented. 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 and waste heat streams from 20 to 130 million BTU/hr.

Meacher, J. S.

1981-01-01T23:59:59.000Z

373

Complete LNG Terminal Status Maps | Department of Energy  

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

LNG Terminal Status Maps Complete LNG Terminal Status Maps A series of slides showing the status of various LNG terminals (existing, under construction, proposed, etc.) in North...

374

Photovoltaic module electrical termination design requirement study  

DOE Green Energy (OSTI)

Motorola Inc., in conjunction with ITT Cannon, has conducted a study to develop information to facilitate the selection of existing, commercial, electrical termination hardware for photovoltaic modules and arrays. This volume of the report contains the executive summary. Module and array design parameters were investigated and recommendations were developed for use in surveying, evaluating, and comparing electrical termination hardware. Electrical termination selection criteria factors were developed and applied to nine generic termination types in each of the four application sectors: remote, residential, intermediate and industrial. Existing terminations best suited for photovoltaic modules and arrays were identified. Cost information was developed to identify cost drivers and/or requirements which might lead to cost reductions. The general conclusion is that there is no single generic termination that is best suited for photovoltaic application, but that the appropriate termination is strongly dependent upon the module construction and its support structure as well as the specific application sector.

Mosna, F.J. Jr.; Donlinger, J.

1980-07-01T23:59:59.000Z

375

Use of various acute, sublethal and early life-stage tests to evaluate the toxicity of refinery effluents  

Science Conference Proceedings (OSTI)

The toxicities of effluents from three Ontario, Canada, refineries were assessed with microbes, plants, invertebrates, and fish. Acute toxicity was assessed by the Microtox test, an assay based on electron transport activity in submitochondrial particles, and Daphnia magna (water flea); growth of Selenastrum capricornutum (alga); growth of Lemna minor (aquatic plant); germination of Lactuca sativa (nonaquatic plant); survival, growth, and maturation of Panagrellus redivivus (nematode); and genotoxicity in the SOS-Chromotest. Only the Microtox test and the submitochondrial particle test detected acute toxicity in the effluent samples. Reduced survival and sublethal responses were caused by some effluents, but not all effluents were toxic, and none caused a response in all of the tests applied. The results suggest that the effluent treatment systems used at Ontario refineries have largely eliminated acute toxicity to the organisms in their test battery. Although reduced survival and sublethal effects were detected in some of the effluents, the effects were minor. Some of the tests provided evidence, albeit weak, of variations in the responses of the test organisms to a temporal series of effluent samples. Not unexpectedly, there were also minor differences in the responses of the tests to effluents from the three refineries. The fathead minnow test seems to be a sensitive indicator of the sublethal toxicity of Ontario refinery effluents.

Sherry, J.; Scott, B.; Dutka, B. [National Water Research Inst., Burlington, Ontario (Canada)

1997-11-01T23:59:59.000Z

376

Micro benchtop optics by bulk silicon micromachining  

DOE Patents (OSTI)

Micromachining of bulk silicon utilizing the parallel etching characteristics of bulk silicon and integrating the parallel etch planes of silicon with silicon wafer bonding and impurity doping, enables the fabrication of on-chip optics with in situ aligned etched grooves for optical fibers, micro-lenses, photodiodes, and laser diodes. Other optical components that can be microfabricated and integrated include semi-transparent beam splitters, micro-optical scanners, pinholes, optical gratings, micro-optical filters, etc. Micromachining of bulk silicon utilizing the parallel etching characteristics thereof can be utilized to develop miniaturization of bio-instrumentation such as wavelength monitoring by fluorescence spectrometers, and other miniaturized optical systems such as Fabry-Perot interferometry for filtering of wavelengths, tunable cavity lasers, micro-holography modules, and wavelength splitters for optical communication systems.

Lee, Abraham P. (Walnut Creek, CA); Pocha, Michael D. (Livermore, CA); McConaghy, Charles F. (Livermore, CA); Deri, Robert J. (Pleasanton, CA)

2000-01-01T23:59:59.000Z

377

Two terminal micropower radar sensor  

DOE Patents (OSTI)

A simple, low power ultra-wideband radar motion sensor/switch configuration connects a power source and load to ground. The switch is connected to and controlled by the signal output of a radar motion sensor. The power input of the motion sensor is connected to the load through a diode which conducts power to the motion sensor when the switch is open. A storage capacitor or rechargeable battery is connected to the power input of the motion sensor. The storage capacitor or battery is charged when the switch is open and powers the motion sensor when the switch is closed. The motion sensor and switch are connected between the same two terminals between the source/load and ground. 3 figs.

McEwan, T.E.

1995-11-07T23:59:59.000Z

378

Two terminal micropower radar sensor  

SciTech Connect

A simple, low power ultra-wideband radar motion sensor/switch configuration connects a power source and load to ground. The switch is connected to and controlled by the signal output of a radar motion sensor. The power input of the motion sensor is connected to the load through a diode which conducts power to the motion sensor when the switch is open. A storage capacitor or rechargeable battery is connected to the power input of the motion sensor. The storage capacitor or battery is charged when the switch is open and powers the motion sensor when the switch is closed. The motion sensor and switch are connected between the same two terminals between the source/load and ground.

McEwan, Thomas E. (Livermore, CA)

1995-01-01T23:59:59.000Z

379

Plaquemines parish Deep Draft top-off terminal  

SciTech Connect

The recently completed ''Deep River Study, Lower Mississippi River'' sponsored by the ''Governor's Task Force on Deep-Draft Vessel Access to the Lower Mississippi River'' contained the following recommended program: Dredge the present 40 foot deep channel to 45 feet initially from the Gulf via Southwest Pass to Mile 172 AHP to provide for two-way navigation of the deep draft vessels that would serve the forecasted most likely level of waterborne commerce (Alternative 9). Plan and seek authorization to further deepen the channel in stages to 55 feet in the future should actual increases in commerce equal the high level level of commerce (Alternative 11). Put into operation, as soon as possible, facilities for loading and topping-off grain ships midstream and topping-off coal carriers in the Gulf in order to attract and establish patterns of trade in large ships. The South Pass Bulk Terminal is a project that responds to the last section of this three-part recommendation. It was conceived as a means of providing the Gulf Coast region with low cost and efficient access to the economics of scale offered by using deep-draft vessels for ocean transport of dry bulk commodities. The proposed facility seeks to combine the advantages of a deep-draft port with those typical of a topping-off operation. It is intended as an interim measure that will serve to maintain and attract trade until such time as the river is dredged.

Nelson, C.; Morehiser, M.

1983-11-01T23:59:59.000Z

380

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

Note: This page contains sample records for the topic "refinery bulk terminal" 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

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

382

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

Reports and Publications (EIA)

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 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 U.S. 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.

Information Center

1998-01-02T23:59:59.000Z

383

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

SciTech Connect

This report summarizes the accomplishments toward project goals during the second six months of the third year 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 and examination of carbon material, the use of a research gasoline engine to test coal-based gasoline, and modification of diesel engines for use in evaluating diesel produced in the project. At the pilot scale, the hydrotreating process was modified to separate the heavy components from the LCO and RCO fractions before hydrotreating in order to improve the performance of the catalysts in further processing. Characterization of the gasoline fuel indicates a dominance of single ring alkylcycloalkanes that have a low octane rating; however, blends containing these compounds do not have a negative effect upon gasoline when blended in refinery gasoline streams. Characterization of the diesel fuel indicates a dominance of 3-ring aromatics that have a low cetane value; however, these compounds do not have a negative effect upon diesel when blended in refinery diesel streams. Both gasoline and diesel continue to be tested for combustion performance. 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. Activated carbons have proven useful to remove the heavy sulfur components, and unsupported Ni/Mo and Ni/Co catalysts have been very effective for hydrodesulfurization. Equipment is now in place to begin fuel oil evaluations to assess the quality of coal based fuel oil. Combustion and characterization of the latest fuel oil (the high temperature fraction of RCO from the latest modification) indicates that the fraction is heavier than a No. 6 fuel oil. Combustion efficiency on our research boiler is {approx}63% for the heavy RCO fraction, lower than the combustion performance for previous co-coking fuel oils and No. 6 fuel oil. An additional coal has been procured and is being processed for the next series of delayed co-coking runs. Work continues on characterization of liquids and solids from co-coking of hydrotreated decant oils; liquid yields include more saturated and hydro- aromatics, while the coke quality varies depending on the conditions used. Pitch material is being generated from the heavy fraction of co-coking. Investigation of coal extraction as a method to produce RCO continues; the reactor modifications to filter the products hot and to do multi-stage extraction improve extraction yields from {approx}50 % to {approx}70%. Carbon characterization of co-cokes for use as various carbon artifacts continues.

Caroline E. Burgess Clifford; Andre' Boehman; Chunshan Song; Bruce Miller; Gareth Mitchell

2006-09-17T23:59:59.000Z

384

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

Science Conference Proceedings (OSTI)

This report summarizes the accomplishments toward project goals during the no cost extension period of the third year 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 for a third round of testing, the use of a research gasoline engine to test coal-based gasoline, and modification of diesel engines for use in evaluating diesel produced in the project. At the pilot scale, the hydrotreating process was modified to separate the heavy components from the LCO and RCO fractions before hydrotreating in order to improve the performance of the catalysts in further processing. Hydrotreating and hydrogenation of the product has been completed, and due to removal of material before processing, yield of the jet fuel fraction has decreased relative to an increase in the gasoline fraction. Characterization of the gasoline fuel indicates a dominance of single ring alkylcycloalkanes that have a low octane rating; however, blends containing these compounds do not have a negative effect upon gasoline when blended in refinery gasoline streams. Characterization of the diesel fuel indicates a dominance of 3-ring aromatics that have a low cetane value; however, these compounds do not have a negative effect upon diesel when blended in refinery diesel streams. Both gasoline and diesel continue to be tested for combustion performance. 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. Activated carbons have proven useful to remove the heavy sulfur components, and unsupported Ni/Mo and Ni/Co catalysts have been very effective for hydrodesulfurization. Equipment is now in place to begin fuel oil evaluations to assess the quality of coal based fuel oil. Combustion and characterization of the latest fuel oil (the high temperature fraction of RCO from the latest modification) indicates that the fraction is heavier than a No. 6 fuel oil. Combustion efficiency on our research boiler is {approx}63% for the heavy RCO fraction, lower than the combustion performance for previous co-coking fuel oils and No. 6 fuel oil. Emission testing indicates that the coal derived material has more trace metals related to coal than petroleum, as seen in previous runs. An additional coal has been procured and is being processed for the next series of delayed co-coking runs. The co-coking of the runs with the new coal have begun, with the coke yield similar to previous runs, but the gas yield is lower and the liquid yield is higher. Characterization of the products continues. Work continues on characterization of liquids and solids from co-coking of hydrotreated decant oils; liquid yields include more saturated and hydro- aromatics, while the coke quality varies depending on the conditions used. Pitch material is being generated from the heavy fraction of co-coking.

Caroline E. Burgess Clifford; Andre Boehman; Chunshan Song; Bruce Miller; Gareth Mitchell

2007-03-17T23:59:59.000Z

385

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

386

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

SciTech Connect

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

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

1995-09-01T23:59:59.000Z

387

Lifecycle Analysis of Air Quality Impacts of Hydrogen and Gasoline Transportation Fuel Pathways  

E-Print Network (OSTI)

Tanker delivery Oil refinery Pipeline Storage TruckTanker delivery Oil refinery Pipeline Terminal storage Truckoil extraction sites and refineries are so far away from

Wang, Guihua

2008-01-01T23:59:59.000Z

388

Bulk materials storage handling and transportation  

Science Conference Proceedings (OSTI)

This book contains papers on bulk materials storage, handling, and transportation. Topic areas covered include: mechanical handling; pneumatic conveying; transportation; freight pipeliners; storage and discharge systems; integrated handling systems; automation; environment and sampling; feeders and flow control; structural design; large mobile machines; and grain handling.

Not Available

1983-01-01T23:59:59.000Z

389

Refinery Integration of By-Products from Coal-Derived Jet Fuels  

SciTech Connect

The final report summarizes the accomplishments toward project goals during length of the project. The goal of this project was to integrate coal into a refinery in order to produce coal-based jet fuel, with the major goal to examine the products other than jet fuel. 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. The main goal of Task 1 was the production of coal-based jet fuel and other products that would need to be utilized in other fuels or for non-fuel sources, using known refining technology. The gasoline, diesel fuel, and fuel oil were tested in other aspects of the project. Light cycle oil (LCO) and refined chemical oil (RCO) were blended, hydrotreated to removed sulfur, and hydrogenated, then fractionated in the original production of jet fuel. Two main approaches, taken during the project period, varied where the fractionation took place, in order to preserve the life of catalysts used, which includes (1) fractionation of the hydrotreated blend to remove sulfur and nitrogen, followed by a hydrogenation step of the lighter fraction, and (2) fractionation of the LCO and RCO before any hydrotreatment. Task 2 involved assessment of the impact of refinery integration of JP-900 production on gasoline and diesel fuel. Fuel properties, ignition characteristics and engine combustion of model fuels and fuel samples from pilot-scale production runs were characterized. The model fuels used to represent the coal-based fuel streams were blended into full-boiling range fuels to simulate the mixing of fuel streams within the refinery to create potential 'finished' fuels. The representative compounds of the coal-based gasoline were cyclohexane and methyl cyclohexane, and for the coal-base diesel fuel they were fluorine and phenanthrene. Both the octane number (ON) of the coal-based gasoline and the cetane number (CN) of the coal-based diesel were low, relative to commercial fuels ({approx}60 ON for coal-based gasoline and {approx}20 CN for coal-based diesel fuel). Therefore, the allowable range of blending levels was studied where the blend would achieve acceptable performance. However, in both cases of the coal-based fuels, their ignition characteristics may make them ideal fuels for advanced combustion strategies where lower ON and CN are desirable. Task 3 was designed to develop new approaches for producing ultra clean fuels and value-added chemicals from refinery streams involving coal as a part of the feedstock. It consisted of the following three parts: (1) desulfurization and denitrogenation which involves both new adsorption approach for selective removal of nitrogen and sulfur and new catalysts for more effective hydrotreating and the combination of adsorption denitrogenation with hydrodesulfurization; (2) saturation of two-ring aromatics that included new design of sulfur resistant noble-metal catalysts for hydrogenation of naphthalene and tetralin in middle distillate fuels, and (3) value-added chemicals from naphthalene and biphenyl, which aimed at developing value-added organic chemicals from refinery streams such as 2,6-dimethylnaphthalene and 4,4{prime}-dimethylbiphenyl as precursors to advanced polymer materials. Major advances were achieved in this project in designing the catalysts and sorbent materials, and in developing fundamental understanding. The objective of Task 4 was to evaluate the effect of introducing coal into an existing petroleum refinery on the fuel oil product, specifically trace element emissions. Activities performed to accomplish this objective included analyzing two petroleum-based commercial heavy fuel oils (i.e., No. 6 fuel oils) as baseline fuels and three co-processed fuel oils, characterizing the atomization performance of a No. 6 fuel oil, measuring the combustion performance and emissions of the five fuels, specifically major, minor, and trace elements when fired in a watertube boiler designed for natural gas/fuel oil, and determining the boiler performance when firing the five fuels. Two

Caroline Clifford; Andre Boehman; Chunshan Song; Bruce Miller; Gareth Mitchell

2008-03-31T23:59:59.000Z

390

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

391

Termination in language-based systems  

Science Conference Proceedings (OSTI)

Language run-time systems are increasingly being embedded in systems to support run-time extensibility via mobile code. Such systems raise a number of concerns when the code running in such systems is potentially buggy or untrusted. Although sophisticated access ... Keywords: Applets, Internet, Java, resource control, soft termination, termination

Algis Rudys; Dan S. Wallach

2002-05-01T23:59:59.000Z

392

Bulk viscosity in quasi particle models  

E-Print Network (OSTI)

We discuss transport properties of dynamical fluid composed of quasi-particles whose masses depend on temperature and charge chemical potentials. Based on the relativistic kinetic theory formulated under the relaxation time approximation, we derive a general expression for the bulk viscosity in the quasi-particle medium. We show that dynamically generated particle masses imply an essential modification of the fluid compressibility. As an application of our results we consider a class of quasi-particle models with the chiral phase transition belonging to O(4) and Z(2) universality class. Based on the Ginzburg-Landau and the scaling theory we study the critical properties of the bulk viscosity zeta near the phase transition. We show that under the relaxation time approximation the zeta is not expected to show singular behavior near the O(4) and Z(2) critical point through static critical exponents.

Sasaki, C

2008-01-01T23:59:59.000Z

393

Bulk viscosity in quasi particle models  

E-Print Network (OSTI)

We discuss transport properties of dynamical fluid composed of quasi-particles whose masses depend on temperature and charge chemical potentials. Based on the relativistic kinetic theory formulated under the relaxation time approximation, we derive a general expression for the bulk viscosity in the quasi-particle medium. We show that dynamically generated particle masses imply an essential modification of the fluid compressibility. As an application of our results we consider a class of quasi-particle models with the chiral phase transition belonging to O(4) and Z(2) universality class. Based on the Ginzburg-Landau and the scaling theory we study the critical properties of the bulk viscosity zeta near the phase transition. We show that under the relaxation time approximation the zeta is not expected to show singular behavior near the O(4) and Z(2) critical point through static critical exponents.

C. Sasaki; K. Redlich

2008-06-29T23:59:59.000Z

394

Isotopically engineered semiconductors: from the bulk tonanostructures  

SciTech Connect

Research performed with semiconductors with controlled isotopic composition is evolving from the measurement of fundamental properties in the bulk to those measured in superlattices and nanostructures. This is driven in part by interests associated with the fields of 'spintronics' and quantum computing. In this topical review, which is dedicated to Prof. Abstreiter, we introduce the subject by reviewing classic and recent measurements of phonon frequencies, thermal conductivity, bandgap renormalizations, and spin coherence lifetimes in isotopically controlled bulk group IV semiconductors. Next, we review phonon properties measured in isotope heterostructures, including pioneering work made possible by superlattices grown by the group of Prof. Abstreiter. We close the review with an outlook on the exciting future possibilities offered through isotope control in 1, 2, and 3 dimensions that will be possible due to advances in nanoscience.

Ager III, Joel W.; Haller, Eugene E.

2006-04-07T23:59:59.000Z

395

Hydrogen isotope separation utilizing bulk getters  

DOE Patents (OSTI)

Tritium and deuterium are separated from a gaseous mixture thereof, derived from a nuclear fusion reactor or some other source, by providing a casing with a bulk getter therein for absorbing the gaseous mixture to produce an initial loading of the getter, partially desorbing the getter to produce a desorbed mixture which is tritium-enriched, pumping the desorbed mixture into a separate container, the remaining gaseous loading in the getter being deuterium-enriched, desorbing the getter to a substantially greater extent to produce a deuterium-enriched gaseous mixture, and removing the deuterium-enriched mixture into another container. The bulk getter may comprise a zirconium-aluminum alloy, or a zirconium-vanadium-iron alloy. The partial desorption may reduce the loading by approximately fifty percent. The basic procedure may be extended to produce a multistage isotope separator, including at least one additional bulk getter into which the tritium-enriched mixture is absorbed. The second getter is then partially desorbed to produce a desorbed mixture which is further tritium-enriched. The last-mentioned mixture is then removed from the container for the second getter, which is then desorbed to a substantially greater extent to produce a desorbed mixture which is deuterium-enriched. The last-mentioned mixture is then removed so that the cycle can be continued and repeated. The method of isotope separation is also applicable to other hydrogen isotopes, in that the method can be employed for separating either deuterium or tritium from normal hydrogen.

Knize, Randall J. (Los Angeles, CA); Cecchi, Joseph L. (Lawrenceville, NJ)

1991-01-01T23:59:59.000Z

396

Hydrogen isotope separation utilizing bulk getters  

DOE Patents (OSTI)

Tritium and deuterium are separated from a gaseous mixture thereof, derived from a nuclear fusion reactor or some other source, by providing a casing with a bulk getter therein for absorbing the gaseous mixture to produce an initial loading of the getter, partially desorbing the getter to produce a desorbed mixture which is tritium-enriched, pumping the desorbed mixture into a separate container, the remaining gaseous loading in the getter being deuterium-enriched, desorbing the getter to a substantially greater extent to produce a deuterium-enriched gaseous mixture, and removing the deuterium-enriched mixture into another container. The bulk getter may comprise a zirconium-aluminum alloy, or a zirconium-vanadium-iron alloy. The partial desorption may reduce the loading by approximately fifty percent. The basic procedure may be extended to produce a multistage isotope separator, including at least one additional bulk getter into which the tritium-enriched mixture is absorbed. The second getter is then partially desorbed to produce a desorbed mixture which is further tritium-enriched. The last-mentioned mixture is then removed from the container for the second getter, which is then desorbed to a substantially greater extent to produce a desorbed mixture which is deuterium-enriched. The last-mentioned mixture is then removed so that the cycle can be continued and repeated. The method of isotope separation is also applicable to other hydrogen isotopes, in that the method can be employed for separating either deuterium or tritium from normal hydrogen.

Knize, Randall J. (Los Angeles, CA); Cecchi, Joseph L. (Lawrenceville, NJ)

1990-01-01T23:59:59.000Z

397

Hydrogen isotope separation utilizing bulk getters  

DOE Patents (OSTI)

Tritium and deuterium are separated from a gaseous mixture thereof, derived from a nuclear fusion reactor or some other source, by providing a casing with a bulk getter therein for absorbing the gaseous mixture to produce an initial loading of the getter, partially desorbing the getter to produce a desorbed mixture which is tritium-enriched, pumping the desorbed mixture into a separate container, the remaining gaseous loading in the getter being deuterium-enriched, desorbing the getter to a substantially greater extent to produce a deuterium-enriched gaseous mixture, and removing the deuterium-enriched mixture into another container. The bulk getter may comprise a zirconium-aluminum alloy, or a zirconium-vanadium-iron alloy. The partial desorption may reduce the loading by approximately fifty percent. The basic procedure may be extended to produce a multistage isotope separator, including at least one additional bulk getter into which the tritium-enriched mixture is absorbed. The second getter is then partially desorbed to produce a desorbed mixture which is further tritium-enriched. The last-mentioned mixture is then removed from the container for the second getter, which is then desorbed to a substantially greater extent to produce a desorbed mixture which is deuterium-enriched. The last-mentioned mixture is then removed so that the cycle can be continued and repeated. The method of isotope separation is also applicable to other hydrogen isotopes, in that the method can be employed for separating either deuterium or tritium from normal hydrogen. 4 figures.

Knize, R.J.; Cecchi, J.L.

1991-08-20T23:59:59.000Z

398

Carbon Capture and Sequestration from a Hydrogen Production Facility in an Oil Refinery  

SciTech Connect

The project proposed a commercial demonstration of advanced technologies that would capture and sequester CO2 emissions from an existing hydrogen production facility in an oil refinery into underground formations in combination with Enhanced Oil Recovery (EOR). The project is led by Praxair, Inc., with other project participants: BP Products North America Inc., Denbury Onshore, LLC (Denbury), and Gulf Coast Carbon Center (GCCC) at the Bureau of Economic Geology of The University of Texas at Austin. The project is located at the BP Refinery at Texas City, Texas. Praxair owns and operates a large hydrogen production facility within the refinery. As part of the project, Praxair would construct a CO2 capture and compression facility. The project aimed at demonstrating a novel vacuum pressure swing adsorption (VPSA) based technology to remove CO2 from the Steam Methane Reformers (SMR) process gas. The captured CO2 would be purified using refrigerated partial condensation separation (i.e., cold box). Denbury would purchase the CO2 from the project and inject the CO2 as part of its independent commercial EOR projects. The Gulf Coast Carbon Center at the Bureau of Economic Geology, a unit of University of Texas at Austin, would manage the research monitoring, verification and accounting (MVA) project for the sequestered CO2, in conjunction with Denbury. The sequestration and associated MVA activities would be carried out in the Hastings field at Brazoria County, TX. The project would exceed DOE?s target of capturing one million tons of CO2 per year (MTPY) by 2015. Phase 1 of the project (Project Definition) is being completed. The key objective of Phase 1 is to define the project in sufficient detail to enable an economic decision with regard to proceeding with Phase 2. This topical report summarizes the administrative, programmatic and technical accomplishments completed in Phase 1 of the project. It describes the work relative to project technical and design activities (associated with CO2 capture technologies and geologic sequestration MVA), and Environmental Information Volume. Specific accomplishments of this Phase include: 1. Finalization of the Project Management Plan 2. Development of engineering designs in sufficient detail for defining project performance and costs 3. Preparation of Environmental Information Volume 4. Completion of Hazard Identification Studies 5. Completion of control cost estimates and preparation of business plan During the Phase 1 detailed cost estimate, project costs increased substantially from the previous estimate. Furthermore, the detailed risk assessment identified integration risks associated with potentially impacting the steam methane reformer operation. While the Phase 1 work identified ways to mitigate these integration risks satisfactorily from an operational perspective, the associated costs and potential schedule impacts contributed to the decision not to proceed to Phase 2. We have concluded that the project costs and integration risks at Texas City are not commensurate with the potential benefits of the project at this time.

Engels, Cheryl; Williams, Bryan, Valluri, Kiranmal; Watwe, Ramchandra; Kumar, Ravi; Mehlman, Stewart

2010-06-21T23:59:59.000Z

399

Production of ethanol from refinery waste gases. Phase 3. Engineering development. Annual report, April 1, 1995--May 15, 1996  

DOE Green Energy (OSTI)

Refineries discharge large volumes of H2, CO, and CO 2 from cracking, coking, and hydrotreating operations. This R&D program seeks to develop, demonstrate, and commercialize a biological process for converting these waste gases into ethanol for blending with gasoline. A 200,000 BPD refinery could produce up to 38 million gallons ethanol per year. The program is being conducted in 3 phases: II, technology development; III, engineering development; and IV, demonstration. Phase I, exploratory development, has been completed. The research effort has yielded two strains (Isolates O-52 and C-01) which are to be used in the pilot studies to produce ethanol from CO, CO2, and H2 in petroleum waste gas. Results from single continuous stirred tank reactor (CSTR) laboratory tests have shown that 20-25 g/L ethanol can be produced with < 5 g/L acetic acid byproduct. Laboratory studies with two CSTRs in series have yielded ethanol concentrations of 30-35 g/L with 2-4 g/L acetic acid byproduct. Water recycle from distillation back to the fermenter shows that filtration of the water before distillation eliminates the recycle of toxic materials back to the fermenter. Product recovery in the process will use direct distillation to the azeotrope, followed by adsorption to produce neat ethanol. This is less energy intensive than e.g. solvent extraction, azeotropic distillation, or pervaporation. Economic projections are quite attractive; the economics are refinery stream dependent and thus vary depending on refinery location and operation.

Arora, D.; Basu, R.; Phillips, J.R.; Wikstrom, C.V.; Clausen, E.C; Gaddy, J.L.

1996-11-01T23:59:59.000Z

400

The potential application of fuel cell cogeneration systems in petroleum refineries. [Phosphoric acid, molten carbonate and solid oxide fuel cells  

Science Conference Proceedings (OSTI)

The market potential for fuel cell cogeneration systems within the petroleum refinery industry is evaluated. Phosphoric acid (PAFC), molten carbonate (MCFC), and solid oxide (SOFC) fuel cells were considered. Conventional competitive systems now available including purchased power plus boiler-generated steam, gas turbine combined cycle, and a relatively new coke fluidized bed-boiler were characterized. Refineries use large quantities of steam at pressures ranging from about 15 to 650 psig. PAFCs can only meet a limited number of steam requirements because of their relatively low operating temperature. The high temperature MCFC and SOFC are technically much more attractive for this application. However, current estimates of their capital costs are too large to make the technologies competitive. The capital costs of MCFCs and SOFCs would have to decrease approx.50% from their present estimated $1300/kWe. If costs could be decreased to give a 10% energy cost advantage to fuel cells, the industry projects that fuel cells might supply about 300 MWe by the year 2000, and modules in the 5- to 20-MWe size would be of interest. The market opportunities in refineries are varied - the industry is large, each plant is unique, thermal energy consumption is large, and both domestic and international competitiveness is intense. 10 refs., 26 figs., 17 tabs.

Altseimer, J.H.; Roach, F.; Anderson, J.M.; Krupka, M.C.

1987-08-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Controlled Shear Band and Fracture in Bulk Metallic Glasses  

Science Conference Proceedings (OSTI)

Aerospace and Spacecraft Applications for Bulk Metallic Glasses and Matrix Composites · Air Oxidation of a Binary Cu64.5Zr35.5 Bulk Metallic Alloy at 573 ...

402

Controlling Defect Density in Polymer-Fullerene Bulk Heterojunction ...  

Science Conference Proceedings (OSTI)

Controlling Defect Density in Polymer-Fullerene Bulk Heterojunction Solar Cells by Optimizing ... Engineering Carbon Nanomaterials for Energy Application.

403

Superconductivity in bulk ultrafine-grained metals prepared by high ...  

Science Conference Proceedings (OSTI)

About this Abstract. Meeting, 2014 TMS Annual Meeting & Exhibition. Symposium , Ultrafine Grained Materials VIII. Presentation Title, Superconductivity in bulk ...

404

Initial Assessment of U.S. Refineries for Purposes of Potential Bio-Based Oil Insertions  

SciTech Connect

This study examines how existing U.S. refining infrastructure matches in geography and processing capability with the needs projected from anticipated biofuels production. Key findings include: ? a potential shortfall in both overall hydrotreating capacity and hydrogen production capacity in refineries to manage the conversion of certain bio-derived feedstocks having high oxygen contents; ? a regional concentration of anticipated biofuel resources, placing added stress in particular refining regions (e.g. the Gulf Coast); ? uncertainties surrounding the impact of bio-derived fuel intermediates on the refiner’s ability to meet product performance and product quantity demands, and the need for better and more comprehensive chemical composition information; ? the need for considerably more data and experience on the behavior of projected biofuels feedstocks in refining processes (e.g. impacts on process performance and reliability); ? and the need to examine the optimum capital investment locations for additional processing equipment. For example, whether it is better to further refine biofuels at the new production sites, in centralized biofuel "depots", or whether the existing refining facilities should be expanded to better handle a more 'raw' biofuel.

Freeman, Charles J.; Jones, Susanne B.; Padmaperuma, Asanga B.; Santosa, Daniel M.; Valkenburg, Corinne; Shinn, John

2013-04-25T23:59:59.000Z

405

Cracking of simulated oil refinery off-gas over a coal char, petroleum coke, and quartz  

Science Conference Proceedings (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

406

Summary of the proceedings of the workshop on the refinery of the future  

SciTech Connect

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.

1994-06-01T23:59:59.000Z

407

Biofacts: Fueling a stronger economy. Renewable fuel solutions for petroleum refineries  

DOE Green Energy (OSTI)

The DOE Biofuels Program is investigating processes to condition synthesis gas (syngas) produced from the gasification of biomass, coke, waste oils, and other inexpensive feedstocks and low-cost by-products. Syngas technologies offer refiners economical, flexible solutions to the challenges presented by today`s market forces and regulatory environment, such as: increasingly stringent environmental regulations that dictate the composition of petroleum products; increasingly sour crudes; increased coke production and hydrogen use resulting from heavier crude; increased disposal cost for coke and residuals oils; and decreasing hydrogen supply resulting from decreased catalytic reforming severity--a necessity to comply with requirements for reduced aromatic content. Most importantly, refiners can use the DOE syngas processes to upgrade refinery residuals and coke, which minimizes environmental problems and maximizes profitability. DOE`s solution also offers refiners the flexibility to economically supplement petroleum feedstocks with a wide variety of locally available renewable feedstocks that can be fed into the gasifier--feedstocks such as energy crops, municipal solid wastes, many industrial wastes, and agricultural by-products.

NONE

1995-07-01T23:59:59.000Z

408

Bayesian-lopa methodology for risk assessment of an LNG importation terminal  

E-Print Network (OSTI)

LNG (Liquefied Natural Gas) is one of the fastest growing energy sources in the U.S. to fulfill the increasing energy demands. In order to meet the LNG demand, many LNG facilities including LNG importation terminals are operating currently. Therefore, it is important to estimate the potential risks in LNG terminals to ensure their safety. One of the best ways to estimate the risk is LOPA (Layer of Protection Analysis) because it can provide quantified risk results with less time and efforts than other methods. For LOPA application, failure data are essential to compute risk frequencies. However, the failure data from the LNG industry are very sparse. Bayesian estimation is identified as one method to compensate for its weaknesses. It can update the generic data with plant specific data. Based on Bayesian estimation, the frequencies of initiating events were obtained using a conjugate gamma prior distribution such as OREDA (Offshore Reliability Data) database and Poisson likelihood distribution. If there is no prior information, Jeffreys noninformative prior may be used. The LNG plant failure database was used as plant specific likelihood information. The PFDs (Probability of Failure on Demand) of IPLs (Independent Protection Layers) were estimated with the conjugate beta prior such as EIReDA (European Industry Reliability Data Bank) database and binomial likelihood distribution. In some cases EIReDA did not provide failure data, so the newly developed Frequency-PFD conversion method was used instead. By the combination of Bayesian estimation and LOPA procedures, the Bayesian-LOPA methodology was developed and was applied to an LNG importation terminal. The found risk values were compared to the tolerable risk criteria to make risk decisions. Finally, the risk values of seven incident scenarios were compared to each other to make a risk ranking. In conclusion, the newly developed Bayesian-LOPA methodology really does work well in an LNG importation terminal and it can be applied in other industries including refineries and petrochemicals. Moreover, it can be used with other frequency analysis methods such as Fault Tree Analysis (FTA).

Yun, Geun-Woong

2007-12-01T23:59:59.000Z

409

Design of a Graphic Generator for Remote Terminal Application  

Science Conference Proceedings (OSTI)

The design of a graphic display system for remote terminal application is presented. Control data requirements are reduced by generating a useful set of graphic primitives locally at the remote terminals. Keywords: Computer graphics, digital differential analyzers, peripherals, remote terminals.

J. R. Armstrong

1973-05-01T23:59:59.000Z

410

Hanford ETR Bulk Vitrification System - Demonstration Bulk Vitrification System (DBVS) Review Report  

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

A Comprehensive Technical A Comprehensive Technical Review of the Demonstration Bulk Vitrification System Technical Assessment Conducted by an Independent and External Team of Experts Volume 1 September 28, 2006 Chartered by CH2M HILL Hanford Group, Inc. Richland, Washington 99352 RPP-31314 Executive Summary In May 2006, CH2M HILL Hanford Group, Inc. chartered an Expert Review Panel (ERP) to review the current status of the Demonstration Bulk Vitrification System (DBVS). It is the consensus of the ERP that bulk vitrification is a technology that requires further development and evaluation to determine its potential for meeting the Hanford waste stabilization mission. No fatal flaws (issues that would jeopardize the overall DBVS mission that cannot be mitigated) were found, given the current state of the project.

411

Improving the bulk data transfer experience  

Science Conference Proceedings (OSTI)

Scientific computations and collaborations increasingly rely on the network to provide high-speed data transfer, dissemination of results, access to instruments, support for computational steering, etc. The Energy Sciences Network is establishing a science data network to provide user driven bandwidth allocation. In a shared network environment, some reservations may not be granted due to the lack of available bandwidth on any single path. In many cases, the available bandwidth across multiple paths would be sufficient to grant the reservation. In this paper we investigate how to utilize the available bandwidth across multiple paths in the case of bulk data transfer.

Guok, Chin; Guok, Chin; Lee, Jason R.; Berket, Karlo

2008-05-07T23:59:59.000Z

412

Examination of Terminal Land Requirements for Hydrogen Delivery  

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

May 8, 2007 Jerry Gillette Examination of Terminal Land Requirements for Hydrogen Hydrogen Delivery Analysis Meeting Argonne National Laboratory A Variety of Terminal...

413

A 39 year follow-up of the UK oil refinery and distribution centre studies: results for kidney cancer and leukaemia. Environ Health Perspect Suppl 101(Suppl  

E-Print Network (OSTI)

This paper presents briefly some of the principal results of a mortality analysis of a cohort of workers employed for at least 1 year between 1950 and 1975 at eight oil refineries and approximately 750 distribution centers in the U.K, together with detailed results for kidney cancer and leukemia. Over 99 % of the workers were successfully traced. Their mortality was compared with that of all males in the national population. The mortality from all causes of death is lower than that of the comparison population in both studies, and reduced mortality is also found for many of the major nonmalignant causes of death. In the refinery study, some increased mortality patterns are found for diseases of the arteries, and no healthy worker effect is found in the distribution center study for ischemic heart disease. Mortality from all neoplasms is lower than expected overall in both studies, largely due to a deficit of deaths from malignant neoplasm of the lung. Mortality from malignant neoplasm of the kidney is increased overall in the distribution center study, and in drivers in particular. The mortality from this disease increases with increased time since first exposure. The observed deaths from leukemia are slightly less than expected in the refinery study and slightly more than expected in the distribution center study. One refinery shows increased mortality due to in myeloid leukemia, and mortality is increased among refinery operators. Mortality is also raised in distribution center drivers, particularly for myeloid leukemias, including acute myeloid leukemia.

Lesley Rushton

1993-01-01T23:59:59.000Z

414

Conversion of high carbon refinery by-products. Quarterly report, October 1--December 31, 1995  

SciTech Connect

The overall objective of the project is to demonstrate that a partial oxidation system, which utilizes a transport reactor, is a viable means of converting refinery wastes, byproducts, and other low value materials into valuable products. The primary product would be a high quality fuel gas, which could also be used as a source of hydrogen. The concept involves subjecting the hydrocarbon feed to pyrolysis and steam gasification in a circulating bed of solids. Carbon residue formed during pyrolysis, as well as metals in the feed, are captured by the circulating solids which are returned to the bottom of the transport reactor. Air or oxygen is introduced in this lower zone and sufficient carbon is burned, sub-stoichiometrically, to provide the necessary heat for the endothermic pyrolysis and gasification reactions. The hot solids and gases leaving this zone pass upward to contact the feed material and continue the partial oxidation process. Studies were conducted in the Transport Reactor Test Unit (TRTU) to pyrolyze naphtha with untreated as well as potassium-impregnated spent FCC (Fluid Catalytic Cracker) catalyst as the circulating medium over a temperature range of 1,400 to 1,600 F. The results from these studies are presented and discussed here. Studies were also performed in the Bench Scale Reactor Unit (BRU) in an effort to develop suitable catalyst formulations and to study the steam reforming of methane and propane in support of the experiments conducted in the TRTU. The results from these studies are also presented here. A Cold Flow Simulator (CFS) was designed and built to investigate the flow problems experienced in the TRTU.

O`Donnell, J.; Katta, S.; Henningsen, G.; Lin, Y.Y.

1996-01-19T23:59:59.000Z

415

PCs and Computer Terminals in Commercial Buildings  

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

Special Topics and Data Reports > PC's and Computer Terminals Special Topics and Data Reports > PC's and Computer Terminals Picture of a personal computer Personal Computers and Computer Terminals in Commercial Buildings PCs and Computer Terminals in 1995 Changes Between 1992 and 1995 How the Number of PCs and Computer Terminals Were Estimated References and Additional Links Over the past 10 to 15 years, the use of personal computers (PCs) has risen dramatically. The energy consumed by PCs and other types of office equipment has become a significant component of electricity consumption in commercial buildings -- 13 percent (98 billion kWh) of all electricity consumed in 1995. That amount was nearly as much as the amount used to air condition these buildings. The Energy Information Administration's 1999 Annual Energy Outlook[1] forecasts that, for the next two decades, electricity consumption for office equipment (3.2 percent annually) will grow over twice as fast as electricity use as a whole (1.4 percent annually).

416

Charm mass effects in bulk channel correlations  

E-Print Network (OSTI)

The bulk viscosity of thermalized QCD matter at temperatures above a few hundred MeV could be significantly influenced by charm quarks because their contribution arises four perturbative orders before purely gluonic effects. In an attempt to clarify the challenges of a lattice study, we determine the relevant imaginary-time correlator (of massive scalar densities) up to NLO in perturbation theory, and compare with existing data. We find discrepancies much larger than in the vector channel; this may hint, apart from the importance of taking a continuum limit, to larger non-perturbative effects in the scalar channel. We also recall how a transport peak related to the scalar density spectral function encodes non-perturbative information concerning the charm quark chemical equilibration rate close to equilibrium.

Y. Burnier; M. Laine

2013-09-06T23:59:59.000Z

417

Interface control of bulk ferroelectric polarization  

SciTech Connect

The control of material interfaces at the atomic level has led to no- vel interfacial properties and functionalities. In particular, the study of polar discontinuities at interfaces between complex oxides lies at the frontier of modern condensed matter research. Here we em- ploy a combination of experimental measurements and theoretical calculations to demonstrate the control of a bulk property, namely ferroelectric polarization, of a heteroepitaxial bilayer by precise atomic-scale interface engineering. More specifically, the control is achieved by exploiting the interfacial valence mismatch to influence the electrostatic potential step across the interface, which manifests itself as the biased-voltage in ferroelectric hysteresis loops and determines the ferroelectric state. A broad study of diverse systems comprising different ferroelectrics and conducting perovskite un- derlayers extends the generality of this phenomenon.

Yu, P [University of California, Berkeley; Luo, Weidong [ORNL; Yi, D. [University of California, Berkeley; Zhang, J.-X. [University of California, Berkeley; Rossell, M.D. [Lawrence Berkeley National Laboratory (LBNL); Yang, C.-H. [Korea Advanced Institute of Science and Technology; You, L. [University of California, Berkeley; Singh-Bhalla, G. B. [University of California, Berkeley & LBNL; Yang, S.Y [University of California, Berkeley; He, Q [University of California, Berkeley; Ramasse, Q. M. [Lawrence Berkeley National Laboratory (LBNL); Erni, R. [Lawrence Berkeley National Laboratory (LBNL); Martin, L. W. [University of Illinois, Urbana-Champaign; Chu, Y. H. [University of California, Berkeley; Pantelides, Sokrates T [ORNL; Pennycook, Stephen J [ORNL; Ramesh, R. [University of California, Berkeley

2012-01-01T23:59:59.000Z

418

DEVELOPMENT OF THE BULK TRITIUM SHIPPING PACKAGING  

SciTech Connect

A new radioactive shipping packaging for transporting bulk quantities of tritium, the Bulk Tritium Shipping Package (BTSP), has been designed for the Department of Energy (DOE) as a replacement for a package designed in the early 1970s. This paper summarizes significant design features and describes how the design satisfies the regulatory safety requirements of the Code of Federal Regulations and the International Atomic Energy Agency. The BTSP design incorporates many improvements over its predecessor by implementing improved testing, handling, and maintenance capabilities, while improving manufacturability and incorporating new engineered materials. This paper also discusses the results from testing of the BTSP to 10 CFR 71 Normal Conditions of Transport and Hypothetical Accident Condition events. The programmatic need of the Department of Energy (DOE) to ship bulk quantities of tritium has been satisfied since the late 1970s by the UC-609 shipping package. The current Certificate of Conformance for the UC-609, USA/9932/B(U) (DOE), will expire in late 2011. Since the UC-609 was not designed to meet current regulatory requirements, it will not be recertified and thereby necessitates a replacement Type B shipping package for continued DOE tritium shipments in the future. A replacement tritium packaging called the Bulk Tritium Shipping Package (BTSP) is currently being designed and tested by Savannah River National Laboratory (SRNL). The BTSP consists of two primary assemblies, an outer Drum Assembly and an inner Containment Vessel Assembly (CV), both designed to mitigate damage and to protect the tritium contents from leaking during the regulatory Hypothetical Accident Condition (HAC) events and during Normal Conditions of Transport (NCT). During transport, the CV rests on a silicone pad within the Drum Liner and is covered with a thermal insulating disk within the insulated Drum Assembly. The BTSP packaging weighs approximately 500 lbs without contents and is 50-1/2 inches high by 24-1/2 inches in outside diameter. With contents the gross weight of the BTSP is 650 lbs. The BTSP is designed for the safe shipment of 150 grams of tritium in a solid or gaseous state. To comply with the federal regulations that govern Type B shipping packages, the BTSP is designed so that it will not lose tritium at a rate greater than the limits stated in 10CFR 71.51 of 10{sup -6} A2 per hour for the 'Normal Conditions of Transport' (NCT) and an A2 in 1 week under 'Hypothetical Accident Conditions' (HAC). Additionally, since the BTSP design incorporates a valve as part of the tritium containment boundary, secondary containment features are incorporated in the CV Lid to protect against gas leakage past the valve as required by 10CFR71.43(e). This secondary containment boundary is designed to provide the same level of containment as the primary containment boundary when subjected to the HAC and NCT criteria.

Blanton, P.; Eberl, K.

2008-09-14T23:59:59.000Z

419

Bulk Heterojunction Organic Photovoltaic Devices Using Dendrimers  

Science Conference Proceedings (OSTI)

A family of prototype ..pi..-conjugated dendrimers has been synthesized and incorporated into solution-processable organic photovoltaic (OPV) devices. Bulk heterojunction devices were fabricated by blending the dendrimers with a solubilized fullerene. The best of these initial devices, which were not optimized for morphology, exhibited external quantum efficiencies of 22% at peak wavelength. It was found that 3-arm dendrimers, when sufficiently soluble, yielded higher photocurrents than their 4-arm counterparts. This was attributed to better planarity and intermolecular alignment of the 3-arm version. Device efficiency was seen to increase with increasing arm length. A reduced-band gap dendrimer was synthesized by attaching electron-withdrawing groups onto the core to yield an optical band gap of 1.82 eV.

Kopidakis, N.; Mitchell, W. J.; Bozell, J. J.; Piris, J.; Ginley, D. S.; Rumbles, G.; Shaheen S. E.

2005-11-01T23:59:59.000Z

420

Organic hybrid planar-nanocrystalline bulk heterojunctions  

DOE Patents (OSTI)

A photosensitive optoelectronic device having an improved hybrid planar bulk heterojunction includes a plurality of photoconductive materials disposed between the anode and the cathode. The photoconductive materials include a first continuous layer of donor material and a second continuous layer of acceptor material. A first network of donor material or materials extends from the first continuous layer toward the second continuous layer, providing continuous pathways for conduction of holes to the first continuous layer. A second network of acceptor material or materials extends from the second continuous layer toward the first continuous layer, providing continuous pathways for conduction of electrons to the second continuous layer. The first network and the second network are interlaced with each other. At least one other photoconductive material is interspersed between the interlaced networks. This other photoconductive material or materials has an absorption spectra different from the donor and acceptor materials.

Forrest, Stephen R. (Ann Arbor, MI); Yang, Fan (Piscataway, NJ)

2011-03-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Organic hybrid planar-nanocrystalline bulk heterojunctions  

DOE Patents (OSTI)

A photosensitive optoelectronic device having an improved hybrid planar bulk heterojunction includes a plurality of photoconductive materials disposed between the anode and the cathode. The photoconductive materials include a first continuous layer of donor material and a second continuous layer of acceptor material. A first network of donor material or materials extends from the first continuous layer toward the second continuous layer, providing continuous pathways for conduction of holes to the first continuous layer. A second network of acceptor material or materials extends from the second continuous layer toward the first continuous layer, providing continuous pathways for conduction of electrons to the second continuous layer. The first network and the second network are interlaced with each other. At least one other photoconductive material is interspersed between the interlaced networks. This other photoconductive material or materials has an absorption spectra different from the donor and acceptor materials.

Forrest, Stephen R.; Yang, Fan

2013-04-09T23:59:59.000Z

422

Economic impacts of oil spills: Spill unit costs for tankers, pipelines, refineries, and offshore facilities. [Task 1, Final report  

SciTech Connect

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

423

Standard practice for evaluating and qualifying oil field and refinery corrosion inhibitors using the rotating cylinder electrode  

E-Print Network (OSTI)

1.1 This practice covers a generally accepted procedure to use the rotating cylinder electrode (RCE) for evaluating corrosion inhibitors for oil field and refinery applications in defined flow conditions. 1.2 The values stated in SI units are to be regarded as the standard. The values given in parentheses are for information only. 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 limitations prior to use.

American Society for Testing and Materials. Philadelphia

2006-01-01T23:59:59.000Z

424

Optimization Control Strategies for HVAC Terminal Boxes  

E-Print Network (OSTI)

The HVAC terminal boxes are one of the major building HVAC components. They directly impact the building room comfort conditions and the energy costs. How to operate the box in a highly energy efficient way and maintain the room comfort level is an important topic in today's building energy management and HVAC control field. The authors developed novel optimized control strategies and operation schedules for the terminal boxes for both occupied and non-occupied hours. The optimized control schedules were implemented in a medical complex during the commissioning. This not only improved the building comfort conditions but also reduced the energy costs.

Zhu, Y.; Batten, T.; Noboa, H.; Claridge, D. E.; Turner, W. D.; Liu, M.; Zhou, J.; Cameron, C.; Keeble, D.; Hirchak, R.

2000-01-01T23:59:59.000Z

425

Vibrated Bulk Density (VBD) of Calcined Petroleum Coke and ...  

Science Conference Proceedings (OSTI)

Abstract Scope, Vibrated bulk density (VBD) is a quantitative measurement used in the aluminum industry to evaluate the density of calcined petroleum coke.

426

Vibrated Bulk Density (VBD) of Calcined Petroleum Coke and ...  

Science Conference Proceedings (OSTI)

Presentation Title, Vibrated Bulk Density (VBD) of Calcined Petroleum Coke and Implications of Changes in the ASTM Method D4292. Author(s), Bill Spencer, ...

427

Innovative approaches to improve bulk heterojuction organic photovoltaic device performance.  

E-Print Network (OSTI)

??In this thesis we studied the electrical properties of bulk heterojunction organic photovoltaic (OPV) devices fabricated using a variety of conjugated polymers, including regioregular P3HT,… (more)

Zhang, Ye

2010-01-01T23:59:59.000Z

428

Synthesis and Characterization of Bulk Nano Crystalline Pb Free ...  

Science Conference Proceedings (OSTI)

High energy ball milling route was adopted for production of bulk nano crystalline solders from these alloy powders. The milling was carried out for a period of ...

429

Fabrication of Bulk Metallic Glass Foams via Severe Plastic ...  

Science Conference Proceedings (OSTI)

Symposium, M. Bulk Metallic Glasses, Nanocrystalline Materials, and ... Application of Metallic Glass for High Performance Si Solar Cell: Oxidation Behavior of ...

430

Bulk Metallic Glass Composites Fabricated within the Supercooled ...  

Science Conference Proceedings (OSTI)

In the present work, lightweight magnesium base Bulk Metallic Glass Composites ... Application of Metallic Glass for High Performance Si Solar Cell: Oxidation ...

431

Modular Electromechanical Batteries for Cost-Effective Bulk ...  

The "new breed" of flywheel under development at the Lawrence Livermore National Laboratory is aimed specifically at the "bulk storage" of electrical energy where the ...

432

PCN-based measured rate termination  

Science Conference Proceedings (OSTI)

Overload in a packet-based network can be prevented by admitting or blocking new flows depending on its load conditions. However, overload can occur in spite of admission control due to unforseen events, e.g., when admitted traffic is rerouted in the ... Keywords: Admission control, Differentiated services, Flow termination, QoS, Resilience

Michael Menth; Frank Lehrieder

2010-09-01T23:59:59.000Z

433

Termination for superconducting power transmission systems  

DOE Patents (OSTI)

This patent relates to a cold, electrical gradient, terminal section for a superconducting cable for alternating current power transmission. A cold electrical gradient section filled with a gaseous coolant acting as an insulator is provided in series with a separate thermal gradient section. (auth)

Forsyth, E.B.; Jensen, J.E.

1975-08-26T23:59:59.000Z

434

Aggregate Terminal Velocity/Temperature Relations  

Science Conference Proceedings (OSTI)

Terminal velocities of snow aggregates in storms along the Front Range in eastern Colorado are examined with a ground-based two-dimensional video disdrometer. Power-law relationships for particles having equivalent volume diameters of 0.5–20 mm ...

Edward A. Brandes; Kyoko Ikeda; Gregory Thompson; Michael Schönhuber

2008-10-01T23:59:59.000Z

435

Texas Bulk Power Study-- An Overview  

E-Print Network (OSTI)

In the 1980's, several significant changes have evolved in markets for electric power in Texas. Cogeneration, fuel market volatility, electric system reliability, generation and transmission facility construction delays, construction cost escalation, regional disparities in load growth, severe economic cycles, and a variety of legal, health and environmental issues have contributed to increasing uncertainty in the utility planning process. Through more coordination and power pooling among the state's major utilities within the Electric Reliability Council of Texas (ERCOT), a potentially higher level of bulk power transactions may reduce some uncertainty and result in cost savings to the utilities involved. However, both the transactions potential and any corresponding changes in operating costs are quite sensitive to assumptions about the price of natural gas for use as a utility boiler fuel. A large computer model which simulates the operation of the utilities under the extreme boundary conditions of zero transactions and fully coordinated economic dispatch results in a range of transactions from 5% to 14% of total system energy requirements and a range of cost savings from less than 1% to nearly 6% of the ERCOT system variable operating costs.

Moore, B.

1988-09-01T23:59:59.000Z

436

Prediction of Graupel Density in a Bulk Microphysics Scheme  

Science Conference Proceedings (OSTI)

A method to predict the bulk density of graupel ?g has been added to the two-moment Milbrandt–Yau bulk microphysics scheme. The simulation of graupel using the modified scheme is illustrated through idealized simulations of a mesoscale convective ...

Jason A. Milbrandt; Hugh Morrison

2013-02-01T23:59:59.000Z

437

An evolutionary optimization approach for bulk material blending systems  

Science Conference Proceedings (OSTI)

Bulk material blending systems still mostly implement static and non-reactive material blending methods like the well-known Chevron stacking. The optimization potential in the existing systems which can be made available using quality analyzing methods ... Keywords: bulk material blending, chevron stacking, multi-objective evolutionary algorithms

Michael P. Cipold; Pradyumn Kumar Shukla; Claus C. Bachmann; Kaibin Bao; Hartmut Schmeck

2012-09-01T23:59:59.000Z

438

Preparation of bulk 13C-enriched graphene materials  

Science Conference Proceedings (OSTI)

Arc-discharge has been widely used in the bulk production of various carbon nanomaterials, especially for structurally more robust single-walled carbon nanotubes. In this paper, the same bulk-production technique was applied to the synthesis of significantly ...

Leilei Tian; Xin Wang; Li Cao; Mohammed J. Meziani; Chang Yi Kong; Fushen Lu; Ya-Ping Sun

2010-01-01T23:59:59.000Z

439

An Empirical Analysis of Bulk Cn2 Models over Water  

Science Conference Proceedings (OSTI)

This article examines some of the difficulties associated with the determination of C2n over water in a coastal region using a bulk model. The analysis shows the need to supplement bulk models with elements that do not belong to traditional Monin–...

Guy Potvin; Denis Dion; Jacques Claverie; Paul A. Frederickson; Kenneth L. Davidson; J. Luc Forand

2008-12-01T23:59:59.000Z

440

Bulk Vitrification Castable Refractory Block Protection Study  

Science Conference Proceedings (OSTI)

Bulk vitrification (BV) was selected for a pilot-scale test and demonstration facility for supplemental treatment to accelerate the cleanup of low-activity waste (LAW) at the Hanford U.S. DOE Site. During engineering-scale (ES) tests, a small fraction of radioactive Tc (and Re, its nonradioactive surrogate) were transferred out of the LAW glass feed and molten LAW glass, and deposited on the surface and within the pores of the castable refractory block (CRB). Laboratory experiments were undertaken to understand the mechanisms of the transport Tc/Re into the CRB during vitrification and to evaluate various means of CRB protection against the deposition of leachable Tc/Re. The tests used Re as a chemical surrogate for Tc. The tests with the baseline CRB showed that the molten LAW penetrates into CRB pores before it converts to glass, leaving deposits of sulfates and chlorides when the nitrate components decompose. Na2O from the LAW reacts with the CRB to create a durable glass phase that may contain Tc/Re. Limited data from a single CRB sample taken from an ES experiment indicate that, while a fraction of Tc/Re is present in the CRB in a readily leachable form, most of the Tc/Re deposited in the refractory is retained in the form of a durable glass phase. In addition, the molten salts from the LAW, mainly sulfates, chlorides, and nitrates, begin to evaporate from BV feeds at temperatures below 800 C and condense on solid surfaces at temperatures below 530 C. Three approaches aimed at reducing or preventing the deposition of soluble Tc/Re within the CRB were proposed: metal lining, sealing the CRB surface with a glaze, and lining the CRB with ceramic tiles. Metal liners were deemed unsuitable because evaluations showed that they can cause unacceptable distortions of the electric field in the BV system. Sodium silicate and a low-alkali borosilicate glaze were selected for testing. The glazes slowed down molten salt condensate penetration, but did little to reduce the penetration of molten salt. Out of several refractory tile candidates, only greystone and fused-cast alumina-zirconia-silica (AZS) refractory remained intact and well bonded to the CRB after firing to 1000 C. The deformation of the refractory-tile composite was avoided by prefiring the greystone tile to 800 C. Condensed vapors did not penetrate the tiles, but Re salts condensed on their surface. Refractory corrosion tests indicated that a 0.25-inch-thick greystone tile would not corrode during a BV melt. Tiles can reduce both vapor penetration and molten salt penetration, but vapor deposition above the melt line will occur even on tiles. The Tc/Re transport scenario was outlined as follows. At temperatures below 700 C, molten ionic salt (MIS) that includes all the Tc/Re penetrates, by capillarity, from the feed into the CRB open porosity. At approximately 750 C, the MIS decomposes through the loss of NOx, leaving mainly sulfate and chloride salts. The Na2O formed in the decomposition of the nitrates reacts with insoluble grains in the feed and with the aluminosilicates in the CRB to form more viscous liquids that reduce further liquid penetration into the CRB. At 800 to 1000 C, a continuous glass phase traps the remains of the MIS in the form of inclusions in the bulk glass melt. At 1000 to 1200 C, the salt inclusions in the glass slowly dissolve but also rise to the surface. The Tc/Re salts also evaporate from the free surface of the glass melt that is rapidly renewed by convective currents. The vapors condense on cooler surfaces in the upper portion of the CRB, the box lid, and the off-gas system.

Hrma, Pavel R.; Bagaasen, Larry M.; Beck, Andrew E.; Brouns, Thomas M.; Caldwell, Dustin D.; Elliott, Michael L.; Matyas, Josef; Minister, Kevin BC; Schweiger, Michael J.; Strachan, Denis M.; Tinsley, Bronnie P.; Hollenberg, Glenn W.

2005-05-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

Silicon bulk micromachined hybrid dimensional artifact.  

Science Conference Proceedings (OSTI)

A mesoscale dimensional artifact based on silicon bulk micromachining fabrication has been developed and manufactured with the intention of evaluating the artifact both on a high precision coordinate measuring machine (CMM) and video-probe based measuring systems. This hybrid artifact has features that can be located by both a touch probe and a video probe system with a k=2 uncertainty of 0.4 {micro}m, more than twice as good as a glass reference artifact. We also present evidence that this uncertainty could be lowered to as little as 50 nm (k=2). While video-probe based systems are commonly used to inspect mesoscale mechanical components, a video-probe system's certified accuracy is generally much worse than its repeatability. To solve this problem, an artifact has been developed which can be calibrated using a commercially available high-accuracy tactile system and then be used to calibrate typical production vision-based measurement systems. This allows for error mapping to a higher degree of accuracy than is possible with a glass reference artifact. Details of the designed features and manufacturing process of the hybrid dimensional artifact are given and a comparison of the designed features to the measured features of the manufactured artifact is presented and discussed. Measurement results from vision and touch probe systems are compared and evaluated to determine the capability of the manufactured artifact to serve as a calibration tool for video-probe systems. An uncertainty analysis for calibration of the artifact using a CMM is presented.

Claudet, Andre A.; Tran, Hy D.; Bauer, Todd Marks; Shilling, Katherine Meghan; Oliver, Andrew David

2010-03-01T23:59:59.000Z

442

Carbon nanotubes grown on bulk materials and methods for fabrication  

DOE Patents (OSTI)

Disclosed are structures formed as bulk support media having carbon nanotubes formed therewith. The bulk support media may comprise fibers or particles and the fibers or particles may be formed from such materials as quartz, carbon, or activated carbon. Metal catalyst species are formed adjacent the surfaces of the bulk support material, and carbon nanotubes are grown adjacent the surfaces of the metal catalyst species. Methods employ metal salt solutions that may comprise iron salts such as iron chloride, aluminum salts such as aluminum chloride, or nickel salts such as nickel chloride. Carbon nanotubes may be separated from the carbon-based bulk support media and the metal catalyst species by using concentrated acids to oxidize the carbon-based bulk support media and the metal catalyst species.

Menchhofer, Paul A. (Clinton, TN); Montgomery, Frederick C. (Oak Ridge, TN); Baker, Frederick S. (Oak Ridge, TN)

2011-11-08T23:59:59.000Z

443

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

SciTech Connect

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

444

Design and implementation of a fuzzy expert system for performance assessment of an integrated health, safety, environment (HSE) and ergonomics system: The case of a gas refinery  

Science Conference Proceedings (OSTI)

The objective of this study is to design a fuzzy expert system for performance assessment of health, safety, environment (HSE) and ergonomics system factors in a gas refinery. This will lead to a robust control system for continuous assessment and improvement ... Keywords: Environment, Ergonomics, Expert system, Fuzzy logic, Health, Safety

A. Azadeh; I. M. Fam; M. Khoshnoud; M. Nikafrouz

2008-11-01T23:59:59.000Z

445

Declaration of Termination of Domestic Partnership Form  

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

DPT (01-2012) DPT (01-2012) SANDIA PROPRIETARY INFORMATION PERSONALLY IDENTIFIABLE INFORMATION (PII) (WHEN COMPLETE) Declaration of Termination of Domestic Partnership Form To be completed by the employee and submitted to the Sandia Benefits Customer Service Center at the address above. Please keep a copy for your records. Sworn Affidavit We, __________________________________________ and _____________________________________________ Employee Domestic Partner __________________________________________ _____________________________________________ Employee Social Security Number Domestic Partner Social Security Number __________________________________________ _____________________________________________ Employee Date of Birth Domestic Partner Date of Birth

446

Environmental Assessment for the Terminal Expansion Project.  

SciTech Connect

The Terminal Expansion Project is proposed by Bonneville Power Administration (BPA), Southern California Edison (SCE), and the Los Angeles Department of Water and Power (LADWP) to increase the operating capacity of the existing bipole direct current (dc) Intertie line between the Celilo Converter Station at The Dalles, Oregon, and the Sylmar converter Station at Sylmar, California. The proposal will allow a greater exchange of electric power between the Pacific Northwest (PNW) and Southern California without constructing new interregional transmission lines. By adding more alternating ac/dc converter equipment at the terminals, the conductors on the existing 845-mile dc intertie transmission line can be operated at full design capacity. The dc Intertie plus two other ac lines which terminate near San Francisco comprise the ''Intertie.'' Though the project is interregional, relatively little construction will be needed. This Environmental Assessment addresses the environmental impacts of the proposed actions and makes a determination as to their significance. Though LADWP is complying with the State environmental process, as required by the California Environmental Quality Act (CEQA), the impacts of their construction are being considered as part of the impacts of the overall proposal and are considered in the determination of significance.

United States. Bonneville Power Administration.

1985-02-01T23:59:59.000Z

447

Table Definitions, Sources, and Explanatory Notes  

Gasoline and Diesel Fuel Update (EIA)

Refinery, Bulk Terminal, and Natural Gas Plant Stocks by State Refinery, Bulk Terminal, and Natural Gas Plant Stocks by State Definitions Key Terms Definition Bulk Terminal A facility used primarily for the storage and/or marketing of petroleum products which has a total bulk storage capacity of 50,000 barrels or more and/or receives petroleum products by tanker, barge, or pipeline. Conventional Gasoline Finished motor gasoline not included in the oxygenated or reformulated gasoline categories. Excludes reformulated gasoline blendstock for oxygenate blending (RBOB) as well as other blendstock. Crude Oil A mixture of hydrocarbons that exists in liquid phase in natural underground reservoirs and remains liquid at atmospheric pressure after passing through surface separating facilities. Depending upon the characteristics of the crude stream, it may also include:

448

ZigZag Decoding: Combating Hidden Terminals in Wireless Networks  

E-Print Network (OSTI)

This paper presents ZigZag, an 802.11 receiver that combats hidden terminals. ZigZag exploits 802.11 retransmissions which, in the case of hidden terminals, cause successive collisions. Due to asynchrony, these collisions ...

Katabi, Dina

2008-04-08T23:59:59.000Z

449

BULK FLOW OF HALOS IN {Lambda}CDM SIMULATION  

Science Conference Proceedings (OSTI)

Analysis of the Pangu N-body simulation validates that the bulk flow of halos follows a Maxwellian distribution with variance that is consistent with the prediction of the linear theory of structure formation. We propose that the consistency between the observed bulk velocity and theories should be examined at the effective scale of the radius of a spherical top-hat window function yielding the same smoothed velocity variance in linear theory as the sample window function does. We compared some recently estimated bulk flows from observational samples with the prediction of the {Lambda}CDM model we used; some results deviate from expectation at a level of {approx}3{sigma}, but the discrepancy is not as severe as previously claimed. We show that bulk flow is only weakly correlated with the dipole of the internal mass distribution, that the alignment angle between the mass dipole and the bulk flow has a broad distribution peaked at {approx}30 Degree-Sign -50 Degree-Sign , and also that the bulk flow shows little dependence on the mass of the halos used in the estimation. In a simulation of box size 1 h {sup -1} Gpc, for a cell of radius 100 h {sup -1} Mpc the maximal bulk velocity is >500 km s{sup -1}; dipoles of the environmental mass outside the cell are not tightly aligned with the bulk flow, but are rather located randomly around it with separation angles {approx}20 Degree-Sign -40 Degree-Sign . In the fastest cell there is a slightly smaller number of low-mass halos; however, halos inside are clustered more strongly at scales {approx}> 20 h {sup -1} Mpc, which might be a significant feature since the correlation between bulk flow and halo clustering actually increases in significance beyond such scales.

Li Ming; Pan Jun; Feng Longlong; Kang Xi [Purple Mountain Observatory, 2 West Beijing Road, Nanjing 210008 (China); Gao Liang [National Astronomical Observatories, Chinese Academy of Sciences, 20A Datun Road, Chaoyang District, Beijing 100012 (China); Jing Yipeng; Yang Xiaohu; Lin Weipeng; Zhao Donghai; Zhang Pengjie [Key Laboratory for Research in Galaxies and Cosmology, Shanghai Astronomical Observatory, 80 Nandan Road, Shanghai 200030 (China); Chi Xuebin; Shan Guihua; Wang Long, E-mail: jpan@bao.ac.cn [Supercomputing Center, Computer Network Information Center, Chinese Academy of Sciences, 4 Zhongguancun Nansijie, Haidian District, Beijing 100190 (China)

2012-12-20T23:59:59.000Z

450

Brane-Bulk energy exchange and agegraphic dark energy  

E-Print Network (OSTI)

We consider the agegraphic models of dark energy in a braneworld scenario with brane-bulk energy exchange. We assume that the adiabatic equation for the dark matter is satisfied while it is violated for the agegraphic dark energy due to the energy exchange between the brane and the bulk. Our study shows that with the brane-bulk interaction, the equation of state parameter of agegraphic dark energy on the brane, $w_D$, can have a transition from normal state where $w_D >-1 $ to the phantom regime where $w_D energy always satisfies $w^{\\mathrm{eff}}_D\\geq-1$.

Ahmad Sheykhi

2009-08-09T23:59:59.000Z

451

Feasibility Study of Economics and Performance of Solar Photovoltaics at the Former St. Marks Refinery in St. Marks, Florida  

NLE Websites -- All DOE Office Websites (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

452

1170-MW(t) HTGR-PS/C plant application study report: Geismar, Louisiana refinery/chemical complex application  

SciTech Connect

This report summarizes a study to apply an 1170-MW(t) high-temperature gas-cooled reactor - process steam/cogeneration (HTGR-PS/C) to an industrial complex at Geismar, Louisiana. This study compares the HTGR with coal and oil as process plant fuels. This study uses a previous broad energy alternative study by the Stone and Webster Corporation on refinery and chemical plant needs in the Gulf States Utilities service area. The HTGR-PS/C was developed by General Atomic (GA) specifically for industries which require both steam and electric energy. The GA 1170-MW(t) HTGR-PC/C design is particularly well suited to industrial applications and is expected to have excellent cost benefits over other energy sources.

McMain, Jr., A. T.; Stanley, J. D.

1981-05-01T23:59:59.000Z

453

ARM - Campaign Instrument - ec-convair580-bulk  

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

govInstrumentsec-convair580-bulk govInstrumentsec-convair580-bulk Comments? We would love to hear from you! Send us a note below or call us at 1-888-ARM-DATA. Send Campaign Instrument : Environment Canada Convair 580 Bulk Parameters (EC-CONVAIR580-BULK) Instrument Categories Aerosols, Cloud Properties, Airborne Observations Campaigns Indirect and Semi-Direct Aerosol Campaign (ISDAC) [ Download Data ] North Slope Alaska, 2008.04.01 - 2008.04.30 Primary Measurements Taken The following measurements are those considered scientifically relevant. Refer to the datastream (netcdf) file headers for the list of all available measurements, including those recorded for diagnostic or quality assurance purposes. Ice water content Liquid water content Hydrometeor size Cloud particle number concentration Aerosol concentration

454

Bulk Energy Storage Webinar Rescheduled for February 9, 2012 | Department  

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

Bulk Energy Storage Webinar Rescheduled for February 9, 2012 Bulk Energy Storage Webinar Rescheduled for February 9, 2012 Bulk Energy Storage Webinar Rescheduled for February 9, 2012 February 1, 2012 - 12:48pm Addthis The U.S. Department of Energy (DOE) and the Iowa Stored Energy Park (ISEP) are conducting a free, 1-hour webinar, Lessons from Iowa: The Economic, Market, and Organizational Issues in Making Bulk Energy Storage Work, on Thursday, February 9, 2012 at 1 p.m. ET. Presenters include Dr. Imre Gyuk of DOE's Office of Electricity Deliverability and Energy Reliability and Bob Schulte from ISEP. The webinar was original scheduled for January 20, 2012, but experienced technical difficulties due to the large number of participants and was rescheduled. All participants must reregister. Funded by a DOE grant and managed by Sandia National Laboratories, ISEP's

455

Design of Bulk Nanocomposites as High Efficiency Thermoelectric Materials |  

Office of Science (SC) Website

Design of Bulk Nanocomposites as High Design of Bulk Nanocomposites as High Efficiency Thermoelectric Materials Energy Frontier Research Centers (EFRCs) EFRCs Home Centers Research Science Highlights Highlight Archives News & Events Publications Contact BES Home 04.27.12 Design of Bulk Nanocomposites as High Efficiency Thermoelectric Materials Print Text Size: A A A RSS Feeds FeedbackShare Page Scientific Achievement A newly synthesized bulk thermoelectric material that contains nanocrystals with the same orientation and structure as the host material breaks thermoelectric efficiency records by blocking thermal, but not electrical, conductivity. Significance and Impact A new strategy to design inexpensive materials that more efficiently convert heat to electricity. Research Details Thermoelectric materials directly generate electrical power from heat, but

456

Modeling Bulk Atmospheric Drainage Flow in a Valley  

Science Conference Proceedings (OSTI)

Most simulations of bulk valley-drainage flows depend heavily on parameterizations. The 1984 Atmospheric Studies in Complex Terrain (ASCOT) field experiment in Brush Creek Valley, Colorado, provided an unprecedented density of measurements in a ...

Ronald J. Dobosy

1989-09-01T23:59:59.000Z

457

Structural and economic analysis of capesize bulk carriers  

E-Print Network (OSTI)

Structural failures of bulk carriers continue to account for the loss of many lives every year. Capes are particularly vulnerable to cracking because of their large length, their trade in high density cargos, and the high ...

Hadjiyiannis, Nicholas

2010-01-01T23:59:59.000Z

458

Bodipy-backboned polymers as electron donor in bulk heterojunction ...  

Bodipy-backboned polymers as electron donor in bulk heterojunction solar cellsw BongSoo Kim,a Biwu Ma,*b Venkat R. Donuru,c Haiying Liuc and Jean M. J. Fre´chet*ab

459

A Bulk Microphysics Parameterization with Multiple Ice Precipitation Categories  

Science Conference Proceedings (OSTI)

A single-moment bulk microphysics scheme with multiple ice precipitation categories is described. It has 2 liquid hydrometeor categories (cloud droplets and rain) and 10 ice categories that are characterized by habit, size, and density—two ice ...

Jerry M. Straka; Edward R. Mansell

2005-04-01T23:59:59.000Z

460

Bulk viscosity in nuclear and quark matter: A short review  

E-Print Network (OSTI)

The history and recent progresses in the study of bulk viscosity in nuclear and quark matter are reviewed. The constraints from baryon number conservation and electric neutrality in quark matter on particle densities and fluid velocity divergences are discussed.

Hui Dong; Nan Su; Qun Wang

2007-02-07T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

A Second-Order Bulk Boundary-Layer Model  

Science Conference Proceedings (OSTI)

Bulk mass-flux models represent the large eddies that are primarily responsible for the turbulent fluxes in the planetary boundary layer as convective circulations, with an associated convective mass flux. In order for such models to be useful, ...

David A. Randall; Qingqiu Shao; Chin-Hoh Moeng

1992-10-01T23:59:59.000Z

462

Influence of Bulk Convection on Freckle Formation in Castings  

Science Conference Proceedings (OSTI)

compartments, a hot zone and a cold zone as shown in Figure l(a) below. A baffle is used to .... that the bulk convection cell will not distort the flow at the inlet.

463

Mapping the Strain Distributions in Deformed Bulk Metallic Glasses ...  

Science Conference Proceedings (OSTI)

Abstract Scope, Bulk metallic glasses (BMGs) represent relatively new class of ... Evolution of Internal Strain with Temperature in Depleted Uranium in the ... Structural Effects upon Macroscopic Phenomena in Strained Ordered Oxide Films.

464

Development of Bulk Metallic Glasses with High Plasticity Using the ...  

Science Conference Proceedings (OSTI)

Air-Oxidation of a (Zr55Cu30Al10Ni5)98Er2 Bulk Metallic Glass at 350-500oc · Anelastic Deformation of a Metallic Glass · Anisotropy in Metallic Glasses.

465

Photonic integration in a commercial scaled bulk-CMOS process  

E-Print Network (OSTI)

We demonstrate the first photonic chip designed for a commercial bulk CMOS process (65 nm-node) using standard process layers combined with post-processing, enabling dense photonic integration with high-performance ...

Kaertner, Franz X.

466

South Dakota Gasoline Midgrade Bulk Sales (Volume) by Refiners ...  

U.S. Energy Information Administration (EIA)

South Dakota Gasoline Midgrade Bulk Sales (Volume) by Refiners (Thousand Gallons per Day) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9;

467

Termination of Safeguards on ULWBR Material  

SciTech Connect

The Department of Energy (DOE), Office of Environmental Management, has approved the disposition of 31 metric tons of Unirradiated Light Water Breeder Reactor (ULWBR) material in canisters stored within dry wells of the Underground Fuel Storage Facility at the Idaho Nuclear Technology and Engineering Center (INTEC). This unirradiated material consists primarily of ceramic pellets of thorium oxide in stainless steel cladding, but it also contains 300 kilograms of uranium that is 98 wt% U-233. The ULWBR material was not processed at the INTEC because it was incompatible with prior chemical separation schemes. Other economical recovery options have not been identified, and expressions of interest for consolidating the material with existing projects at other DOE sites have not been received. The U-233 could be used for producing the medical isotope Actinium-225, but the proof-of-principle demonstration and follow-on pilot program have not been developed to the point of requiring production quantities of U-233. Consequently, the selected disposition of the ULWBR material was burial as Low Level Waste at the Nevada Test Site (NTS), which required terminating safeguards controls for the contained Category II quantity of Attractiveness Level D special nuclear material (SNM). The requested termination followed the twelve point evaluation criteria of the Historical Defense Program Discard Guidance and included a security analysis for evaluating the risks of theft, diversion, and radiological sabotage associated with the material. Continuity of knowledge in the book inventory was assured by documenting that the original shipper’s measurements accurately reflected the quantities of materials received and that the ULWBR materials had remained under adequate physical protection and had been subject to periodic physical inventories. The method selected for substantiating the book values as the basis for terminating safeguards was the nondestructive assay used during physical inventories. Shipping arrangements included refurbishing a licensed cask to be reused over the duration of the termination process. An accompanying batching plan and shipping schedule were developed to accommodate multiple commercial shipments of Category III quantities of SNM in the selected cask, such that all canisters would be received at NTS prior to the expiration of the nonrenewable cask license.

Ivan R. Thomas; Ernest L. Laible

2008-07-01T23:59:59.000Z

468

Compositional ordering and stability in nanostructured, bulk thermoelectric alloys.  

SciTech Connect

Thermoelectric materials have many applications in the conversion of thermal energy to electrical power and in solid-state cooling. One route to improving thermoelectric energy conversion efficiency in bulk material is to embed nanoscale inclusions. This report summarize key results from a recently completed LDRD project exploring the science underpinning the formation and stability of nanostructures in bulk thermoelectric and the quantitative relationships between such structures and thermoelectric properties.

Hekmaty, Michelle A.; Faleev, S.; Medlin, Douglas L.; Leonard, F.; Lensch-Falk, J.; Sharma, Peter Anand; Sugar, J. D.

2009-09-01T23:59:59.000Z

469

Bulk viscosity and the conformal anomaly in the pion gas  

E-Print Network (OSTI)

We calculate the bulk viscosity of the massive pion gas within Unitarized Chiral Perturbation Theory. We obtain a low temperature peak arising from explicit conformal breaking due to the pion mass and another peak near the critical temperature, dominated by the conformal anomaly through gluon condensate terms. The correlation between bulk viscosity and conformal breaking supports a recent QCD proposal. We discuss the role of resonances, heavier states and large-$N_c$ counting.

D. Fernandez-Fraile; A. Gomez Nicola

2008-09-26T23:59:59.000Z

470

Finsler geometric perspective on the bulk flow in the universe  

E-Print Network (OSTI)

Astronomical observations showed that there may exist a bulk flow with peculiar velocities in the universe, which contradicts with the (\\Lambda)CDM model. The bulk flow reveals that the observational universe is anisotropic at large scales. In fact, a more reliable observation on the anisotropy of spacetime comes from the CMB power spectra. The WMAP and Planck satellites both show that there is a hemispherical power asymmetry at large-angular scales. In this paper, we propose a "wind" scenario to the bulk flow (or the anisotropy of spacetime). Under the influence of the "wind", the spacetime metric could become a Finsler structure. By resolving the null geodesic equation, we obtain the modified luminosity distance, which has a dipolar form at the leading order. Thus, the "wind" describes well the bulk flow. In addition, we perform a least-(\\chi^2) fit to the data of type Ia supernovae (SNe Ia) in the Union2.1 compilation. The peculiar velocity of the bulk flow has an upper limit (v_{bulk}\\lesssim 4000 \\rm{km/s}), which is compatible with all the existing observational values.

Zhe Chang; Ming-Hua Li; Sai Wang

2013-03-07T23:59:59.000Z

471

Photovoltaic module electrical termination design requirement study. Final report  

DOE Green Energy (OSTI)

Motorola Inc., in conjunction with ITT Cannon, has conducted a study to develop information to facilitate the selection of existing, commercial, electrical termination hardware for photovoltaic modules and arrays. Details of the study are presented in this volume. Module and array design parameters were investigated and recommendations were developed for use in surveying, evaluating, and comparing electrical termination hardware. Electrical termination selection criteria factors were developed and applied to nine generic termination types in each of the four application sectors. Remote, residential, intermediate and industrial. Existing terminations best suited for photovoltaic modules and arrays were identified. Cost information was developed to identify cost drivers and/or requirements which might lead to cost reductions. The general conclusion is that there is no single generic termination that is best suited for photovoltaic application, but that the appropriate termination is strongly dependent upon the module construction and its support structure as well as the specific application sector.

Mosna, F.J. Jr.; Donlinger, J.

1980-07-01T23:59:59.000Z

472

A Probabilistic Bulk Model of Coupled Mixed Layer and Convection. Part I: Clear-Sky Case  

Science Conference Proceedings (OSTI)

A new bulk model of the convective boundary layer, the probabilistic bulk convection model (PBCM), is presented. Unlike prior bulk approaches that have modeled the mixed-layer-top buoyancy flux as a constant fraction of the surface buoyancy flux, ...

Pierre Gentine; Alan K. Betts; Benjamin R. Lintner; Kirsten L. Findell; Chiel C. van Heerwaarden; Alexandra Tzella; Fabio D’Andrea

2013-06-01T23:59:59.000Z

473

Solar Cells: Spin-Cast Bulk Heterojunction Solar Cells: A Dynamical...  

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

Solar Cells: Spin-Cast Bulk Heterojunction Solar Cells: A Dynamical Investigation Solar Cells: Spin-Cast Bulk Heterojunction Solar Cells: A Dynamical Investigation Print Wednesday,...

474

A simulation study for designing a rail terminal in a container port  

Science Conference Proceedings (OSTI)

Rail terminals in port container terminals play an important role for transshipping containers between rail wagons and port container terminals. This paper addresses a case study for designing a new rail terminal which is planned to be constructed in ...

Byung Kwon Lee; Bong Joo Jung; Kap Hwan Kim; Soon Oh Park; Jeong Hoon Seo

2006-12-01T23:59:59.000Z

475

Carbon Capture and Sequestration (via Enhanced Oil Recovery) from a Hydrogen Production Facility in an Oil Refinery  

Science Conference Proceedings (OSTI)

The project proposed a commercial demonstration of advanced technologies that would capture and sequester CO2 emissions from an existing hydrogen production facility in an oil refinery into underground formations in combination with Enhanced Oil Recovery (EOR). The project is led by Praxair, Inc., with other project participants: BP Products North America Inc., Denbury Onshore, LLC (Denbury), and Gulf Coast Carbon Center (GCCC) at the Bureau of Economic Geology of The University of Texas at Austin. The project is located at the BP Refinery at Texas City, Texas. Praxair owns and operates a large hydrogen production facility within the refinery. As part of the project, Praxair would construct a CO2 capture and compression facility. The project aimed at demonstrating a novel vacuum pressure swing adsorption (VPSA) based technology to remove CO2 from the Steam Methane Reformers (SMR) process gas. The captured CO2 would be purified using refrigerated partial condensation separation (i.e., cold box). Denbury would purchase the CO2 from the project and inject the CO2 as part of its independent commercial EOR projects. The Gulf Coast Carbon Center at the Bureau of Economic Geology, a unit of University of Texas at Austin, would manage the research monitoring, verification and accounting (MVA) project for the sequestered CO2, in conjunction with Denbury. The sequestration and associated MVA activities would be carried out in the Hastings field at Brazoria County, TX. The project would exceed DOE’s target of capturing one million tons of CO2 per year (MTPY) by 2015. Phase 1 of the project (Project Definition) is being completed. The key objective of Phase 1 is to define the project in sufficient detail to enable an economic decision with regard to proceeding with Phase 2. This topical report summarizes the administrative, programmatic and technical accomplishments completed in Phase 1 of the project. It describes the work relative to project technical and design activities (associated with CO2 capture technologies and geologic sequestration MVA), and Environmental Information Volume. Specific accomplishments of this Phase include: 1. Finalization of the Project Management Plan 2. Development of engineering designs in sufficient detail for defining project performance and costs 3. Preparation of Environmental Information Volume 4. Completion of Hazard Identification Studies 5. Completion of control cost estimates and preparation of business plan During the Phase 1 detailed cost estimate, project costs increased substantially from the previous estimate. Furthermore, the detailed risk assessment identified integration risks associated with potentially impacting the steam methane reformer operation. While the Phase 1 work identified ways to mitigate these integration risks satisfactorily from an operational perspective, the associated costs and potential schedule impacts contributed to the decision not to proceed to Phase 2. We have concluded that the project costs and integration risks at Texas City are not commensurate with the potential benefits of the project at this time.

Stewart Mehlman

2010-06-16T23:59:59.000Z

476

Automatic Commissioning of Multiple VAV Terminals  

E-Print Network (OSTI)

A site survey on a modern operating commercial building screened 261 ineffective VAV (Variable Air Volume) boxes (20.9% of the total boxes in the building) and summarized ten typical faults for VAV air-conditioning system(s) resulting in energy waste, performance degradation or totally out of control. A strategy is developed to automatically check the health condition of VAV terminals and diagnose the faults. Hybrid approach is employed to establish a commissioning and re-commissioning tool of VAV air-conditioning system. Performance indices with expert rules based on system physical characteristics are adopted to detect and diagnose the nine of the ten faults. PCA (Principal Component Analysis) method is developed to detect and diagnose the VAV box flow sensor bias (Fault 10) and to reconstruct the faulty sensors. A multiple VAV fault FDD strategy for a VAV entire system is developed, which is validated in simulation and filed tests.

Qin, J.; Wang, S.

2004-01-01T23:59:59.000Z

477

Theory Of Alkyl Terminated Silicon Quantum Dots  

DOE Green Energy (OSTI)

We have carried out a series of ab-initio calculations to investigate changes in the optical properties of Si quantum dots as a function of surface passivation. In particular, we have compared hydrogen passivated dots with those having alkyl groups at the surface. We find that, while on clusters with reconstructed surfaces a complete alkyl passivation is possible, steric repulsion prevents full passivation of Si dots with unreconstructed surfaces. In addition, our calculations show that steric repulsion may have a dominant effect in determining the surface structure, and eventually the stability of alkyl passivated clusters, with results dependent on the length of the carbon chain. Alkyl passivation weakly affects optical gaps of silicon quantum dots, while it substantially decreases ionization potentials and electron affinities and affect their excited state properties. On the basis of our results we propose that alkyl terminated quantum dots may be size selected taking advantage of the change in ionization potential as a function of the cluster size.

Reboredo, F; Galli, G

2004-08-19T23:59:59.000Z

478

U.S. Energy Information Administration (EIA)  

Gasoline and Diesel Fuel Update (EIA)

Survey Forms Survey Forms Changes to Petroleum Supply Survey Forms for 2013 Released: November 27, 2012 Federal Register Notice The U.S. Energy Information Administration is requesting comments on the following proposed 2013 Petroleum Supply survey forms: EIA-800, Weekly Refinery and Fractionator Report EIA-801, Weekly Bulk Terminal Report EIA-802, Weekly Product Pipeline Report EIA-803, Weekly Crude Oil Report EIA-804, Weekly Imports Report EIA-805, Weekly Bulk Terminal and Blender Report EIA-809, Weekly Oxygenate Report EIA-22M, Monthly Biodiesel Production Report EIA-810, Monthly Refinery Report EIA-812, Monthly Product Pipeline Report EIA-813, Monthly Crude Oil Report EIA-814, Monthly Imports Report EIA-815, Monthly Bulk Terminal and Blender Report EIA-816, Monthly Natural Gas Plant Liquids Report

479

Rechargeable battery with separate charging terminal contact ring  

SciTech Connect

A generally cylindrical rechargeable battery is provided leaving a pair of power terminals for delivering energy to an energy-using device. The battery further includes a charging terminal contact spaced apart from the power terminals and extending substantially around the circumference of the battery whereby charging contact on the battery may engage a corresponding charging contact in the energy-using device to charge the battery in all rotational positions of the battery.

Beachy, R. W.

1984-12-18T23:59:59.000Z

480

Optical control system for high-voltage terminals  

DOE Patents (OSTI)

An optical control system for the control of devices in the terminal of an electrostatic accelerator includes a laser that is modulated by a series of preselected codes produced by an encoder. A photodiode receiver is placed in the laser beam at the high-voltage terminal of an electrostatic accelerator. A decoder connected to the photodiode decodes the signals to provide control impulses for a plurality of devices at the high voltage of the terminal.

Bicek, John J. (Tinley Park, IL)

1978-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "refinery bulk terminal" 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

High Accuracy Predictions of the Bulk Properties of Water | Argonne  

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

High Accuracy Predictions of the Bulk Properties of Water High Accuracy Predictions of the Bulk Properties of Water High Accuracy Predictions of the Bulk Properties of Water PI Name: Mark Gordon PI Email: mark@si.msg.chem.iastate.edu Institution: Iowa State University Allocation Program: ESP Allocation Hours at ALCF: 150 Million Year: 2010 to 2013 Research Domain: Chemistry Among the ab initio methods, second-order perturbation theory (MP2) predicts highly accurate structures and relative energies for water clusters. Researchers will carry out molecular dynamics simulations of water at the MP2 level. However, full MP2 calculations of even modest-sized water clusters are far too time-consuming for dynamical simulations, even on the next-generation Blue Gene. Therefore, a key element of the current approach will be the use of MP2 in conjunction with the Fragment Molecular

482

Preparation of bulk superhard B-C-N nanocomposite compact  

DOE Patents (OSTI)

Bulk, superhard, B--C--N nanocomposite compacts were prepared by ball milling a mixture of graphite and hexagonal boron nitride, encapsulating the ball-milled mixture at a pressure in a range of from about 15 GPa to about 25 GPa, and sintering the pressurized encapsulated ball-milled mixture at a temperature in a range of from about 1800-2500 K. The product bulk, superhard, nanocomposite compacts were well sintered compacts with nanocrystalline grains of at least one high-pressure phase of B--C--N surrounded by amorphous diamond-like carbon grain boundaries. The bulk compacts had a measured Vicker's hardness in a range of from about 41 GPa to about 68 GPa.

Zhao, Yusheng (Los Alamos, NM); He, Duanwei (Sichuan, CN)

2011-05-10T23:59:59.000Z

483

Phantom dark energy as an effect of bulk viscosity  

E-Print Network (OSTI)

In a homogeneous and isotropic universe bulk viscosity is the unique viscous effect capable to modify the background dynamics. Effects like shear viscosity or heat conduction can only change the evolution of the perturbations. The existence of a bulk viscous pressure in a fluid, which in order to obey to the second law of thermodynamics is negative, reduces its effective pressure. We discuss in this study the degeneracy in bulk viscous cosmologies and address the possibility that phantom dark energy cosmology could be caused by the existence of non-equilibrium pressure in any cosmic component. We establish the conditions under which either matter or radiation viscous cosmologies can be mapped into the phantom dark energy scenario with constraints from multiple observational data-sets

Hermano Velten; Jiaxin Wang; Xinhe Meng

2013-07-16T23:59:59.000Z

484

Analysis of Multi-terminal HVDC Systems Harold Kirkham Pacific...  

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

Analysis of Multi-terminal HVDC Systems Harold Kirkham Pacific Northwest National Laboratory harold.kirkham@pnnl.gov 2728 June 2013 Washington, DC DOEOE Transmission Reliability...

485

The impact on transmission line terminations on radiated emissions.  

E-Print Network (OSTI)

??Terminating transmission lines at either the source or the load end with a damping resistor is frequently used to improve the signal integrity of clock… (more)

Wong, Wei-Juet

2007-01-01T23:59:59.000Z

486

Properties of Bulk Sintered Silver As a Function of Porosity  

SciTech Connect

This report summarizes a study where various properties of bulk-sintered silver were investigated over a range of porosity. This work was conducted within the National Transportation Research Center's Power Device Packaging project that is part of the DOE Vehicle Technologies Advanced Power Electronics and Electric Motors Program. Sintered silver, as an interconnect material in power electronics, inherently has porosity in its produced structure because of the way it is made. Therefore, interest existed in this study to examine if that porosity affected electrical properties, thermal properties, and mechanical properties because any dependencies could affect the intended function (e.g., thermal transfer, mechanical stress relief, etc.) or reliability of that interconnect layer and alter how its performance is modeled. Disks of bulk-sintered silver were fabricated using different starting silver pastes and different sintering conditions to promote different amounts of porosity. Test coupons were harvested out of the disks to measure electrical resistivity and electrical conductivity, thermal conductivity, coefficient of thermal expansion, elastic modulus, Poisson's ratio, and yield stress. The authors fully recognize that the microstructure of processed bulk silver coupons may indeed not be identical to the microstructure produced in thin (20-50 microns) layers of sintered silver. However, measuring these same properties with such a thin actual structure is very difficult, requires very specialized specimen preparation and unique testing instrumentation, is expensive, and has experimental shortfalls of its own, so the authors concluded that the herein measured responses using processed bulk sintered silver coupons would be sufficient to determine acceptable values of those properties. Almost all the investigated properties of bulk sintered silver changed with porosity content within a range of 3-38% porosity. Electrical resistivity, electrical conductivity, thermal conductivity, elastic modulus, Poisson's ratio, and yield stress all depended on the porosity content in bulk-sintered silver. The only investigated property that was independent of porosity in that range was coefficient of thermal expansion.

Wereszczak, Andrew A [ORNL; Vuono, Daniel J [ORNL; Wang, Hsin [ORNL; Ferber, Mattison K [ORNL; Liang, Zhenxian [ORNL

2012-06-01T23:59:59.000Z

487

Physical factors controlling the ductility of bulk metallic glasses  

SciTech Connect

In order to identify key physical factor controlling the deformation and fracture behavior of bulk metallic glasses (BMGs), we compiled and analyzed the elastic moduli and compressive ductility for BMGs. In addition, new modulus data were generated in the critical ranges in order to facilitate the analysis. We have found that the intrinsic ductility of BMGs can be correlated with the bulk-to-shear modulus ratio B/G according to Pugh's [Philos. Mag. 45, 823 (1954) ] rule. In some individual BMG systems, for example, Fe based, the relationship seems to be very clear. The physical meaning of this correlation is discussed in terms of atomic bonding and connectivity.

Liu, Y. [Central South University, China; Liu, Chain T [ORNL; Zhang, Z. [University of Tennessee, Knoxville (UTK); Keppens, V. [University of Tennessee, Knoxville (UTK)

2008-01-01T23:59:59.000Z

488

Nucleation of bulk superconductivity close to critical magnetic field  

E-Print Network (OSTI)

We consider the two-dimensional Ginzburg-Landau functional with constant applied magnetic field. For applied magnetic fields close to the second critical field $H_{C_2}$ and large Ginzburg-Landau parameter, we provide leading order estimates on the energy of minimizing configurations. We obtain a fine threshold value of the applied magnetic field for which bulk superconductivity contributes to the leading order of the energy. Furthermore, the energy of the bulk is related to that of the Abrikosov problem in a periodic lattice. A key ingredient of the proof is a novel $L^\\infty$-bound which is of independent interest.

S. Fournais; A. Kachmar

2009-09-30T23:59:59.000Z

489

Methanol production from eucalyptus wood chips. Attachment III. Florida's eucalyptus energy farm and methanol refinery: the background environment  

DOE Green Energy (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

490

Influence of a combustion-driven oscillation on global mixing in the flame from a refinery flare  

Science Conference Proceedings (OSTI)

An assessment of the influence of strong combustion-driven oscillations on mixing rates and visible radiation in the flame from a full-scale refinery flare is reported. Importantly, the oscillations were generated naturally, with no external forcing, and at a high Reynolds number of 4 x 10{sup 6}. These conditions differentiate this study from those of previous investigations, which all involved some external forcing and were at a Re too low to ensure fully turbulent flow within the flame. A frame-by-frame analysis of video footage, providing good resolution of the instantaneous edge of each flame, was used to assess flame dimensions, and so to determine a global residence time. Since the flames are in the fast-chemistry regime, the visual imagers can be used to determine a global mixing rate. The analysis reveals a consistent picture that the combustion-driven oscillations do not result in a significant change to the global mixing rate, but do increase the visible radiation. This is in contrast to previous investigations, using externally forced jets, where forcing at the preferred mode has been found to increase mixing rates and reduce radiation. (author)

Langman, A.S.; Nathan, G.J. [School of Mechanical Engineering, Centre for Energy Technology, The University of Adelaide, SA 5005 (Australia)

2011-01-15T23:59:59.000Z

491

Effectiveness of in site biodegradation for the remediation of polycyclic aromatic hydrocarbons at a contaminated oil refinery, Port Arthur, Texas  

E-Print Network (OSTI)

The effectiveness of bioremediation for the removal of polycyclic aromatic hydrocarbons (PAHs) from sediments contaminated with highly weathered petroleum was evaluated at a contaminated oil refinery. The sediments were chronically contaminated with crude oil and Bunker C fuel oil for the past 20 years. Two treatments, Inipol EAP-22 (INIPOL) and basic nutrients with indigenous organisms (BNIO), were compared to a control (CONTROL) plot over an 11 week period. In site PAH biodegradation was quantified by plotting the time dependence of PAH to 17?,21?-hopane concentration ratios. 17?,21?-hopane, a nondegradable, C30 triterpane, was used as a natural internal standard. Sediment characterization was performed to determine the effect of geologic conditions on PAH biodegradation rates. Total Ion Chromatograms (TICs) of extracted oil showed high concentrations of an unresolved complex mixture that did not change over the 11 week period. The particle size of the sediments from the plots averaged 51% and 34% for clay and silt content, respectively. Sediment mineralogy was dominated by kaolinite and smectite. [PAH]/[Hopane] ratios indicate no significant PAH degradation in either the INIPOL, BNIO, or CONTROL plots over the 11 week period. This data indicates that bioremediation was unsuccessful at this site due to the extreme weathered state of the oil, the limited bioavailability of the PAH compounds, and the potential toxicity of the petroleum. The use of hopane as a natural internal standard was important in quantifying the effectiveness of bioremediation due to the high spatial variability in initial oil concentrations.

Moffit, Alfred Edward

2000-01-01T23:59:59.000Z

492

Refinery Net Production of Liquefied Refinery Gases  

U.S. Energy Information Administration (EIA)

La. Gulf Coast: 6,043: 6,574: 5,527: 5,960: 5,850: 5,083: 2005-2013: N. La., Ark: 80: 84: 64: 42: 46: 15: 2005-2013: New Mexico: 78: 71: 53: 62: 62: ...

493

PION CONDENSATION IN A FIELD THEORY CONSISTENT WITH BULK PROPERTIES OF NUCLEAR MATTER  

E-Print Network (OSTI)

theory is constrained to reproduce the known bulk properties of nuclear matter, namely its saturation energy,

Banerjee, B.

2013-01-01T23:59:59.000Z

494

Effect of Varying Bulk Viscosity on Generalized Chaplygin Gas  

E-Print Network (OSTI)

In this paper, viscous generalized Chaplygin gas as a model of dark energy considered. We assume non-constant bulk viscous coefficient and study dark energy density. We consider several cases of density-dependent viscosities. We find that, in the special case, the viscous generalized Chaplygin gas is corresponding to modified Chaplygin gas.

Saadat, H

2013-01-01T23:59:59.000Z

495

Effect of Varying Bulk Viscosity on Generalized Chaplygin Gas  

E-Print Network (OSTI)

In this paper, viscous generalized Chaplygin gas as a model of dark energy considered. We assume non-constant bulk viscous coefficient and study dark energy density. We consider several cases of density-dependent viscosities. We find that, in the special case, the viscous generalized Chaplygin gas is corresponding to modified Chaplygin gas.

H. Saadat; B. Pourhassan

2013-05-26T23:59:59.000Z

496

Security-Constrained Adequacy Evaluation of Bulk Power System Reliability  

E-Print Network (OSTI)

Security-Constrained Adequacy Evaluation of Bulk Power System Reliability Fang Yang, Student Member. Stefopoulos, Student Member, IEEE Abstract -- A framework of security-constrained adequacy evaluation (SCAE electric load while satisfying security constraints. It encompasses three main steps: (a) critical

497

ENVIRONMENTAL BIOTECHNOLOGY Effect of bulk liquid BOD concentration on activity  

E-Print Network (OSTI)

to assess the impact of bulk liquid biological oxygen demand (BOD) concentrations on the activity oxygen demand (BOD) for denitrification, are critical for improving current wastewater treatment and Geological Sciences, University of Notre Dame, 156 Fitzpatrick Hall, Notre Dame, IN 46556, USA e

Nerenberg, Robert

498

A Warm-Bin–Cold-Bulk Hybrid Cloud Microphysical Model  

Science Conference Proceedings (OSTI)

This study describes a newly developed bin–bulk hybrid cloud microphysical model named MSSG-Bin, which has been implemented in the Multi-Scale Simulator for the Geoenvironment (MSSG). In the hybrid approach, a spectral bin scheme is used for ...

Ryo Onishi; Keiko Takahashi

2012-05-01T23:59:59.000Z

499

Experiences with bulk SMS for health financing in Uganda  

Science Conference Proceedings (OSTI)

Short message service (SMS, aka text messaging) is a low-cost and effective means of communication for organizations attempting to maintain contact with many people. In this paper we look at the deployment and of a bulk mobile text-messaging platform ... Keywords: braided communications, bulksms, health, ictd, mobile phone, sms

Melissa Densmore

2012-05-01T23:59:59.000Z

500

Columbia River : Terminal Fisheries Research Report : Annual Report 1994.  

DOE Green Energy (OSTI)

In 1993 the Northwest Power Planning Council recommended in its Strategy for Salmon that terminal fishing sites be identified and developed. The Council called on the Bonneville Power Administration to fund a 10-year study to investigate the feasibility of creating and expanding terminal known stock fisheries in the Columbia River Basin.

Hirose, Paul; Miller, Marc; Hill, Jim

1996-12-01T23:59:59.000Z