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Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Lower Atlantic (PADD 1C) Distillate Fuel Oil and Kerosene ...  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 300,889: 274,739: 263,252: 232,429: 230,287: 254,322: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 275,489: ...

2

California Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 309,249: 232,151: 190,082: 225,123: 257,297: 241,967: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 101,932: ...

3

Rocky Mountain (PADD4) Distillate Fuel Oil and Kerosene Sales ...  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 262,644: 222,054: 212,571: 228,200: 245,446: 214,160: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 27: 26: 19: ...

4

Kentucky Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 170,042: 94,124: 48,002: 42,101: 67,347: 61,840: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 91,516: 104,387: ...

5

Pennsylvania Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 118,670: 113,851: 90,800: 124,258: 146,291: 140,663: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 25,735: ...

6

Georgia Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 78,927: 69,710: 62,072: 63,770: 71,374: 63,902: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 14,016: 10,831: ...

7

Illinois Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 40,116: 51,287: 55,322: 72,188: 58,526: 63,808: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 71,805: 101,851: ...

8

Ohio Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 333,069: 316,926: 206,134: 179,048: 203,135: 175,258: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 12,122: ...

9

,"U.S. Total Distillate Fuel Oil and Kerosene Sales by End Use...  

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

Distillate Fuel Oil and Kerosene Sales by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for"...

10

Connecticut Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 314,674: 301,591: 272,255: 271,852: 274,578: 274,507: 1984-2012: ...

11

South Carolina Adjusted Distillate Fuel Oil and Kerosene Sales ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 751,994: 695,077: 654,296: 726,647: 725,148: 655,638: 1984-2012: ...

12

Maryland Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 606,247: 548,583: 540,590: 579,203: 540,843: 531,683: 1984-2012: ...

13

Nebraska Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 446,825: 433,745: 461,938: 639,618: 603,268: 584,362: 1984-2012: ...

14

Massachusetts Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 487,861: 463,886: 443,620: 445,626: 460,154: 444,532: 1984-2012: ...

15

Michigan Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 970,806: 891,487: 819,086: 864,049: 854,644: 877,692: 1984-2012: ...

16

Minnesota Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 804,699: 761,187: 633,806: 665,652: 704,971: 746,974: 1984-2012: ...

17

District of Columbia Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 10,721: 15,894: 11,949: 13,216: 15,149: 15,321: 1984-2012: Residual ...

18

Minnesota Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 817,786: 767,218: 640,572: 678,530: 713,572: 763,303: 1984-2012: ...

19

New Jersey Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 1,088,505: 978,515: 760,035: 831,955: 952,930: 837,191: 1984-2012: ...

20

Wisconsin Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 788,665: 798,348: 703,583: 738,953: 719,417: 780,145: 1984-2012: ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Connecticut Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 314,309: 300,255: 272,598: 271,767: 274,640: 273,827: 1984-2012: ...

22

Kansas Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 581,898: 610,088: 588,362: 554,334: 548,183: 573,992: 1984-2012: ...

23

Michigan Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 964,966: 888,432: 814,460: 855,592: 850,681: 871,756: 1984-2012: ...

24

Delaware Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 68,223: 61,302: 57,382: 56,676: 57,720: 57,230: 1984-2012: Residual ...

25

Nebraska Adjusted Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 448,098: 435,444: 472,303: 689,579: 627,110: 613,232: 1984-2012: ...

26

Utah Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 525,714: 470,714: 420,706: 426,584: 508,266: 486,456: 1984-2012: ...

27

,"U.S. Total Adjusted Distillate Fuel Oil and Kerosene Sales by End Use"  

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

Distillate Fuel Oil and Kerosene Sales by End Use" Distillate Fuel Oil and Kerosene Sales by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Residential",4,"Annual",2012,"6/30/1984" ,"Data 2","Commercial",10,"Annual",2012,"6/30/1984" ,"Data 3","Industrial",9,"Annual",2012,"6/30/1984" ,"Data 4","Farm",4,"Annual",2012,"6/30/1984" ,"Data 5","Electric Power",2,"Annual",2012,"6/30/1984" ,"Data 6","Oil Company",2,"Annual",2012,"6/30/1984"

28

Gulf Coast (PADD 3) Distillate Fuel Oil and Kerosene Sales by ...  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 699,882: 631,796: 542,036: 573,037: 694,053: 729,109: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 613,864: ...

29

New York Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 63,226: 44,510: 35,307: 33,709: 42,254: 35,237: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 12,339: 10,814: ...

30

Florida Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 71,962: 55,219: 35,537: 41,430: 47,283: 61,059: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 140,493: 153,438: ...

31

West Virginia Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Railroad : Distillate Fuel Oil: 15,766: 15,416: 10,143: 11,650: 12,711: 10,456: 1984-2012: Vessel Bunkering : Distillate Fuel Oil: 45,429: 28,568: 99: ...

32

Distillate Fuel Oil Sales for Residential Use  

Annual Energy Outlook 2012 (EIA)

End Use Product: Residential - Distillate Fuel Oil Residential - No. 1 Residential - No. 2 Residential - Kerosene Commercial - Distillate Fuel Oil Commercial - No. 1 Distillate...

33

Alabama Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 979,566: 854,244: 791,004: 859,486: 917,892: 871,796: 1984-2012: ...

34

Arizona Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 877,174: 799,123: 746,952: 751,025: 767,565: 761,995: 1984-2012: ...

35

Rhode Island Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 77,882: 61,856: 59,789: 65,067: 65,295: 62,041: 1984-2012: Residual ...

36

South Carolina Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 752,984: 699,864: 653,641: 726,889: 724,974: 656,396: 1984-2012: ...

37

Utah Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 512,415: 464,448: 420,807: 427,293: 507,559: 486,956: 1984-2012: ...

38

New Jersey Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

Total Transportation (Railroad, Vessel Bunkering, On-Highway) Distillate Fuel Oil: 1,091,896: 991,981: 755,753: 832,806: 951,803: 842,035: 1984-2012: ...

39

,"U.S. Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates"  

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

Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates" Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates",11,"Monthly","9/2013","1/15/1983" ,"Release Date:","12/2/2013" ,"Next Release Date:","1/2/2014" ,"Excel File Name:","pet_cons_refoth_d_nus_vtr_mgalpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_cons_refoth_d_nus_vtr_mgalpd_m.htm"

40

,"U.S. Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates"  

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

Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates" Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. 2 Distillates",11,"Monthly","9/2013","1/15/1983" ,"Release Date:","12/2/2013" ,"Next Release Date:","1/2/2014" ,"Excel File Name:","pet_cons_refoth_d_nus_vwr_mgalpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_cons_refoth_d_nus_vwr_mgalpd_m.htm"

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Table 41. Refiner Volumes of Aviation Fuels, Kerosene, No. 1 ...  

U.S. Energy Information Administration (EIA)

Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel Kerosene No. 1 Distillate Propane ... 51.4 75.5 6,451.9 3,309.5 W 476.2 ...

42

Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils...  

Gasoline and Diesel Fuel Update (EIA)

50. Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene by PAD District and State (Thousand Gallons per Day) Geographic Area Month Kerosene No. 1 Distillate No. 2...

43

Adjusted Distillate Fuel Oil Sales for Residential Use  

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

End Use/ Product: Residential - Distillate Fuel Oil Residential - No. 1 Residential - No. 2 Residential - Kerosene Commercial - Distillate Fuel Oil Commercial - No. 1 Distillate Commercial - No. 2 Distillate Commercial - No. 2 Fuel Oil Commercial - Ultra Low Sulfur Diesel Commercial - Low Sulfur Diesel Commercial - High Sulfur Diesel Commercial - No. 4 Fuel Oil Commercial - Residual Fuel Oil Commercial - Kerosene Industrial - Distillate Fuel Oil Industrial - No. 1 Distillate Industrial - No. 2 Distillate Industrial - No. 2 Fuel Oil Industrial - Low Sulfur Diesel Industrial - High Sulfur Diesel Industrial - No. 4 Fuel Oil Industrial - Residual Fuel Oil Industrial - Kerosene Farm - Distillate Fuel Oil Farm - Diesel Farm - Other Distillate Farm - Kerosene Electric Power - Distillate Fuel Oil Electric Power - Residual Fuel Oil Oil Company Use - Distillate Fuel Oil Oil Company Use - Residual Fuel Oil Total Transportation - Distillate Fuel Oil Total Transportation - Residual Fuel Oil Railroad Use - Distillate Fuel Oil Vessel Bunkering - Distillate Fuel Oil Vessel Bunkering - Residual Fuel Oil On-Highway - No. 2 Diesel Military - Distillate Fuel Oil Military - Diesel Military - Other Distillate Military - Residual Fuel Oil Off-Highway - Distillate Fuel Oil Off-Highway - Distillate F.O., Construction Off-Highway - Distillate F.O., Non-Construction All Other - Distillate Fuel Oil All Other - Residual Fuel Oil All Other - Kerosene Period:

44

Fuel oil and kerosene sales, 1989  

Science Conference Proceedings (OSTI)

Despite the rise in petroleum products prices, a colder-than-normal winter in the latter part of 1989 spurred an increase in demand for distillate fuel oils. The shipping and electric utilities industries contributed to a significant rise in demand for both distillate and residual fuels oils in 1989. A total of 72.9 billion gallons of fuel oil and kerosene were sold to consumers in 1989, an increase of 3.0 percent over 1988 sales volumes. Of all fuel oil sold during 1989, distillate fuel oil accounted for 68.3 percent, which was an increase over 1988 when distillate fuel oil accounted for 67.2 percent of all fuel oil products sold in the United States. Residual fuel oil's share of total fuel oil sold fell slightly to 29.9 percent from 30.7 percent in 1988. Kerosene followed with a 1.8 percent share, also falling from the previous year when it accounted for a 2.1 percent share of total fuel oil sold. 3 figs., 24 tabs.

Not Available

1991-01-22T23:59:59.000Z

45

Fuel oil and kerosene sales 1994  

SciTech Connect

This publication contains the 1994 survey results of the ``Annual Fuel Oil and Kerosene Sales Report`` (Form EIA-821). This is the sixth year that the survey data have appeared in a separate publication. Prior to the 1989 report, the statistics appeared in the Petroleum Marketing Annual (PMA)for reference year 1988 and the Petroleum Marketing Monthly (PMM) for reference years 1984 through 1987. The 1994 edition marks the 11th annual presentation of the results of the ongoing ``Annual Fuel Oil and Kerosene Sales Report`` survey. Distillate and residual fuel oil sales continued to move in opposite directions during 1994. Distillate sales rose for the third year in a row, due to a growing economy. Residual fuel oil sales, on the other hand, declined for the sixth year in a row, due to competitive natural gas prices, and a warmer heating season than in 1993. Distillate fuel oil sales increased 4.4 percent while residual fuel oil sales declined 1.6 percent. Kerosene sales decreased 1.4 percent in 1994.

NONE

1995-09-27T23:59:59.000Z

46

Fuel Oil and Kerosene Sales - Energy Information Administration  

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

Petrolem Reports Petrolem Reports Fuel Oil and Kerosene Sales With Data for 2012 | Release Date: November 15, 2013 | Next Release Date: November 2014 Previous Issues Year: 2012 2011 2010 2009 2008 2007 2006 2005 2004 2003 2002 2001 2000 1999 1998 1997 1996 1995 Go The Fuel Oil and Kerosene Sales 2012 report provides information, illustrations and State-level statistical data on end-use sales of kerosene; No.1, No. 2, and No. 4 distillate fuel oil; and residual fuel oil. State-level kerosene sales include volumes for residential, commercial, industrial, farm, and all other uses. State-level distillate sales include volumes for residential, commercial, industrial, oil company, railroad, vessel bunkering, military, electric utility, farm, on-highway, off-highway construction, and other uses. State-level residual fuel sales

47

Fuel oil and kerosene sales 1995  

Science Conference Proceedings (OSTI)

This publication contains the 1995 survey results of the ``Annual Fuel Oil and Kerosene Sales Report`` (Form EIA-821). This is the seventh year that the survey data have appeared in a separate publication. Except for the kerosene and on-highway diesel information, data presented in Tables 1 through 12 (Sales of Fuel Oil and Kerosene) present results of the EIA-821 survey. Tables 13 through 24 (Adjusted Sales of Fuel Oil and Kerosene) include volumes that are based on the EIA-821 survey but have been adjusted to equal the product supplied volumes published in the Petroleum Supply Annual (PSA). 24 tabs.

NONE

1996-09-01T23:59:59.000Z

48

Idaho Kerosene-Type Jet Fuel Retail Sales by Refiners ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Idaho Kerosene-Type Jet Fuel Refiner Sales Volumes; Idaho Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene, ...

49

Figure HL1. U.S. Sales of Distillate and Residual Fuel Oils by ...  

U.S. Energy Information Administration (EIA)

Sales of Fuel Oil and Kerosene in 2009 . ... the need for electric utilities to consume distillate fuel to meet peak summer generation loads remained ...

50

Table 4. Sales of Distillate Fuel Oil by End Use, 1999 and 2000 ...  

U.S. Energy Information Administration (EIA)

Energy Information Administration 13 Fuel Oil and Kerosene Sales 2000 Table 4. Sales of Distillate Fuel Oil by End Use, 1999 and 2000 (Thousand Gallons)

51

Fuel oil and kerosene sales 1992  

SciTech Connect

This publication contains the 1992 survey results of the ``Annual Fuel Oil and Kerosene Sales Report`` (Form EIA-821). This is the fourth year that the survey data have appeared in a separate publication. Prior to the 1989 report, the statistics appeared in the Petroleum Marketing Annual (PMA) for reference year 1988 and the Petroleum Marketing Monthly (PMM for reference years 1984 through 1987. The 1992 edition marks the ninth annual presentation of the results of the ongoing ``Annual Fuel Oil and Kerosene Sales Report`` survey. Except for the kerosene and on-highway diesel information, data presented in Tables 1 through 12 (Sales of Fuel Oil and Kerosene) present results of the EIA-821 survey. Tables 13 through 24 (Adjusted Sales of Fuel Oil and Kerosene) include volumes that are based on the EIA-821 survey but have been adjusted to equal the products supplied volumes published in the Petroleum Supply Annual (PSA).

Not Available

1993-10-29T23:59:59.000Z

52

Fuel oil and kerosene sales 1993  

Science Conference Proceedings (OSTI)

This publication contains the 1993 survey results of the ``Annual Fuel Oil and Kerosene, Sales Report`` (Form EIA-821). This is the fifth year that the survey data have appeared in a separate publication. Prior to the 1989 report, the statistics appeared in the Petroleum Marketing Annual (PMA) for reference year 1988 and the Petroleum Marketing Monthly (PMM) for reference years 1984 through 1987. The 1993 edition marks the 10th annual presentation of the results of the ongoing ``Annual Fuel Oil and Kerosene Sales Report`` survey. Except for the kerosene and on-highway diesel information, data presented in Tables 1 through 12 (Sales of Fuel Oil and Kerosene) present results of the EIA-821 survey. Tables 13 through 24 (Adjusted Sales of Fuel Oil and Kerosene) include volumes that are based on the EIA-821 survey but have been adjusted to equal the products supplied volumes published in the Petroleum Supply Annual (PSA).

Not Available

1994-10-03T23:59:59.000Z

53

Fuel Oil and Kerosene Sales 2012  

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

Fuel Oil and Kerosene Sales Fuel Oil and Kerosene Sales 2012 November 2013 Independent Statistics & Analysis www.eia.gov U.S. Department of Energy Washington, DC 20585 U.S. Energy Information Administration | Fuel Oil and Kerosene Sales 2012 i 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 U.S. Department of Energy or other federal agencies. U.S. Energy Information Administration | Fuel Oil and Kerosene Sales 2012 1

54

U.S. Exports of Kerosene-Type Jet Fuel (Thousand Barrels per Day)  

U.S. Energy Information Administration (EIA)

Kerosene-Type Jet Fuel Exports; Kerosene-Type Jet Fuel Exports by Destination; Kerosene-Type Jet Fuel Supply and Disposition ...

55

Household Fuel Oil or Kerosene Usage Form  

U.S. Energy Information Administration (EIA)

Contractor’s Street Address . Contractor’s City, State, and ZIP Code . ... is a light distillate fuel oil intended for use in vaporizing pot-type burners.

56

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)

57

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 ...

58

Fuel oil and kerosene sales, 1990  

Science Conference Proceedings (OSTI)

Sales data is presented for kerosene and fuel oils. This is the second year that the survey data have appeared in a separate publication. Prior to the 1989 report, the statistics appeared in the Petroleum Marketing Annual (PMA) for reference year 1988 and the Petroleum Marketing Monthly (PMM) for reference years 1984 through 1987. 4 figs., 24 tabs.

Not Available

1991-10-10T23:59:59.000Z

59

Fuel Oil and Kerosene Sales - Energy Information Administration  

U.S. Energy Information Administration (EIA)

The Fuel Oil and Kerosene Sales 2011 report provides information, illustrations and State-level statistical data on end-use sales of kerosene; No.1, No. 2, and No. 4 ...

60

Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel  

Gasoline and Diesel Fuel Update (EIA)

Gallon Excluding Taxes) - Continued Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel Kerosene Sales to End Users Sales for Resale Sales to End Users Sales for Resale...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

FORM EIA-821 ANNUAL FUEL OIL AND KEROSENE SALES REPORT ...  

U.S. Energy Information Administration (EIA)

An energy-consuming sector that consists of living quarters and ... buildings. EIA-821, Annual Fuel Oil and Kerosene Sales Report Page 3 Commercial Use ...

62

FORM EIA-821 ANNUAL FUEL OIL AND KEROSENE SALES REPORT  

U.S. Energy Information Administration (EIA)

Version No.: 2013.01. FORM EIA-821 ANNUAL FUEL OIL AND KEROSENE SALES REPORT REFERENCE YEAR 2012 ; This report is ; ... 2012 . 10. Type of Report

63

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 ...

64

Arkansas Kerosene-Type Jet Fuel Retail Sales by Refiners (Thousand ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Arkansas Kerosene-Type Jet Fuel Refiner Sales Volumes; Arkansas Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 ...

65

Missouri Kerosene-Type Jet Fuel Wholesale/Resale Volume by ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Kerosene-Type Jet Fuel Sales for Resale Refiner Sales Volumes; Missouri Kerosene-Type Jet Fuel Refiner Sales Volumes; Missouri Sales for Resale ...

66

New Mexico Kerosene-Type Jet Fuel Wholesale/Resale Volume by ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Kerosene-Type Jet Fuel Sales for Resale Refiner Sales Volumes; New Mexico Kerosene-Type Jet Fuel Refiner Sales Volumes; New Mexico Sales for Resale ...

67

South Carolina Kerosene-Type Jet Fuel All Sales/Deliveries by ...  

U.S. Energy Information Administration (EIA)

South Carolina Kerosene-Type Jet Fuel All Sales/Deliveries by Prime Supplier (Thousand Gallons per Day)

68

Table 36. Refiner Prices of Aviation Fuels and Kerosene by PAD ...  

U.S. Energy Information Administration (EIA)

Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel Kerosene Sales to End Users Sales for Resale Sales to ... 102.5 96.1 51.9 53.7 72.9 54.7 Florida

69

U.S. Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene,  

Gasoline and Diesel Fuel Update (EIA)

Sales Type: Sales to End Users Sales for Resale Sales Type: Sales to End Users Sales for Resale Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Product Sales Type Area May-13 Jun-13 Jul-13 Aug-13 Sep-13 Oct-13 View History Aviation Gasoline 93.3 8.2 10.0 12.0 10.9 11.4 1983-2013 Kerosene-Type Jet Fuel 32,893.1 32,452.7 33,281.4 32,532.8 29,876.9 29,004.1 1983-2013 Propane (Consumer Grade) 6,321.3 6,161.4 5,990.4 6,377.7 6,892.8 3,264.5 1983-2013 Kerosene 3.5 2.4 3.6 2.2 3.6 8.8 1983-2013 No. 1 Distillate 45.2 31.9 36.3 32.5 44.6 103.0 1983-2013 No. 2 Distillate 11,266.8 11,311.6 11,647.9 11,375.1 11,192.1 12,138.1 1983-2013 No. 2 Diesel Fuel NA NA NA NA NA NA 1994-2013

70

Sales of Fuel Oil and Kerosene in 2009 - U.S. Energy ...  

U.S. Energy Information Administration (EIA)

Crop Production 2009 Summary, January 2010, page 76. Energy Information Administration Fuel Oil and Kerosene Sales 2009 vii drilling rigs in operation, an important ...

71

U.S. Sales to End Users Refiner Sales Volumes of Aviation Fuels, Kerosene,  

Gasoline and Diesel Fuel Update (EIA)

103.5 144.3 150.9 116.6 117.5 101.0 1983-2012 103.5 144.3 150.9 116.6 117.5 101.0 1983-2012 Kerosene-Type Jet Fuel 40,136.3 39,913.9 37,954.6 34,775.2 33,272.0 32,545.7 1983-2012 Propane (Consumer Grade) 3,263.4 2,672.2 3,671.1 3,871.2 4,457.3 5,556.4 1983-2012 Kerosene 139.7 46.0 39.8 30.3 27.1 21.0 1983-2012 No. 1 Distillate 161.0 102.0 100.9 107.8 108.9 108.5 1983-2012 No. 2 Distillate 24,345.6 20,801.6 17,757.7 15,767.1 13,802.1 12,536.7 1983-2012 No. 2 Diesel Fuel NA NA NA NA NA NA 1994-2012 Ultra Low-Sulfur 12,415.9 12,419.4 12,458.2 11,698.0 10,441.1 10,608.9 2007-2012 Low-Sulfur 7,720.2 6,037.6 3,392.4 3,186.1 2,579.3 1,185.4 1994-2012 High-Sulfur 3,419.6 1,403.5 1,028.3 448.8 402.0 427.5 1994-2012 No. 2 Fuel Oil 789.9 941.0 878.9 434.2 379.7 314.9

72

New Jersey No 1 Distillate Wholesale/Resale Volume by ...  

U.S. Energy Information Administration (EIA)

Referring Pages: New Jersey No. 1 Distillate Refiner Sales Volumes; New Jersey Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene, ...

73

U.S. Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene,  

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 Aviation Gasoline 413.1 602.6 593.2 547.1 431.5 432.6 1983-2013 Kerosene-Type Jet Fuel 26,119.1 27,197.0 28,168.9 27,226.7 25,645.0 27,379.5 1983-2013 Propane (Consumer Grade) 26,164.7 24,627.2 25,506.9 30,382.5 31,250.8 38,981.9 1983-2013 Kerosene 1,302.3 897.9 1,049.8 1,199.7 1,224.4 1,318.9 1983-2013 No. 1 Distillate 197.2 124.8 141.7 228.9 336.0 947.3 1983-2013 No. 2 Distillate 148,472.9 149,527.5 153,402.1 152,957.9 149,298.1 160,704.2 1983-2013 No. 2 Diesel Fuel NA NA NA NA NA NA 1994-2013 Ultra Low-Sulfur 140,589.9 143,645.5 145,899.9 142,352.7 139,922.9 151,092.7 2007-2013 Low-Sulfur 1,976.7 1,020.9 2,521.9 2,944.3 2,205.9 3,904.5 1994-2013 High-Sulfur

74

Distillation of liquid fuels by thermogravimetry  

Science Conference Proceedings (OSTI)

In this paper, design and operation of a custom-built thermogravimetric apparatus for the distillation of liquid fuels are reported. Using a sensitive balance with scale of 0.001 g and ASTM distillation glassware, several petroleum and petroleum-derived samples have been analyzed by the thermogravimetric distillation method. When the ASTM distillation glassware is replaced by a micro-scale unit, sample size could be reduced from 100 g to 5-10 g. A computer program has been developed to transfer the data into a distillation plot, e.g. Weight Percent Distilled vs. Boiling Point. It also generates a report on the characteristic distillation parameters, such as, IBP (Initial Boiling Point), FBP (Final Boiling Point), and boiling point at 50 wt% distilled. Comparison of the boiling point distributions determined by TG (thermogravimetry) with those by SimDis GC (Simulated-Distillation Gas Chromatography) on two liquid fuel samples (i.e. a decanted oil and a filtered crude oil) are also discussed in this paper.

Huang, He; Wang, Keyu; Wang, Shaojie; Klein, M.T.; Calkins, W.H.

1996-12-31T23:59:59.000Z

75

U.S. Product Supplied of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Product Supplied of Kerosene-Type Jet Fuel (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: 295,460 ...

76

U.S. Exports to Italy of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Exports to Italy of Kerosene-Type Jet Fuel (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2005: 2: 2008: 23: 9: 18: 2009: 89: 2010: 10 ...

77

New Jersey Kerosene-Type Jet Fuel All Sales/Deliveries by Prime ...  

U.S. Energy Information Administration (EIA)

New Jersey Kerosene-Type Jet Fuel All Sales/Deliveries by Prime Supplier (Thousand Gallons per Day) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8

78

U.S. Kerosene-Type Jet Fuel All Sales/Deliveries by Prime Supplier ...  

U.S. Energy Information Administration (EIA)

U.S. Kerosene-Type Jet Fuel All Sales/Deliveries by Prime Supplier (Thousand Gallons per Day) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1983: 30,535.1 ...

79

Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene...  

Annual Energy Outlook 2012 (EIA)

824.7 684.2 24,433.3 85,531.2 19,553.6 105,084.8 129,518.1 429.2 131,456.3 July ... 924.3 684.5 23,436.9 87,740.4 20,605.7...

80

Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene...  

Annual Energy Outlook 2012 (EIA)

13,621.8 279.0 14,394.5 1996 Average ... 321.0 6.9 7,031.4 2,531.9 241.1 2,772.9 9,804.4 200.0 10,332.3 Connecticut January ......

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

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)

82

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)

83

,"Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes"  

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

Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes" Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes",60,"Monthly","9/2013","1/15/1983" ,"Release Date:","12/2/2013" ,"Next Release Date:","1/2/2014" ,"Excel File Name:","pet_cons_refoth_a_epjk_vtr_mgalpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_cons_refoth_a_epjk_vtr_mgalpd_m.htm" ,"Source:","Energy Information Administration"

84

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 ...

85

U.S. Imports of Kerosene-Type Jet Fuel, Bonded (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

U.S. Imports of Kerosene-Type Jet Fuel, Bonded (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: 1,406: 1,620: 1,231: 1,388: 1,379: 1,456 ...

86

,,"Distillate Fuel Oil(b)",,,"Alternative Energy Sources(c)"  

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

9 Relative Standard Errors for Table 10.9;" " Unit: Percents." ,,"Distillate Fuel Oil(b)",,,"Alternative Energy Sources(c)" ,,,"Coal Coke" "NAICS"," ","Total","...

87

,,"Distillate Fuel Oil",,,"Alternative Energy Sources(b)"  

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

8 Relative Standard Errors for Table 10.8;" " Unit: Percents." ,,"Distillate Fuel Oil",,,"Alternative Energy Sources(b)" ,,,"Coal Coke" "NAICS"," ","Total","...

88

"Table A10. Total Consumption of LPG, Distillate Fuel Oil, and Residual Fuel"  

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

0. Total Consumption of LPG, Distillate Fuel Oil, and Residual Fuel" 0. Total Consumption of LPG, Distillate Fuel Oil, and Residual Fuel" " Oil for Selected Purposes by Census Region and Economic Characteristics of the" " Establishment, 1991" " (Estimates in Barrels per Day)" ,,,," Inputs for Heat",,," Primary Consumption" " "," Primary Consumption for all Purposes",,," Power, and Generation of Electricity",,," for Nonfuel Purposes",,,"RSE" ," ------------------------------------",,," ------------------------------------",,," -------------------------------",,,"Row" "Economic Characteristics(a)","LPG","Distillate(b)","Residual","LPG","Distillate(b)","Residual","LPG","Distillate(b)","Residual","Factors"

89

Utah Kerosene Wholesale/Resale Volume by Refiners (Thousand ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Kerosene Sales for Resale Refiner Sales Volumes; Utah Kerosene Refiner Sales Volumes; Utah Sales for Resale Refiner Sales Volumes of Aviation Fuels ...

90

Idaho Kerosene Wholesale/Resale Volume by Refiners (Thousand ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Idaho Kerosene Refiner Sales Volumes; Idaho Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene, Propane, No.1 and No. ...

91

U.S. Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

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

Area: U.S. East Coast (PADD 1) New England (PADD 1A) Connecticut Maine Massachusetts New Hampshire Rhode Island Vermont Central Atlantic (PADD 1B) Delaware District of Columbia Maryland New Jersey New York Pennsylvania Lower Atlantic (PADD 1C) Florida Georgia North Carolina South Carolina Virginia West Virginia Midwest (PADD 2) Illinois Indiana Iowa Kansas Kentucky Michigan Minnesota Missouri Nebraska North Dakota Ohio Oklahoma South Dakota Tennessee Wisconsin Gulf Coast (PADD 3) Alabama Arkansas Louisiana Mississippi New Mexico Texas Rocky Mountain (PADD 4) Colorado Idaho Montana Utah Wyoming West Coast (PADD 5) Alaska Arizona California Hawaii Nevada Oregon Washington Period:

92

U.S. Distillate Fuel Oil and Kerosene Sales by End Use  

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

Area: U.S. East Coast (PADD 1) New England (PADD 1A) Connecticut Maine Massachusetts New Hampshire Rhode Island Vermont Central Atlantic (PADD 1B) Delaware District of Columbia Maryland New Jersey New York Pennsylvania Lower Atlantic (PADD 1C) Florida Georgia North Carolina South Carolina Virginia West Virginia Midwest (PADD 2) Illinois Indiana Iowa Kansas Kentucky Michigan Minnesota Missouri Nebraska North Dakota Ohio Oklahoma South Dakota Tennessee Wisconsin Gulf Coast (PADD 3) Alabama Arkansas Louisiana Mississippi New Mexico Texas Rocky Mountain (PADD 4) Colorado Idaho Montana Utah Wyoming West Coast (PADD 5) Alaska Arizona California Hawaii Nevada Oregon Washington Period:

93

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1 Distillate,  

Gasoline and Diesel Fuel Update (EIA)

34.7 34.7 428.4 46,539.7 12,728.4 790.3 6,200.2 648.4 4,283.7 3,323.4 44,204.9 February ......................... 151.1 456.7 46,811.8 13,168.9 661.0 5,865.0 639.0 3,498.4 4,030.8 40,811.0 March .............................. 155.1 534.1 47,764.0 11,796.0 685.4 3,081.1 347.2 1,274.9 2,912.8 32,094.6 April ................................ 181.4 632.9 48,092.4 12,418.7 309.0 1,382.4 162.4 425.7 2,671.8 27,292.6 May ................................. 194.0 730.2 48,978.1 11,174.4 288.0 868.9 122.3 240.3 2,628.8 22,213.6 June ................................ 184.4 739.6 50,091.3 10,034.5 424.7 571.0 151.7 314.2 2,237.4 23,117.3 July ................................. 205.9 830.4 50,287.4 11,139.2 226.4 714.5 145.1 261.5 2,057.6 25,037.3 August ............................ 200.2 854.8 50,327.4 11,706.4 202.7 1,112.1

94

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1 Distillate,  

Gasoline and Diesel Fuel Update (EIA)

4.2 4.2 406.0 45,968.1 11,079.0 534.5 5,366.3 833.9 4,675.6 3,248.9 44,872.7 February ......................... 146.6 499.8 47,800.3 10,256.4 357.8 3,591.8 621.7 2,731.9 3,684.2 38,357.8 March .............................. 150.3 518.6 48,152.6 10,316.6 365.5 2,056.1 336.2 1,114.2 3,284.7 28,091.6 April ................................ 171.8 592.8 49,135.3 9,493.8 287.9 1,335.2 199.7 438.4 3,352.9 25,786.2 May ................................. 172.2 665.1 49,770.4 9,886.7 249.2 1,017.4 176.2 314.9 2,935.6 24,783.5 June ................................ 175.3 759.4 52,048.3 10,834.1 192.7 754.0 194.4 360.2 2,313.9 24,285.6 July ................................. 239.2 853.3 51,725.7 10,840.4 136.7 1,348.8 199.7 362.4 2,083.2 26,581.1 August ............................ 201.6 810.9 52,026.8 12,609.7 241.1 1,226.9

95

Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene  

Gasoline and Diesel Fuel Update (EIA)

048.9 048.9 3,882.7 43,253.5 78,544.5 20,983.0 99,527.5 142,781.0 1,215.1 152,927.6 February ............................. 4,331.5 2,419.0 42,453.9 81,957.0 20,781.0 102,737.9 145,191.8 1,145.6 153,087.9 March .................................. 3,374.8 1,616.3 38,313.8 87,940.5 21,866.1 109,806.6 148,120.5 1,062.2 154,173.8 April .................................... 1,699.2 728.2 28,122.4 90,081.2 20,288.6 110,369.8 138,492.2 639.3 141,558.9 May ..................................... 1,294.6 643.7 22,565.9 88,582.4 20,702.3 109,284.6 131,850.5 482.9 134,271.8 June .................................... 1,675.6 579.4 23,580.9 96,532.1 21,436.8 117,968.9 141,549.8 385.0 144,189.9 July ..................................... 1,577.3 605.1 22,198.4 92,096.8 21,709.0 113,805.8 136,004.2 656.0 138,842.6

96

Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene by PAD District and State  

Gasoline and Diesel Fuel Update (EIA)

7,583.7 7,583.7 5,086.5 57,988.5 72,118.7 20,784.9 92,903.6 150,892.1 2,271.3 165,833.6 February ............................. 7,190.5 4,192.4 55,685.0 76,234.8 22,030.8 98,265.6 153,950.6 2,265.8 167,599.4 March .................................. 3,741.4 1,832.9 42,789.1 78,746.7 20,513.7 99,260.4 142,049.5 1,644.7 149,268.5 April .................................... 1,759.1 694.2 33,643.2 85,180.7 21,967.4 107,148.0 140,791.2 1,157.8 144,402.3 May ..................................... 1,029.0 473.8 25,651.8 83,213.2 21,779.5 104,992.8 130,644.5 661.5 132,808.8 June .................................... 1,148.6 527.8 23,238.7 83,513.2 21,394.3 104,907.5 128,146.2 536.4 130,359.0 July ..................................... 868.0 541.3 22,987.0 82,742.6 20,917.3 103,659.8 126,646.8 517.0 128,573.1

97

,"U.S. Total Adjusted Distillate Fuel Oil and Kerosene Sales...  

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

"Back to Contents","Data 10: On-Highway" "Sourcekey","K2DVAHNUS1" "Date","U.S. No 2 Diesel Adj SalesDeliveries to On-Highway Consumers (Thousand Gallons)" 30863,16797423...

98

Idaho Adjusted Distillate Fuel Oil and Kerosene Sales by End Use  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Totals may not equal ...

99

Catalytic hydroprocessing of shale oil to produce distillate fuels  

DOE Green Energy (OSTI)

Results are presented of a Chevron Research Company study sponsored by the Energy Research and Development Administration (ERDA) to demonstrate the feasibility of converting whole shale oil to a synthetic crude resembling a typical petroleum distillate. The synthetic crude thus produced can then be processed, in conventional petroleum-refining facilities, to transportation fuels such as high octane gasoline, diesel, and jet fuel. The raw shale oil feed used is a typical Colorado shale oil produced in a surface retort in the so-called indirectly heated mode. It is shown that whole shale oil can be catalytically hydrodenitrified to reduce the nitrogen to levels as low as one part per million in a single catalytic stage. However, for economic reasons, it appears preferable to denitrify to about 0.05 wt % nitrogen. The resulting synthetic crude resembles a petroleum distillate that can be fractionated and further processed as necessary in conventional petroleum refining facilities. Shale oil contains about 0.6% sulfur. Sulfur is more easily removed by hydrofining than is nitrogen; therefore, only a few parts per million of sulfur remain at a product nitrogen of 0.05 wt %. Oxygen contained in the shale oil is also reduced to low levels during hydrodenitrification. The shale oil contains appreciable quantities of iron and arsenic which are also potential catalyst poisons. These metals are removed by a guard bed placed upstream from the hydrofining catalyst. Based on correlations, the naphthas from the shale oil hydrofiner can readily be upgraded to high octane gasolines by catalytic reforming. The middle distillate fractions may require some additional hydrofining to produce salable diesel or jet fuel. The technology is available, and pilot plant studies are scheduled to verify diesel hydrofiner performance.

Sullivan, R.F.; Stangeland, B.E.

1977-01-01T23:59:59.000Z

100

Table 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil...  

Annual Energy Outlook 2012 (EIA)

342.8 W W 123.0 412.7 W 839.2 135.0 1,251.9 See footnotes at end of table. 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil Volumes by PAD District and State Energy...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Table 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil...  

Gasoline and Diesel Fuel Update (EIA)

116.7 W W W W 379.0 W 1,039.3 132.9 1,418.3 See footnotes at end of table. 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil Volumes by PAD District and State Energy...

102

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)

103

Distillate Fuel Oil Assessment for Winter 1996-1997  

Gasoline and Diesel Fuel Update (EIA)

following Energy Information Administration sources: Weekly following Energy Information Administration sources: Weekly Petroleum Status Report, DOE/EIA-0208(96-39); Petroleum Supply Monthly, September 1996, DOE/EIA-0109(96/09); Petroleum Supply Annual 1995, DOE/EIA-0340(95); Petroleum Marketing Monthly, September 1996, DOE/EIA-0380(96/09); Short-Term Energy Outlook, DOE/EIA-0202(96/4Q) and 4th Quarter 1996 Short-Term Integrated Forecasting System; and an address by EIA Administrator Jay E. Hakes on the Fall 1996 Heating Fuel Assessment before the National Association of State Energy Officials, September 16, 1996. Table FE1. Distillate Fuel Oil Demand and Supply Factors, Winter (October - March) 1993-94 Through 1996-97 History STEO Mid Case Factor Winter Winter Winter Winter 1993-94

104

Distillate Fuel Oil Imports Could Be Available - For A Price  

Gasoline and Diesel Fuel Update (EIA)

4 4 Notes: So it wasn't demand and production explains only part of the reason we got through last winter with enough stocks. The mystery is solved when you look at net imports of distillate fuel last winter. As we found out, while imports are a small contributor to supply, they are sometimes crucial. Last winter, imports were the main source of supply increase following the price spike. Previous record levels were shattered as imports came pouring into the country. The fact that Europe was enjoying a warmer-than-normal winter also encouraged exports to the United States. It was massive amounts of imports, particularly from Russia, that helped us get through last winter in as good a shape as we did. Imports are expected to be relatively normal this winter. Added imports

105

Microchannel Distillation of JP-8 Jet Fuel for Sulfur Content Reduction  

Science Conference Proceedings (OSTI)

In microchannel based distillation processes, thin vapor and liquid films are contacted in small channels where mass transfer is diffusion-limited. The microchannel architecture enables improvements in distillation processes. A shorter height equivalent of a theoretical plate (HETP) and therefore a more compact distillation unit can be achieved. A microchannel distillation unit was used to produce a light fraction of JP-8 fuel with reduced sulfur content for use as feed to produce fuel-cell grade hydrogen. The HETP of the microchannel unit is discussed, as well as the effects of process conditions such as feed temperature, flow rate, and reflux ratio.

Zheng, Feng; Stenkamp, Victoria S.; TeGrotenhuis, Ward E.; Huang, Xiwen; King, David L.

2006-09-16T23:59:59.000Z

106

Midwest Gasoline and Distillate Fuel Near-Term Outlook  

U.S. Energy Information Administration (EIA)

Additionally, the August shutdown of the crude oil distillation unit at the Citgo refinery in Lemont, Illinois due to fire has reduced local production capacity, ...

107

Refiner/marketer targets production of transportation fuels and distillates  

Science Conference Proceedings (OSTI)

Citgo Petroleum Corp., the wholly owned subsidiary of Petroleos de Venezuela, S.A. (PDVSA), the Venezuelan national oil company, owns two gasoline producing refineries, a 305,000-b/d system in Lake Charles, La., and a 130,000-b/d facility in Corpus Christi, Texas. Each is considered a deep conversion facility capable of converting heavy, sour crudes into a high percentage of transportation fuels and distillates. Two smaller refineries, one in Paulsboro, N.J., and one in Savannah, GA., have the capacity to process 40,000 b/d and 28,000 b/d of crude, respectively, for asphalt products. In the past two years, Citgo`s light oils refineries operated safely and reliably with a minimum of unscheduled shutdowns. An ongoing emphasis to increase reliability has resulted in extended run lengths at the refineries. Citgo has invested $314 million at its facilities in 1995, much of this toward environmental and regulatory projects, such as the new waste water treatment unit at the Lake Charles refinery. Over the next few years, Citgo expects to complete $1.5 billion in capital spending for major processing units such as a 60,000-b/d FCC feed hydrotreater unit at the Lake Charles refinery and crude expansion at the Corpus Christi refinery. Product exchanges and expanded transport agreements are allowing Citgo to extend its marketing reach.

Thompson, J.E.

1997-01-01T23:59:59.000Z

108

U.S. Product Supplied of Distillate Fuel Oil (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

View History: Monthly Annual : Download Data (XLS File) U.S. Product Supplied of Distillate Fuel Oil (Thousand Barrels) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov

109

U.S. distillate fuel exports continue to grow - Today in ...  

U.S. Energy Information Administration (EIA)

U.S. exports of distillate fuel (which includes diesel) reached a record 656,000 barrels per day (bbl/d) in 2010 and have grown every year since 2003.

110

,"U.S. Total Adjusted Sales of Distillate Fuel Oil by End Use...  

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

,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Total Adjusted Sales of Distillate Fuel Oil by End Use",13,"Annual",2012,"6301984"...

111

Distillate Fuel Oil Assessment for Winter 1995-1996  

Gasoline and Diesel Fuel Update (EIA)

U.S. Refining Capacity Utilization U.S. Refining Capacity Utilization by Tancred Lidderdale, Nancy Masterson, and Nicholas Dazzo* U.S. crude oil refinery utilization rates have steadily increased since oil price and allocation decontrol in 1981. The annual average atmospheric distillation utilization rate has increased from 68.6 percent of operable capacity in 1981 to 92.6 percent in 1994. The distillation utilization rate reached a peak of 96.4 percent in August 1994, the highest one-month average rate in over 20 years. This dramatic increase in refining capacity utilization has stimulated a growing interest in the ability of U.S. refineries to supply domestic requirements for finished petroleum products. This article briefly reviews recent trends in domestic refining capacity utilization and examines in detail the differences in

112

Composition-explicit distillation curves of aviation fuel JP-8 and a coal-based jet fuel  

Science Conference Proceedings (OSTI)

We have recently introduced several important improvements in the measurement of distillation curves for complex fluids. The modifications to the classical measurement provide for (1) a composition explicit data channel for each distillate fraction (for both qualitative and quantitative analysis); (2) temperature measurements that are true thermodynamic state points; (3) temperature, volume, and pressure measurements of low uncertainty suitable for an equation of state development; (4) consistency with a century of historical data; (5) an assessment of the energy content of each distillate fraction; (6) a trace chemical analysis of each distillate fraction; and (7) a corrosivity assessment of each distillate fraction. The most significant modification is achieved with a new sampling approach that allows precise qualitative as well as quantitative analyses of each fraction, on the fly. We have applied the new method to the measurement of rocket propellant, gasoline, and jet fuels. In this paper, we present the application of the technique to representative batches of the military aviation fuel JP-8, and also to a coal-derived fuel developed as a potential substitute. We present not only the distillation curves but also a chemical characterization of each fraction and discuss the contrasts between the two fluids. 26 refs., 5 figs., 6 tabs.

Beverly L. Smith; Thomas J. Bruno [National Institute of Standards and Technology, Boulder, CO (United States). Physical and Chemical Properties Division

2007-09-15T23:59:59.000Z

113

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

114

Life cycle assessment of off-grid lighting applications : kerosene vs. solar lanterns  

E-Print Network (OSTI)

Access to electricity in developing countries is minimal and if available, often unreliable. As a result, fuel-based kerosene lighting is the most common solution to lighting necessities. However, kerosene combustion affects ...

Dave, Shreya H

2008-01-01T23:59:59.000Z

115

,,"Distillate Fuel Oil(b)",,,"Alternative Energy Sources(c)"  

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

0.9 Relative Standard Errors for Table 10.9;" 0.9 Relative Standard Errors for Table 10.9;" " Unit: Percents." ,,"Distillate Fuel Oil(b)",,,"Alternative Energy Sources(c)" ,,,,,,,,,,"Coal Coke" "NAICS"," ","Total"," ","Not","Electricity","Natural","Residual",,,"and" "Code(a)","Subsector and Industry","Consumed(d)","Switchable","Switchable","Receipts(e)","Gas","Fuel Oil","Coal","LPG","Breeze","Other(f)" ,,"Total United States" 311,"Food",8,15,9,21,19,18,0,27,0,41 311221," Wet Corn Milling",0,0,0,0,0,0,0,0,0,0

116

Fuel-blending stocks from the hydrotreatment of a distillate formed by direct coal liquefaction  

SciTech Connect

The direct liquefaction of coal in the iron-catalyzed Suplex process was evaluated as a technology complementary to Fischer-Tropsch synthesis. A distinguishing feature of the Suplex process, from other direct liquefaction processes, is the use of a combination of light- and heavy-oil fractions as the slurrying solvent. This results in a product slate with a small residue fraction, a distillate/naphtha mass ratio of 6, and a 65.8 mass % yield of liquid fuel product on a dry, ash-free coal basis. The densities of the resulting naphtha (C{sub 5}-200{sup o}C) and distillate (200-400{sup o}C) fractions from the hydroprocessing of the straight-run Suplex distillate fraction were high (0.86 and 1.04 kg/L, respectively). The aromaticity of the distillate fraction was found to be typical of coal liquefaction liquids, at 60-65%, with a Ramsbottom carbon residue content of 0.38 mass %. Hydrotreatment of the distillate fraction under severe conditions (200{sup o}C, 20.3 MPa, and 0.41 g{sub feed} h{sup -1} g{sub catalyst}{sup -1}) with a NiMo/Al{sub 2}O{sub 3} catalyst gave a product with a phenol content of {lt}1 ppm, a nitrogen content {lt}200 ppm, and a sulfur content {lt}25 ppm. The temperature was found to be the main factor affecting diesel fraction selectivity when operating at conditions of WHSV = 0.41 g{sub feed} h{sup -1} g{sub catalyst}{sup -1} and PH{sub 2} = 20.3 MPa, with excessively high temperatures (T {gt} 420{sup o}C) leading to a decrease in diesel selectivity. The fuels produced by the hydroprocessing of the straight-run Suplex distillate fraction have properties that make them desirable as blending components, with the diesel fraction having a cetane number of 48 and a density of 0.90 kg/L. The gasoline fraction was found to have a research octane number (RON) of 66 and (N + 2A) value of 100, making it ideal as a feedstock for catalytic reforming and further blending with Fischer-Tropsch liquids. 44 refs., 9 figs., 12 tabs.

Andile B. Mzinyati [Sasol Technology Research and Development, Sasolburg (South Africa). Fischer-Tropsch Refinery Catalysis

2007-09-15T23:59:59.000Z

117

Conversion to Dual Fuel Capability in Combustion Turbine Plants: Addition of Distillate Oil Firing for Combined Cycles  

Science Conference Proceedings (OSTI)

During development of combined cycle projects, key assumptions and estimates regarding markets and technology on which the project is based may change. With fuel costs of combined cycle plants representing over 90 percent of annual operating cost, sudden changes in fuel pricing demand attention and re-evaluation. Conversion from natural gas fuel only to dual fuel capability with the addition of distillate oil firing systems is a technical response to market conditions that may have long-term as well as s...

2001-09-26T23:59:59.000Z

118

On the Development of a Distillation Process for the Electrometallurgical Treatment of Irradiated Spent Nuclear Fuel  

Science Conference Proceedings (OSTI)

As part of the spent fuel treatment program at the Idaho National Laboratory, a vacuum distillation process is being employed for the recovery of actinide products following an electrorefining process. Separation of the actinide products from a molten salt electrolyte and cadmium is achieved by a batch operation called cathode processing. A cathode processor has been designed and developed to efficiently remove the process chemicals and consolidate the actinide products for further processing. This paper describes the fundamentals of cathode processing, the evolution of the equipment design, the operation and efficiency of the equipment, and recent developments at the cathode processor. In addition, challenges encountered during the processing of irradiated spent nuclear fuel in the cathode processor will be discussed.

B.R. Westphal; K.C. Marsden; J.C. Price; D.V. Laug

2008-04-01T23:59:59.000Z

119

Atmospheric Crude Oil Distillation Operable Capacity  

Gasoline and Diesel Fuel Update (EIA)

(Barrels per Calendar Day) (Barrels per Calendar Day) 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:

120

Recovery of Navy distillate fuel from reclaimed product. Volume II. Literature review  

SciTech Connect

In an effort to assist the Navy to better utilize its waste hydrocarbons, NIPER, with support from the US Department of Energy, is conducting research designed to ultimately develop a practical technique for converting Reclaimed Product (RP) into specification Naval Distillate Fuel (F-76). This first phase of the project was focused on reviewing the literature and available information from equipment manufacturers. The literature survey has been carefully culled for methodology applicable to the conversion of RP into diesel fuel suitable for Navy use. Based upon the results of this study, a second phase has been developed and outlined in which experiments will be performed to determine the most practical recycling technologies. It is realized that the final selection of one particular technology may be site-specific due to vast differences in RP volume and available facilities. A final phase, if funded, would involve full-scale testing of one of the recommended techniques at a refueling depot. The Phase I investigations are published in two volumes. Volume 1, Technical Discussion, includes the narrative and Appendices I and II. Appendix III, a detailed Literature Review, includes both a narrative portion and an annotated bibliography containing about 800 references and abstracts. This appendix, because of its volume, has been published separately as Volume 2.

Brinkman, D.W.; Whisman, M.L.

1984-11-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Winter Distillate  

Gasoline and Diesel Fuel Update (EIA)

5 5 Notes: Throughout the summer, gasoline prices have drawn most of the public's attention, but EIA has been concerned over winter heating fuels as well. q Distillate inventories are likely to begin the winter heating season at low levels, which increases the chances of price volatility such as that seen last winter. q Natural gas does not look much better. q Winter Distillate http://www.eia.doe.gov/pub/oil_gas/petroleum/presentati...00/winter_distillate_and_natural_gas_outlook/sld001.htm [8/10/2000 4:35:57 PM] Slide 2 of 25 Notes: Residential heating oil prices on the East Coast (PADD 1) were 39 cents per gallon higher this June than last year (120 v 81 cents per gallon). As many of you already know, the increase is due mainly to increased crude oil prices.

122

Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

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

123

1 DISTILLERS BY-PRODUCTS AND CORN STOVER AS FUELS FOR ETHANOL PLANTS  

E-Print Network (OSTI)

Abstract. Dry-grind ethanol plants have the potential to reduce their operating costs and improve their net energy balances by using biomass as the source of process heat and electricity. We utilized ASPEN PLUS software to model various technology bundles of equipment, fuels and operating activities that are capable of supplying energy and satisfying emissions requirements for dry-grind ethanol plants of 50 and 100 million gallons per year capacity using corn stover, distillers dried grains and solubles (DDGS), or a mixture of corn stover and “syrup ” (the solubles portion of DDGS). In addition to their own requirements, plants producing 50 and 100 million gallons of ethanol are capable of supplying 5-7 or 10-14 MegaWatts of electricity to the grid, respectively. Economic analysis showed favorable rates of return for biomass alternatives compared to conventional plants using natural gas and purchased electricity over a range of conditions. The mixture of corn stover and syrup provided the highest rates of return in general. Factors favoring biomass included a higher premium for low carbon footprint ethanol, higher natural gas prices, lower DDGS prices, lower ethanol

Douglas G. Tiffany; R. Vance Morey; Matt De Kam; Douglas G. Tiffany; R. Vance Morey; Matt De Kam

2008-01-01T23:59:59.000Z

124

,"U.S. Total Adjusted Sales of Distillate Fuel Oil by End Use...  

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

SalesDeliveries to Vessel Bunker Consumers (Thousand Gallons)","U.S. No 2 Diesel Adj SalesDeliveries to On-Highway Consumers (Thousand Gallons)","U.S. Total Distillate Adj...

125

Pelleting and characterization of dry distillers' grain with solubles pellets as bio-fuel .  

E-Print Network (OSTI)

??Bio fuels are made from an extensive selection of fuels derived from biomass, including wood waste, agricultural wastes, and alcohol fuels. As a result of… (more)

Saha, Suparna

2011-01-01T23:59:59.000Z

126

U.S. Distillate Market  

Gasoline and Diesel Fuel Update (EIA)

Market Regional Residential Heating Oil Prices Retail Diesel Fuel Oil Prices Crude Oil Price Cycles Spot Distillate & Crude Oil Prices.(Prices through March 3, 2000) Low...

127

Black Carbon and Kerosene Lighting: An Opportunity for Rapid Action on Climate Change and Clean Energy for Development  

Science Conference Proceedings (OSTI)

Replacing inefficient kerosene lighting with electric lighting or other clean alternatives can rapidly achieve development and energy access goals, save money and reduce climate warming. Many of the 250 million households that lack reliable access to electricity rely on inefficient and dangerous simple wick lamps and other kerosene-fueled light sources, using 4 to 25 billion liters of kerosene annually to meet basic lighting needs. Kerosene costs can be a significant household expense and subsidies are expensive. New information on kerosene lamp emissions reveals that their climate impacts are substantial. Eliminating current annual black carbon emissions would provide a climate benefit equivalent to 5 gigatons of carbon dioxide reductions over the next 20 years. Robust and low-cost technologies for supplanting simple wick and other kerosene-fueled lamps exist and are easily distributed and scalable. Improving household lighting offers a low-cost opportunity to improve development, cool the climate and reduce costs.

Jacobson, Arne [Humboldt State Univ., MN (United States). Schatz Energy Research Center; Bond, Tami C. [Univ. of Illinois at Urbana-Champaign, IL (United States). Dept. of Civil and Environmental Engineering; Lam, Nicholoas L. [Univ. of California, Berkeley, CA (United States). Dept. of Environmental Health Sciences; Hultman, Nathan [The Brookings Institution, Washington, DC (United States)

2013-04-15T23:59:59.000Z

128

Soft Sensing Based on LS-SVM and Its Application to a Distillation Column  

Science Conference Proceedings (OSTI)

Dry point of aviation kerosene in the atmospheric distillation column is a very important process value for quality controlling. But unfortunately few on-line hardware sensors are available to this value or such sensors are difficult to maintain. This ...

Yafen Li; Qi Li; Huijuan Wang; Ningsheng Ma

2006-10-01T23:59:59.000Z

129

Prime Supplier Sales Volumes of Total Distillate and Kerosene  

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

158,110.5 153,279.5 150,543.5 150,826.0 154,151.9 151,155.6 158,110.5 153,279.5 150,543.5 150,826.0 154,151.9 151,155.6 1983-2013 East Coast (PADD 1) 45,616.9 39,584.9 37,386.4 37,249.3 38,108.9 40,198.6 1983-2013 New England (PADD 1A) 7,083.6 5,358.2 4,555.3 4,567.5 4,734.9 5,447.0 1983-2013 Connecticut 1,603.8 1,148.9 910.2 889.6 964.7 1,155.0 1983-2013 Maine 1,265.6 1,082.5 977.7 1,002.5 996.8 1,198.0 1983-2013 Massachusetts 2,233.0 1,639.5 1,372.6 1,377.2 1,415.8 1,509.8 1983-2013 New Hampshire 812.5 588.7 497.7 491.5 480.2 607.0 1983-2013 Rhode Island 656.7 518.7 450.0 478.7 499.4 548.0 1983-2013 Vermont 512.0 379.7 347.0 328.0 378.0 429.1 1983-2013 Central Atlantic (PADD 1B) 18,767.7 14,932.6 14,136.2 14,447.3 14,730.4 16,140.3 1983-2013 Delaware 259.8 215.9 200.5 302.1 236.3 296.3 1983-2013

130

Catalytic Distillation  

E-Print Network (OSTI)

Catalytic Distillation' refers to a chemical process which performs both a catalyzed reaction and primary fractionation of the reaction components simultaneously. A structured catalyst which also is an effective distillation component has been patented by Chemical Research & Licensing Co., Houston, Texas, and developed in a joint venture with Neochem Corp., Houston, Texas, and the Department of Energy. The catalytic distillation packing has been commercially demonstrated successfully with nearly three years continuous service for an acid catalyzed reaction in a carbon steel distillation tower.

Smith, L. A., Jr.; Hearn, D.; Wynegar, D. P.

1984-01-01T23:59:59.000Z

131

A techno-economic and environmental assessment of hydroprocessed renewable distillate fuels  

E-Print Network (OSTI)

This thesis presents a model to quantify the economic costs and environmental impacts of producing fuels from hydroprocessed renewable oils (HRO) process. Aspen Plus was used to model bio-refinery operations and supporting ...

Pearlson, Matthew Noah

2011-01-01T23:59:59.000Z

132

Combustion of EDS mid-distillate and refined shale-oil residual fuel in a gas turbine with large single-combustion chamber  

DOE Green Energy (OSTI)

The test fuels included a coal derived mid distillate recycle liquid from the EDS coal liquefaction process, produced by Exxon, and a hydroprocessed residual Paraho shale oil fraction originating from a US Government sponsored program. A BBC (Brown Boveri Co.) type 9 fully equipped 35 MW capacity gas turbine, located at BBC's test facilities near Basel, Switzerland, was utilized. The objective of the combustion test was to establish whether these alternate fuels can be fired in large single combustor turbines without deleterious effects to the turbine or environment. Nitrogen in the shale oil was on the order of 0.4 wt% while the EDS distillate contained slightly less than 10 wt% hydrogen. The test program entailed the firing of 600 barrels of each test fuel at varying turbine loads and a comparison of the results with those from a base case petroleum diesel fuel. Fuel bound nitrogen was not found to contribute significantly to NO/sub x/ emissions in contrast to other work reported earlier in subscale gas turbine tests. Water injection at 0.6 to 0.7 water-fo-fuel mass ratios was effective in meeting EPA requirements for NO/sub x/ emissions from the diesel, shale and coal derived fuels at full turbine load. Low fuel hydrogen content did not cause any operational or emission problems. Combustor wall temperature, the major problem with low hydrogen fuels, rose only slightly within acceptable limits.

Not Available

1983-01-01T23:59:59.000Z

133

U.S. Distillate Inventory Outlook  

Gasoline and Diesel Fuel Update (EIA)

When EIA's demand forecast is combined with its outlook for production and net imports, distillate stocks are projected to remain low for the rest of the year. - Distillate fuel...

134

Vacuum Distillation  

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

Day) Process: Vacuum Distillation Thermal Cracking Thermal Cracking: Coking Thermal Cracking: Delayed Coking Thermal Cracking: Fluid Coking Thermal Cracking: Visbreaking Thermal...

135

Distillate Stocks Expected  

Gasoline and Diesel Fuel Update (EIA)

4 4 Notes: So let's get to what you want to know. What do we expect this upcoming winter? When EIA's demand forecast is combined with its outlook for production and net imports, distillate stocks are projected to remain towards the lower end of the normal range. We are forecasting about an 11 million barrel build between the end of July 2001 and the end of November 2001, slightly more than the average over the past 5 years (10 million barrels), but less than the average of the last 10 years (15 ½ million barrels). If, however, economic incentives are high enough, distillate stocks could build more, resulting in a higher distillate stock level heading into the winter. Of course, the reverse is true as well, if for example, the distillate fuel refining spread declines substantially. Since 1994,

136

Geothermal Energy Market Study on the Atlantic Coastal Plain: Technical Feasibility of use of Eastern Geothermal Energy in Vacuum Distillation of Ethanol Fuel  

DOE Green Energy (OSTI)

The DOE is studying availability, economics, and uses of geothermal energy. These studies are being conducted to assure maximum cost-effective use of geothermal resources. The DOE is also aiding development of a viable ethanol fuel industry. One important point of the ethanol program is to encourage use of non-fossil fuels, such as geothermal energy, as process heat to manufacture ethanol. Geothermal waters available in the eastern US tend to be lower in temperature (180 F or less) than those available in the western states (above 250 F). Technically feasible use of eastern geothermal energy for ethanol process heat requires use of technology that lowers ethanol process temperature requirements. Vacuum (subatmospheric) distillation is one such technology. This study, then, addresses technical feasibility of use of geothermal energy to provide process heat to ethanol distillation units operated at vacuum pressures. They conducted this study by performing energy balances on conventional and vacuum ethanol processes of ten million gallons per year size. Energy and temperature requirements for these processes were obtained from the literature or were estimated (for process units or technologies not covered in available literature). Data on available temperature and energy of eastern geothermal resources was obtained from the literature. These data were compared to ethanol process requirements, assuming a 150 F geothermal resource temperature. Conventional ethanol processes require temperatures of 221 F for mash cooking to 240 F for stripping. Fermentation, conducted at 90 F, is exothermic and requires no process heat. All temperature requirements except those for fermentation exceed assumed geothermal temperatures of 150 F. They assumed a 130 millimeter distillation pressure for the vacuum process. It requires temperatures of 221 F for mash cooking and 140 F for distillation. Data indicate lower energy requirements for the vacuum ethanol process (30 million BTUs per hour) than for the conventional process (36 million BTUs per hour). Lower energy requirements result from improved process energy recovery. Data examined in this study indicate feasible use of eastern geothermal heated waters (150 F) to provide process heat for vacuum (130 mm Hg) ethanol distillation units. Data indicate additional heat sources are needed to raise geothermal temperatures to the 200 F level required by mash cooking. Data also indicate potential savings in overall process energy use through use of vacuum distillation technology. Further study is needed to confirm conclusions reached during this study. Additional work includes obtaining energy use data from vacuum ethanol distillation units currently operating in the 130 millimeter pressure range; economic analysis of different vacuum pressures to select an optimum; and operation of a pilot geothermally heated vacuum column to produce confirmatory process data.

None

1981-04-01T23:59:59.000Z

137

Distillate Demand Strong Last Winter  

Gasoline and Diesel Fuel Update (EIA)

4 Notes: Well, distillate fuel demand wasn't the reason that stocks increased in January 2001 and kept prices from going higher. As you will hear shortly, natural gas prices spiked...

138

Kerosene-Type Jet Fuel Net Production  

U.S. Energy Information Administration (EIA)

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

139

Stocks of Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

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

140

Exports of Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: RBOB with Ether and RBOB ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Kerosene-Type Jet Fuel Exports  

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 exports are ...

142

U.S. Distillate Market  

Gasoline and Diesel Fuel Update (EIA)

diesel and heating fuel prices diesel and heating fuel prices surged. The largest increases occurred in the distillate-based fuels (heating oil and diesel) in the Northeast. The main factors driving up these prices were low stocks leading into January, followed by a bout of severe weather that impacted both supply and demand. Warmer weather and the arrival of new supply, mainly imports, relieved the supply/demand imbalance and brought prices back down. The spike is now behind us, but high crude prices are keeping prices above year-ago levels. The low stock situation that set the stage for the distillate price spike was not unique to the United States, Low stocks exist worldwide and are not limited to distillate. The low stock situation stems from what is happening in the crude oil markets. A crude oil supply shortage drove crude

143

Table 5. Kerosene Consumption and Expenditures in U.S. Households ...  

U.S. Energy Information Administration (EIA)

1 A small amount of kerosene used for water heating and appliances is included in "Kerosene" under "All Uses." (*) ...

144

Table A3. Refiner/Reseller Prices of Distillate and Residual...  

Gasoline and Diesel Fuel Update (EIA)

Fuel Oils, by PAD District, 1983-Present (Cents per Gallon Excluding Taxes) Geographic Area Year No. 1 Distillate No. 2 Distillate a No. 4 Fuel b Residual Fuel Oil Sales to End...

145

Weekly U.S. Exports of Total Distillate (Thousand Barrels ...  

U.S. Energy Information Administration (EIA)

Weekly U.S. Exports of Total Distillate (Thousand Barrels per Day) Year-Month Week 1 Week 2 Week 3 ... Exports of Distillate Fuel Oil ; U.S. Imports ...

146

U.S. Distillate Inventory Outlook  

Gasoline and Diesel Fuel Update (EIA)

As of December 29, distillate fuel oil stocks were about 116 million As of December 29, distillate fuel oil stocks were about 116 million barrels, which is over 14 percent below their 5 year average for this time of year. Heating oil stocks were at 47.4 million barrels, or about 28 percent lower than their seasonal 5-year average. If the currently depressed level of distillate stocks continues, the result could be strong upward pressure on prices for the distillate fuels through the winter. Recently, the tightness in distillate markets, particularly in the Northeast, has worsened and left the heating oil market more vulnerable to near-term shocks from potential cold weather events or disruptions in the logistical system than was expected earlier this fall. Unless the second half of the winter in the Northeast is unusually

147

Heating Fuel Comparision Calculator - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

HEAT CONTENT PRICES INSTRUCTIONS CALCULATOR Fuel Heat Content Per Unit (Btu) Fuel Type Electricity Propane Kerosene Gallon Cord Ton AFUE Natural Gas COP Geothermal ...

148

A GUIDE TO FUEL PERFORMANCE  

Science Conference Proceedings (OSTI)

Heating oil, as its name implies, is intended for end use heating consumption as its primary application. But its identity in reference name and actual chemical properties may vary based on a number of factors. By name, heating oil is sometimes referred to as gas oil, diesel, No. 2 distillate (middle distillate), or light heating oil. Kerosene, also used as a burner fuel, is a No. 1 distillate. Due to the higher heat content and competitive price in most markets, No. 2 heating oil is primarily used in modern, pressure-atomized burners. Using No. 1 oil for heating has the advantages of better cold-flow properties, lower emissions, and better storage properties. Because it is not nearly as abundant in supply, it is often markedly more expensive than No. 2 heating oil. Given the advanced, low-firing rate burners in use today, the objective is for the fuel to be compatible and achieve combustion performance at the highest achievable efficiency of the heating systems--with minimal service requirements. Among the Oil heat industry's top priorities are improving reliability and reducing service costs associated with fuel performance. Poor fuel quality, fuel degradation, and contamination can cause burner shut-downs resulting in ''no-heat'' calls. Many of these unscheduled service calls are preventable with routine inspection of the fuel and the tank. This manual focuses on No. 2 heating oil--its performance, properties, sampling and testing. Its purpose is to provide the marketer, service manager and technician with the proper guidelines for inspecting the product, maintaining good fuel quality, and the best practices for proper storage. Up-to-date information is also provided on commercially available fuel additives, their appropriate use and limitations.

LITZKE,W.

2004-08-01T23:59:59.000Z

149

U.S. Distillate Market  

Gasoline and Diesel Fuel Update (EIA)

U.S. diesel and heating fuel U.S. diesel and heating fuel prices surged. The largest increases occurred in the distillate-based fuels (heating oil and diesel) in the Northeast. From January 17, New England residential heating oil prices rose over 78 cents per gallon to average $1.97 February 7; diesel increased 68 cents per gallon, averaging $2.12 February 7. Prices for both fuels began to fall back by February 14 as new supplies were arriving, and have continued to decline since. The main factors driving up these prices were low stocks leading into January, followed by a bout of severe weather that impacted both supply and demand. Demand: Cold weather increases core heating customer demand. In addition, it was reported that utilities were buying distillate both for peaking power and, along with industrial and commercial users, to

150

U.S. Distillate Inventory Outlook  

U.S. Energy Information Administration (EIA)

These low inventories will put upward pressure on distillate fuel prices and set the stage for price sun-ups should there be an extended period of cold weather or a ...

151

U.S. Distillate Inventory Outlook  

Gasoline and Diesel Fuel Update (EIA)

7 7 Notes: Total distillate stocks rose only marginally in November, to about 117 million barrels from about 115 million barrels at the end of October. The "normal" or average inventory level at end November is 146 million barrels. Thus, by the end of November, instead of seeing an improvement, US distillate inventories were 30 million barrels less than normal rather than the 26 million barrels less as of the end of October, indicating greater tightness in markets for heating oil and diesel fuel. If the currently depressed level of distillate stocks continues, the result could be strong upward pressure on prices for the distillate fuels through the winter. In fact, the tightness in distillate markets, particularly in the Northeast, has worsened and left the heating oil market more vulnerable

152

U.S. Distillate Inventory Outlook  

Gasoline and Diesel Fuel Update (EIA)

9 9 Notes: At the end of December, distillate fuel oil stocks were about 116 million barrels, which is more than 14 percent below their 5-year average for this time of year, and about 7 percent less than last year's low levels. As of January 19, the most recent weekly data, distillate stocks remained at about that level, which is slightly higher than a year ago. If the currently depressed level of distillate stocks continues, the result could be strong upward pressure on prices for the distillate fuels through the winter. Recently, the tightness in distillate markets, particularly in the Northeast, has worsened and left the heating oil market more vulnerable to near-term shocks from potential cold weather events or disruptions in the logistical system than was expected earlier this fall.

153

Catalytic distillation structure  

DOE Patents (OSTI)

Catalytic distillation structure for use in reaction distillation columns, a providing reaction sites and distillation structure and consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and being present with the catalyst component in an amount such that the catalytic distillation structure consist of at least 10 volume % open space.

Smith, Jr., Lawrence A. (Bellaire, TX)

1984-01-01T23:59:59.000Z

154

Distillate in Depth - The Supply, Demand, and Price Picture  

Reports and Publications (EIA)

The presentation provides background on distillate supply and demand, and then focuses on how hurricanes Katrina and Rita impact on refining capacity might affect winter fuels.

Information Center

2005-10-12T23:59:59.000Z

155

Complementarity, distillable secret key, and distillable entanglement  

E-Print Network (OSTI)

We consider controllability of two conjugate observables Z and X by two parties with classical communication. The ability is specified by two alternative tasks, (i) agreement on Z and (ii) preparation of an eigenstate of X with use of an extra communication channel. We prove that their feasibility is equivalent to that of key distillation if the extra channel is quantum, and to that of entanglement distillation if it is classical. This clarifies the distinction between two entanglement measures, distillable key and distillable entanglement.

Masato Koashi

2007-04-27T23:59:59.000Z

156

New Jersey No. 2 Fuel Oil Wholesale/Resale Volume by ...  

U.S. Energy Information Administration (EIA)

Referring Pages: New Jersey No. 2 Fuel Oil Refiner Sales Volumes; New Jersey Sales for Resale Refiner Sales Volumes of Aviation Fuels, Kerosene, ...

157

Table SH2. Total Households by Space Heating Fuels Used, 2005 ...  

U.S. Energy Information Administration (EIA)

Total Households by Space Heating Fuels Used, 2005 ... 2005 Residential Energy Consumption Survey: ... Electricity Natural Gas Fuel Oil Kerosene LPG Other

158

Spot Distillate & Crude Oil Prices  

U.S. Energy Information Administration (EIA)

Retail distillate prices follow the spot distillate markets, and crude oil prices have been the main driver behind distillate spot price increases until recently.

159

U.S. Distillate Market  

Gasoline and Diesel Fuel Update (EIA)

Slide 1 of 11 Notes: During the second half of January, diesel and heating fuel prices surged. The largest increases occurred in the distillate-based fuels (heating oil and diesel) in the Northeast. From January 17, New England residential heating oil prices rose over 78 cents per gallon to average $1.97 February 7; diesel increased 68 cents per gallon, averaging $2.12 February 7, but fell back to $1.93 by February 14 as new supplies are arriving. The main factors driving up these prices were low stocks leading into January, followed by a bout of severe weather that impacted both supply and demand. Demand: Cold weather increases core heating customer demand. In addition, it was reported that utilities were buying distillate both for peaking power and, along with industrial and commercial users, to

160

April 2012 sets U.S. monthly record for distillate net exports ...  

U.S. Energy Information Administration (EIA)

In response to global demand growth, wholesale prices for distillate fuels have generally been high in recent years compared to prices for other fuels.

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Catalytic distillation structure  

DOE Patents (OSTI)

Catalytic distillation structure is described for use in reaction distillation columns, and provides reaction sites and distillation structure consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and is present with the catalyst component in an amount such that the catalytic distillation structure consists of at least 10 volume % open space. 10 figs.

Smith, L.A. Jr.

1984-04-17T23:59:59.000Z

162

Year/PAD District Distillation Crude Oil Atmospheric Distillation  

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

Distillation Crude Oil Atmospheric Distillation Vacuum Cracking Thermal Catalytic Cracking Fresh Recycled Catalytic Hydro- Cracking Catalytic Reforming Desulfurization...

163

Catalytic dewaxing of middle distillates  

SciTech Connect

The fractionation and stripping equipment of a middle distillate catalytic dewaxing unit may be eliminated by integrating the catalytic dewaxing unit with a catalytic cracking unit. The light cycle oil sidestream from the cat cracker fractionator, bypasses the sidestream stripper and serves as the feed to the catalytic dewaxing unit. The dewaxed product is separated into a gasoline fraction which is recycled for fractionation in the cat cracker fractionator and a fuel oil fraction which is recycled to the cat cracker sidestream stripper for removal of light materials to produce a low pour fuel oil meeting product specifications.

Antal, M.J.

1982-06-01T23:59:59.000Z

164

State energy fuel prices by major economic sector from 1960 through 1977  

SciTech Connect

The state energy fuel prices are described and displayed by major economic sector for 1960 to 1977. These prices support the Regional Energy Demand Model. The 7 major fuel commodities in the Price Data System fall into two groups: petroleum products (distillate, residual, kerosene, gasoline, and liquid petroleum gas) and non-petroleum product fuels (electric power and natural gas). The methodology for calculating each commodity is shown. A detailed description of the wholesale and retail price methodology is presented. Appendices A and B display the price series in calorific and physical units, respectively. Some data-supporting tables are presented in Appendix C and Appendix D describes the fuel identifiers for decoding information in Appendices A and B.

Galliker, J.P.

1979-07-01T23:59:59.000Z

165

Table 8.5d Consumption of Combustible Fuels for ...  

U.S. Energy Information Administration (EIA)

biomass. Through 2000, also includes non-renewable waste ... (CHP) and commercial electricity-only plants. 4 Jet fuel, kerosene, other petroleum ...

166

OFF-HIGHWAY TRANSPORTATION-RELATED FUEL USE  

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

Highway Administration FOKS Fuel Oil and Kerosene Sales GGE gasoline gallons equivalent LNG liquid natural gas LPG liquid petroleum gas MBPD million barrels per day MPH miles per...

167

Engineering-Scale Distillation of Cadmium for Actinide Recovery  

Science Conference Proceedings (OSTI)

During the recovery of actinide products from spent nuclear fuel, cadmium is separated from the actinide products by a distillation process. Distillation occurs in an induction-heated furnace called a cathode processor capable of processing kilogram quantities of cadmium. Operating parameters have been established for sufficient recovery of the cadmium based on mass balance and product purity. A cadmium distillation rate similar to previous investigators has also been determined. The development of cadmium distillation for spent fuel treatment enhances the capabilities for actinide recovery processes.

J.C. Price; D. Vaden; R.W. Benedict

2007-10-01T23:59:59.000Z

168

Stocks of Distillate Fuel Oil  

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

Weekly Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area 11/08/13 11/15/13 11/22/13 11/29/13 12/06/13 12/13/13 View History U.S. 117,336 112,541 110,875 113,524 118,065 115,955 1982-2013 PADD 1 37,188 36,279 34,646 36,139 37,685 36,450 1990-2013 New England 7,437 7,125 7,429 7,213 6,570 6,143 1990-2013 Central Atlantic 18,363 17,955 17,103 18,219 19,488 19,010 1990-2013 Lower Atlantic 11,388 11,198 10,114 10,707 11,626 11,297 1990-2013 PADD 2 25,135 24,663 24,159 24,955 25,979 25,894 1990-2013 PADD 3 38,487 35,470 36,422 36,720 37,292 36,874 1990-2013 PADD 4 3,499 3,423 3,401 3,548 3,733 3,789 1990-2013 PADD 5

169

Imports of Distillate Fuel Oil  

U.S. Energy Information Administration (EIA)

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

170

Distillate Fuel Oil Net Production  

U.S. Energy Information Administration (EIA)

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

171

Stocks of Distillate Fuel Oil  

U.S. Energy Information Administration (EIA)

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

172

Imports of Distillate Fuel Oil  

Annual Energy Outlook 2012 (EIA)

226 130 97 158 211 85 1982-2013 East Coast (PADD 1) 173 126 92 153 209 75 2004-2013 Midwest (PADD 2) 7 1 0 0 0 1 2004-2013 Gulf Coast (PADD 3) 44 0 0 0 0 0 2004-2013 Rocky Mountain...

173

Distillate Market Model documentation report  

SciTech Connect

The purpose of this report is to define the objectives of the Distillate Market Model (DMM), describe its basic approach, and to provide details on model functions. This report is intended as a reference document for model analysts, users, and the general public. Documentation of the model is in accordance with EIA`s legal obligation to provide adequate documentation in support of its models. The DMM performs a short-term (6- to 9-month) forecast of demand and retail price for distillate fuel oil in the national US market; it also calculates the end-of-month stock level during the term of the forecast. The model is used to analyze certain market behavior assumptions or shocks and to determine the effect on retail market price, demand, and stock level.

1993-12-01T23:59:59.000Z

174

Random multiparty entanglement distillation  

E-Print Network (OSTI)

We describe various results related to the random distillation of multiparty entangled states - that is, conversion of such states into entangled states shared between fewer parties, where those parties are not predetermined. In previous work [Phys. Rev. Lett. 98, 260501 (2007)] we showed that certain output states (namely Einstein-Podolsky-Rosen (EPR) pairs) could be reliably acquired from a prescribed initial multipartite state (namely the W state) via random distillation that could not be reliably created between predetermined parties. Here we provide a more rigorous definition of what constitutes ``advantageous'' random distillation. We show that random distillation is always advantageous for W-class three-qubit states (but only sometimes for Greenberger-Horne-Zeilinger (GHZ)-class states). We show that the general class of multiparty states known as symmetric Dicke states can be readily converted to many other states in the class via random distillation. Finally we show that random distillation is provab...

Fortescue, Ben

2007-01-01T23:59:59.000Z

175

Multipartite nonlocality distillation  

Science Conference Proceedings (OSTI)

The stronger nonlocality than that allowed in quantum theory can provide an advantage in information processing and computation. Since quantum entanglement is distillable, can nonlocality be distilled in the nonsignalling condition? The answer is positive in the bipartite case. In this article the distillability of the multipartite nonlocality is investigated. We propose a distillation protocol solely exploiting xor operations on output bits. The probability-distribution vectors and matrix are introduced to tackle the correlators. It is shown that only the correlators with extreme values can survive the distillation process. As the main result, the amplified nonlocality cannot maximally violate any Bell-type inequality. Accordingly, a distillability criterion in the postquantum region is proposed.

Hsu, Li-Yi; Wu, Keng-Shuo [Department of Physics, Chung Yuan Christian University, Chungli 32023, Taiwan (China)

2010-11-15T23:59:59.000Z

176

Michigan Kerosene Adj Sales/Deliveries to Residential Consumers ...  

U.S. Energy Information Administration (EIA)

Michigan Kerosene Adj Sales/Deliveries to Residential Consumers (Thousand Gallons) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's:

177

Illinois Kerosene Sales/Deliveries to Residential Consumers ...  

U.S. Energy Information Administration (EIA)

Illinois Kerosene Sales/Deliveries to Residential Consumers (Thousand Gallons) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's ...

178

Distillate and Spot Crude Oil Prices  

Gasoline and Diesel Fuel Update (EIA)

5 5 Notes: This slide shows the strong influence crude oil prices have on retail distillate prices. The price for distillate fuel oil tracks the crude price increases seen in 1996 and the subsequent fall in 1997 and 1998. Distillate prices have also followed crude oil prices up since the beginning of 1999. Actual data show heating oil prices on the East Coast in June at $1.20 per gallon, up 39 cents over last June. However, if heating oil prices are following diesel, they may be up another 5 cents in August. That would put heating oil prices about 40 cents over last August prices. Crude oil prices are only up about 25 cents in August over year ago levels. The extra 15 cents represents improved refiner margins due in part to the very low distillate inventory level.

179

Fuel.vp  

Annual Energy Outlook 2012 (EIA)

Table F7: Distillate Fuel Oil Consumption Estimates, 2011 State Residential Commercial Industrial Transportation Electric Power Total Residential Commercial Industrial...

180

Eclipse Distilled (Eclipse)  

Science Conference Proceedings (OSTI)

Eclipse DistilledDavid CarlsonForeword by Grady BoochSeries EditorsErich Gamma Lee Nackman John WiegandA Concise Introduction to Eclipse for the Productive ProgrammerOrganized for rapid access, focused on productivity, Eclipse Distilled brings together ...

David Carlson

2005-02-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Catalytic distillation process  

DOE Patents (OSTI)

A method for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C.sub.4 feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

Smith, Jr., Lawrence A. (Bellaire, TX)

1982-01-01T23:59:59.000Z

182

Catalytic distillation process  

DOE Patents (OSTI)

A method is described for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C[sub 4] feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

Smith, L.A. Jr.

1982-06-22T23:59:59.000Z

183

International Energy Statistics  

U.S. Energy Information Administration (EIA)

Motor Gasoline: Jet Fuel: Kerosene: Distillate Fuel Oil: Residual Fuel Oil: Liquefied Petroleum Gases: Other Products: Total: North America 622.131

184

International Energy Statistics  

U.S. Energy Information Administration (EIA)

Motor Gasoline: Jet Fuel: Kerosene: Distillate Fuel Oil: Residual Fuel Oil: Liquefied Petroleum Gases: Other Products: Total: World 22,069.0 5,219.8

185

International Energy Statistics - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

Motor Gasoline: Jet Fuel: Kerosene: Distillate Fuel Oil: Residual Fuel Oil: Liquefied Petroleum Gases: Other Products: Total: United States 141.822

186

International Energy Statistics - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Motor Gasoline: Jet Fuel: Kerosene: Distillate Fuel Oil: Residual Fuel Oil: Liquefied Petroleum Gases: Other Products: Total: United States 9,252.5

187

International Energy Statistics - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Motor Gasoline: Jet Fuel: Kerosene: Distillate Fuel Oil: Residual Fuel Oil: Liquefied Petroleum Gases: Other Products: Total: United States 412.649

188

Advanced Distillation Final Report  

Science Conference Proceedings (OSTI)

The Advanced Distillation project was concluded on December 31, 2009. This U.S. Department of Energy (DOE) funded project was completed successfully and within budget during a timeline approved by DOE project managers, which included a one year extension to the initial ending date. The subject technology, Microchannel Process Technology (MPT) distillation, was expected to provide both capital and operating cost savings compared to conventional distillation technology. With efforts from Velocys and its project partners, MPT distillation was successfully demonstrated at a laboratory scale and its energy savings potential was calculated. While many objectives established at the beginning of the project were met, the project was only partially successful. At the conclusion, it appears that MPT distillation is not a good fit for the targeted separation of ethane and ethylene in large-scale ethylene production facilities, as greater advantages were seen for smaller scale distillations. Early in the project, work involved flowsheet analyses to discern the economic viability of ethane-ethylene MPT distillation and develop strategies for maximizing its impact on the economics of the process. This study confirmed that through modification to standard operating processes, MPT can enable net energy savings in excess of 20%. This advantage was used by ABB Lumus to determine the potential impact of MPT distillation on the ethane-ethylene market. The study indicated that a substantial market exists if the energy saving could be realized and if installed capital cost of MPT distillation was on par or less than conventional technology. Unfortunately, it was determined that the large number of MPT distillation units needed to perform ethane-ethylene separation for world-scale ethylene facilities, makes the targeted separation a poor fit for the technology in this application at the current state of manufacturing costs. Over the course of the project, distillation experiments were performed with the targeted mixture, ethane-ethylene, as well as with analogous low relative volatility systems: cyclohexane-hexane and cyclopentane-pentane. Devices and test stands were specifically designed for these efforts. Development progressed from experiments and models considering sections of a full scale device to the design, fabrication, and operation of a single-channel distillation unit with integrated heat transfer. Throughout the project, analytical and numerical models and Computational Fluid Dynamics (CFD) simulations were validated with experiments in the process of developing this platform technology. Experimental trials demonstrated steady and controllable distillation for a variety of process conditions. Values of Height-to-an-Equivalent Theoretical Plate (HETP) ranging from less than 0.5 inch to a few inches were experimentally proven, demonstrating a ten-fold performance enhancement relative to conventional distillation. This improvement, while substantial, is not sufficient for MPT distillation to displace very large scale distillation trains. Fortunately, parallel efforts in the area of business development have yielded other applications for MPT distillation, including smaller scale separations that benefit from the flowsheet flexibility offered by the technology. Talks with multiple potential partners are underway. Their outcome will also help determine the path ahead for MPT distillation.

Maddalena Fanelli; Ravi Arora; Annalee Tonkovich; Jennifer Marco; Ed Rode

2010-03-24T23:59:59.000Z

189

Amine derivatives of thio-bis-lactone acids in combination with coadditive hydrocarbons are flow improvers for middle distillate fuel oils  

Science Conference Proceedings (OSTI)

Amine salts, amino acids, amino acid salts bis-amides and imides of oil-soluble thio-bis-(C12-50 alkyl lactone acid), e.g. a secondary hydrogenated tallow amide of dithio-bis-(C16-c24 alkyl lactone carboxylic acid), are useful in combination with a coadditive hydrocarbon such as an amorphous hydrocarbon or a hydrogenated polybutadiene in improving the cold flow properties of distillate hydrocarbon oils.

Brois, S.J.; Feldman, N.; Gutierrez, A.

1981-02-17T23:59:59.000Z

190

Low Distillate Stocks Set Stage for Price Volatility  

Gasoline and Diesel Fuel Update (EIA)

Along with the recent rise in crude oil prices, low stocks of Along with the recent rise in crude oil prices, low stocks of distillate fuels left markets in a vulnerable position. As we went into our two biggest distillate demand months, January and February, U.S. distillate stocks were very low -- particularly on the East and Gulf Coasts. The East Coast is the primary heating oil region, and it depends heavily on production from the Gulf Coast as well. Distillate stocks in the U.S. and Europe were in surplus supply as recently as October, but distillate stocks did not build as they usually do during the late fall, and declined more sharply than usual in December. December stocks closed well below the normal range. The unusual drawdown, in contrast to the more normal building pattern, resulted in distillate inventory levels about 3 million barrels lower than the very low

191

Table 8.6c Estimated Consumption of Combustible Fuels for Useful ...  

U.S. Energy Information Administration (EIA)

11 Commercial combined-heat-and-power (CHP) plants. 4 Jet fuel, kerosene, other petroleum liquids, and waste oil. 12 Industrial combined-heat-and-power (CHP) plants.

192

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane...  

Annual Energy Outlook 2012 (EIA)

Marketing Annual 1995 467 Table A2. RefinerReseller Prices of Aviation Fuels, Propane, and Kerosene, by PAD District, 1983-Present (Cents per Gallon Excluding Taxes) -...

193

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane...  

Gasoline and Diesel Fuel Update (EIA)

Marketing Annual 1999 421 Table A2. RefinerReseller Prices of Aviation Fuels, Propane, and Kerosene, by PAD District, 1983-Present (Cents per Gallon Excluding Taxes) -...

194

Random multiparty entanglement distillation  

E-Print Network (OSTI)

We describe various results related to the random distillation of multiparty entangled states - that is, conversion of such states into entangled states shared between fewer parties, where those parties are not predetermined. In previous work [Phys. Rev. Lett. 98, 260501 (2007)] we showed that certain output states (namely Einstein-Podolsky-Rosen (EPR) pairs) could be reliably acquired from a prescribed initial multipartite state (namely the W state) via random distillation that could not be reliably created between predetermined parties. Here we provide a more rigorous definition of what constitutes ``advantageous'' random distillation. We show that random distillation is always advantageous for W-class three-qubit states (but only sometimes for Greenberger-Horne-Zeilinger (GHZ)-class states). We show that the general class of multiparty states known as symmetric Dicke states can be readily converted to many other states in the class via random distillation. Finally we show that random distillation is provably not advantageous in the limit of multiple copies of pure states.

Ben Fortescue; Hoi-Kwong Lo

2007-09-25T23:59:59.000Z

195

Adapting to Network and Client Variability via On-Demand Dynamic Distillation  

E-Print Network (OSTI)

distillation curve (ADC), is a significant improvement, featuring (1) a composition-explicit data channel to the comparison of the distillation curve data grid of two aviation turbine fuels, JP-8 and S-8.10,18-20 JP-8 classifications to the data grid, the distillation curve becomes more information rich. In Figure 3, we present

Brewer, Eric A.

196

Alcohol production with solar distillation. Final report, March 31, 1982-June 30, 1982  

SciTech Connect

The purpose of this project was to determine it an absorber in a solar distillation unit that would provide a more efficient and effective way to produce fuel grade ethanol. Four tests of distilling ethanol were made. Numerous other tests were conducted distiling water, drying an assortment at materials, cooking food, and heating various liquids. The absorber in the solar distillation unit creates much heat on the glazing. The mixture in the solar distillation unit, does not have to reach temperatures that boil water to produce distillate.

Wuestenberg, D.

1982-06-01T23:59:59.000Z

197

Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel  

Gasoline and Diesel Fuel Update (EIA)

01.2 01.2 94.7 61.3 60.3 71.8 65.8 February ............................. 100.6 96.5 56.9 57.3 73.4 65.7 March .................................. 105.0 100.6 59.0 59.6 69.0 68.0 April .................................... 111.4 107.5 66.0 65.3 80.5 75.1 May ..................................... 114.4 110.0 63.3 62.2 68.4 66.1 June .................................... 113.5 107.0 57.7 57.5 58.5 59.8 July ..................................... 113.7 105.3 60.3 59.6 64.6 61.7 August ................................ 114.4 107.1 65.1 64.5 69.5 66.6 September .......................... 114.3 106.8 71.8 71.6 76.4 75.6 October ............................... 115.0 107.1 73.6 73.6 87.1 80.7 November ........................... 115.1 108.4 71.7 72.2 88.7 79.7 December ........................... 115.3

198

Refinery & Blender Net Production of Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

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

199

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1...  

Gasoline and Diesel Fuel Update (EIA)

790.3 6,200.2 648.4 4,283.7 3,323.4 44,204.9 February ... 151.1 456.7 46,811.8 13,168.9 661.0 5,865.0 639.0 3,498.4 4,030.8 40,811.0 March...

200

Geographic Area Month Aviation Gasoline Kerosene-Type Jet Fuel  

Gasoline and Diesel Fuel Update (EIA)

99.6 99.6 92.9 52.3 52.2 67.4 56.6 February ............................. 99.8 93.2 52.2 52.0 62.8 55.2 March .................................. 99.0 93.1 50.5 50.1 59.4 52.8 April .................................... 101.3 96.6 52.8 52.6 56.1 56.0 May ..................................... 105.8 102.2 55.0 54.7 51.7 57.7 June .................................... 106.4 101.6 53.2 53.1 54.9 53.2 July ..................................... 101.8 100.1 51.9 51.3 51.3 52.3 August ................................ 99.2 98.9 53.4 53.1 53.3 54.9 September .......................... 101.3 98.7 55.7 55.2 57.3 58.0 October ............................... 96.8 96.3 54.9 54.1 56.5 57.0 November ........................... 95.4 94.2 57.0 56.3 62.8 60.5 December ........................... 96.0 95.3 59.2 58.6

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Prime Supplier Sales Volumes of Kerosene-Type Jet Fuel  

Gasoline and Diesel Fuel Update (EIA)

58,921.8 56,922.5 55,453.9 54,959.2 53,458.9 54,523.8 1983-2012 58,921.8 56,922.5 55,453.9 54,959.2 53,458.9 54,523.8 1983-2012 East Coast (PADD 1) 15,392.8 16,081.8 15,898.2 15,821.2 15,588.0 15,512.9 1983-2012 New England (PADD 1A) 1,279.6 1,525.1 1,132.7 1,146.9 1,177.7 1,153.8 1983-2012 Connecticut 204.6 192.9 153.5 157.1 W 181.0 1983-2012 Maine 175.6 141.7 134.2 161.7 132.7 125.2 1983-2012 Massachusetts 819.4 1,118 676.6 675.6 720.1 710.2 1983-2012 New Hampshire 15.1 15.4 W 62.0 64.1 38.8 1983-2012 Rhode Island 33.3 30.3 75.7 67.2 W W 1983-2012 Vermont 31.6 26.9 W 23.4 23.8 W 1983-2012 Central Atlantic (PADD 1B) 7,527.2 7,614.5 7,315.1 7,397.0 7,311.6 7,228.9 1983-2012 Delaware 11.2 11.9 8.7 10.1 10.0 14.1 1983-2012 District of Columbia - - - - - - 1983-2012

202

Kerosene-Type Jet Fuel Imports from Singapore  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

203

Kerosene-Type Jet Fuel Imports from France  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

204

Kerosene-Type Jet Fuel Imports from Non OPEC  

U.S. Energy Information Administration (EIA)

... Iran, Iraq, Kuwait, Qatar, Saudi Arabia, and United Arab Emirates. Totals may not equal sum of components due to independent rounding.

205

Kerosene-Type Jet Fuel Imports from Aruba  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

206

FORM EIA-821 ANNUAL FUEL OIL AND KEROSENE SALES REPORT ...  

U.S. Energy Information Administration (EIA)

An energy-consuming sector that consists of living ... Infrastructure includes buildings and other major structures such as tanks, towers, monuments,

207

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1...  

Annual Energy Outlook 2012 (EIA)

2,083.2 26,581.1 August ... 201.6 810.9 52,026.8 12,609.7 241.1 1,226.9 227.0 450.2 2,304.5 28,715.2 September ... 179.3 713.1...

208

Kerosene-Type Jet Fuel Imports from Singapore  

U.S. Energy Information Administration (EIA)

Indonesia withdrew from OPEC in January 2009, Angola joined OPEC in January 2007, Ecuador withdrew from OPEC in January 1993 and rejoined in November ...

209

Kerosene-Type Jet Fuel Imports from Indonesia  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

210

Kerosene-Type Jet Fuel Refinery 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 ...

211

Kerosene-Type Jet Fuel Imports from China  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

212

Product Supplied for Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

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

213

Kerosene-Type Jet Fuel Imports from All Countries  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

214

Refinery Net Production of Kerosene-Type Jet Fuel - Commercial  

U.S. Energy Information Administration (EIA)

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

215

Kerosene-Type Jet Fuel Production - 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: Beginning in 1993, motor ...

216

Prime Supplier Sales of Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Retail prices and Prime ...

217

Kerosene-Type Jet Fuel Imports from Mexico  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

218

Refiner Retail Price of Kerosene-Type Jet Fuel  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Retail prices and Prime ...

219

Kerosene-Type Jet Fuel Imports by Area of Entry  

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 includes ...

220

Prime Supplier Sales Volumes of Kerosene-Type Jet Fuel  

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

58,386.8 57,380.8 57,511.7 61,022.4 59,252.0 55,062.2 1983-2013 58,386.8 57,380.8 57,511.7 61,022.4 59,252.0 55,062.2 1983-2013 East Coast (PADD 1) 18,284.2 16,437.1 16,943.8 16,884.2 16,412.3 14,287.5 1983-2013 New England (PADD 1A) 1,211.3 1,172.2 1,228.4 1,207.8 1,432.6 1,121.1 1983-2013 Connecticut 212.1 202.7 207.0 164.4 246.4 169.3 1983-2013 Maine 115.8 127.2 131.1 141.6 144.0 137.8 1983-2013 Massachusetts 738.4 705.5 738.7 743.0 863.8 670.3 1983-2013 New Hampshire 37.4 29.5 35.2 41.8 50.6 44.1 1983-2013 Rhode Island 88.5 W 89.9 89.9 99.2 76.9 1983-2013 Vermont 19.1 W 26.5 27.0 28.7 22.7 1983-2013 Central Atlantic (PADD 1B) 9,320.4 7,996.8 8,594.9 8,104.5 8,284.9 7,114.1 1983-2013 Delaware W W W W W W 1983-2013 District of Columbia W W W W W W 1983-2013

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1...  

Annual Energy Outlook 2012 (EIA)

District I January ... 40.3 90.0 10,208.0 3,500.0 227.8 2,856.8 W 306.2 123.4 7,320.4 February ... 53.1 127.4 11,484.5 3,658.7 165.7...

222

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1...  

Gasoline and Diesel Fuel Update (EIA)

District I January ... 48.5 92.9 13,156.5 2,264.2 160.7 2,282.7 W 48.2 134.5 5,492.8 February ... 55.9 108.8 13,753.8 2,289.2 147.5...

223

Table 45. Refiner Volumes of Aviation Fuels, Kerosene, No. 1...  

Gasoline and Diesel Fuel Update (EIA)

District I January ... 65.1 94.0 13,005.3 1,820.3 216.2 2,794.9 W 73.1 103.6 6,203.4 February ... 74.3 96.6 13,308.6 1,702.8 308.8...

224

Kerosene-Type Jet Fuel Imports from Bahrain  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

225

Kerosene-Type Jet Fuel Exports by Destination  

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 exports are ...

226

Wisconsin Kerosene-Type Jet Fuel Retail Sales by Refiners ...  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1984: 132.4: 141.2: 143.4: 141.9: 1985: 159.3: 174.1: 176.8: 156.5: 121.5: 117.2: 131.5: 137.9: 135.5: 152.8 ...

227

U.S. Kerosene-Type Jet Fuel Imports  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

228

Gulf Coast (PADD 3) Kerosene-Type Jet Fuel Imports  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

229

Missouri Kerosene-Type Jet Fuel Refiner Sales Volumes  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Values shown for the ...

230

DISTILLATION OF CALCIUM  

DOE Patents (OSTI)

This invention relates to an improvement in the process for the purification of caicium or magnesium containing an alkali metal as impurity, which comprises distiiling a batch of the mixture in two stages, the first stage distillation being carried out in the presence of an inert gas at an absolute pressure substantially greater than the vapor pressure of calcium or maguesium at the temperature of distillation, but less than the vaper pressure at that temperature of the alkali metal impurity so that only the alkali metal is vaporized and condensed on a condensing surface. A second stage distilso that substantially only the calcium or magnesium distills under its own vapor pressure only and condenses in solid form on a lower condensing surface.

Barton, J.

1954-07-27T23:59:59.000Z

231

Highlght - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Highlights Sales of Fuel Oil and Kerosene in 1997. Benefiting from the robust economic growth, demand for distillate fuel increased in 1997 for the sixth consecutive ...

232

www.eia.gov  

U.S. Energy Information Administration (EIA)

Idaho Commercial Consumption Coal CLCCB Natural Gas NNCCB Petroleum Distillate Fuel DFCCB Kerosene KSCCB LPG LGCCB Motor Gasoline MGCCB Residual Fuel ...

233

Winter Distillate and Natural Gas Outlook  

U.S. Energy Information Administration (EIA)

Table of Contents. Winter Distillate and Natural Gas Outlook. Distillate Prices Increasing With Crude Oil. Distillate Outlook. When Will Crude Oil Prices Fall?

234

Topological Quantum Distillation  

E-Print Network (OSTI)

We construct a class of topological quantum codes to perform quantum entanglement distillation. These codes implement the whole Clifford group of unitary operations in a fully topological manner and without selective addressing of qubits. This allows us to extend their application also to quantum teleportation, dense coding and computation with magic states.

H. Bombin; M. A. Martin-Delgado

2006-05-16T23:59:59.000Z

235

U.S. Distillate Market  

Gasoline and Diesel Fuel Update (EIA)

Are Important Part of Northeast Winter Supply Distillate Imports Surged to Meet SupplyDemand Imbalance Forecast U.S. Distillate Stocks Forecast Prices (U.S. Monthly Average)...

236

Winter Distillate .and Propane Outlook  

U.S. Energy Information Administration (EIA)

Winter Distillate .and Propane Outlook. Joanne Shore Energy Information Administration State Heating Oil and Propane Program August 2000

237

Fuel Oil Use in Manufacturing  

Gasoline and Diesel Fuel Update (EIA)

and residual fuel oils. Distillate fuel oil, the lighter product, is also used for heating of homes and commercial buildings. Residual oil is a much denser, heavier product...

238

On bound entanglement assisted distillation  

E-Print Network (OSTI)

We investigate asymptotic distillation of entanglement in the presence of an unlimited amount of bound entanglement for bi-partite systems. We show that the distillability is still bounded by the relative entropy of entanglement. This offers a strong support to the fact that bound entanglement does not improve distillation of entanglement.

V. Vedral

1999-08-14T23:59:59.000Z

239

State of California BOARD OF EQUALIZATION USE FUEL TAX REGULATIONS Regulation 1301.  

E-Print Network (OSTI)

Fuel includes any combustible gas or liquid, by whatever name the gas or liquid may be known or sold, of a kind used in an internal combustion engine for the generation of power to propel a motor vehicle on the highways, except fuel that is subject to the tax imposed by the Motor Vehicle Fuel License Tax Law and the Diesel Fuel Tax Law. For example, fuel includes, but is not limited to, liquefied petroleum gases, kerosene, distillate, stove oil, natural gas in liquid or gaseous form, and alcohol fuels. “Alcohol fuel ” includes: ethanol (ethyl alcohol), methanol, (methyl alcohol), or blends of gasoline and alcohol (including any denaturant) containing 15 percent, or less, gasoline by volume measured at 60 degrees Fahrenheit. “Natural gas ” means naturally occurring mixtures of hydrocarbon gases and vapors consisting principally of methane whether in gaseous or liquid form. The taxable unit for compressed natural gas (gaseous form) is 100 cubic feet of gas measured at 14.73 pounds of pressure per square inch at 60 degrees Fahrenheit. The taxable unit for liquid natural gas and other liquid fuels is the United States gallon, which is 231 cubic inches. To convert liters to gallons, the quantity of liters shall be multiplied by.26417 to determine the equivalent quantity in gallons. The resulting figure should be rounded to the nearest tenth of a gallon.

unknown authors

1949-01-01T23:59:59.000Z

240

Gulf Coast Distillate Production  

Gasoline and Diesel Fuel Update (EIA)

4 of 15 4 of 15 Notes: PADD 3 is a major source of supply for the East Coast. This graph shows how during the winter of 1997-1998 when distillate stocks were very high, production fell back. In contrast, we entered the winter of 1996-1997 with very low stocks, and refineries reached record production levels as they tried to build stocks late in the season. Notice that production is normally reduced in January as distillate stocks are used to meet demand and as refineries begin maintenance and turnovers, which continue into February. This January is no different. There is room for some production increases in January and February, if refineries postpone maintenance. But postponing maintenance and turnarounds can create problems when the gasoline production season begins in March and April.

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Simplified distillation column controls  

SciTech Connect

A simple, energy efficient method of controlling single or double distillation columns for the production of ethyl alcohol is described. The control system is based on a material balance scheme centered around a thermostat actuated control valve to regulate reflux rate and product purity. Column bottom's levels are automatically regulated by vented suction lines on the pump inlets. Methods of minimizing control input variations are used including column insulation, stillage-to-beer heat exchanger, and a steam pressure regulator.

Badger, P.; Pile, R.; Lightsey, G.

1984-01-01T23:59:59.000Z

242

Low Energy Distillation Schemes  

E-Print Network (OSTI)

In this paper we look at various options available for the reduction of energy consumption in distillation systems. For binary systems, we look at how heat pumps can be used. With multi-component systems, process integration offers a means of reducing energy consumption. We look at how the better integrated distillation schemes can be quickly identified. It is found that the design of integrated schemes is quicker than that of non-integrated schemes. We then look at how the use of heat pumps, non-isobaric operation and divided wall columns may be incorporated into the synthesis of multi-component separation schemes. It will be seen that process integration provides an important means of reducing energy consumption in distillation processes. However, its conventional use requires the installation of piping (and pipes carrying vapor streams tend to be of large diameter and are consequently expensive). So, finally we examine a way in which the capital cost of such systems can be reduced: the divided wall column.

Polley, G. T.

2002-04-01T23:59:59.000Z

243

Buildings Energy Data Book: 1.5 Generic Fuel Quad and Comparison  

Buildings Energy Data Book (EERE)

3 3 Carbon Emission Comparisons One million metric tons of carbon dioxide-equivalent emissions equals: - the combustion of 530 thousand short tons of coal - the coal input to 1 coal plant (200-MW) in about 1 year - the combustion of 18 billion cubic feet of natural gas - the combustion of 119 million gallons of gasoline = the combustion of gasoline for 7 hours in the U.S. = 323 thousand new cars, each driven 12,400 miles = 282 thousand new light-duty vehicles, each driven 12,200 miles = 274 thousand new light trucks, each driven 11,000 miles = 0.14 million new passenger cars, each making 5 round trips from New York to Los Angeles - the combustion of 192 million gallons of LPG - the combustion of 107 million gallons of kerosene - the combustion of 102 million gallons of distillate fuel

244

EIA Short-Term Energy and Winter Fuels OutlookWinter Fuels Outlook  

U.S. Energy Information Administration (EIA)

heating oil electricity South U.S. total wood kerosene/other/no heating 116 million homes 4 Short-Term Energy and Winter Fuels Outlook October 8, 2013

245

Catalytic distillation : design and application of a catalytic distillation column.  

E-Print Network (OSTI)

??Catalytic Distillation (CD) is a hybrid technology that utilizes the dynamics of si- multaneous reaction and separation in a single process unit to achieve a… (more)

Nieuwoudt, Josias Jakobus (Jako)

2005-01-01T23:59:59.000Z

246

Distillate Stocks Expected to Remain Low  

Gasoline and Diesel Fuel Update (EIA)

5 5 Notes: When EIA's demand forecast is combined with its outlook for production and net imports, distillate stocks are projected to remain low for the rest of the year. - Stocks are beginning at very low levels. The September 1 distillate fuel stock level (112 million barrels) is nearly 20% less than last year, and about 15% below the 10 year average for end of August levels. - But stocks on the East Coast, at 39.8 million barrels, are 39% behind year-ago levels, and about a similar percentage below end-of-August 10-year average levels. Over the last 10 years, the average stock build from the end of August through the end of November has been about 10 million barrels. We are forecasting about a 12 million barrel build, which does not reach the normal band. Forecast stocks peak at the end of November at 127 million

247

On bound entanglement assisted distillation  

E-Print Network (OSTI)

We investigate asymptotic distillation of entanglement in the presence of an unlimited amount of bound entanglement for bi-partite systems. We show that the distillability is still bounded by the relative entropy of entanglement. This offers a strong support to the fact that bound entanglement does not improve distillation of entanglement. PACS number(s): 03.65.Bz, 89.70.+c,89.80.+h

Vlatko Vedral

1999-01-01T23:59:59.000Z

248

Optimization approach to entanglement distillation  

E-Print Network (OSTI)

We put forward a method for optimized distillation of partly entangled pairs of qubits into a smaller number of more entangled pairs by recurrent local unitary operations and projections. Optimized distillation is achieved by minimization of a cost function with up to 30 real parameters, which is chosen to be sensitive to the fidelity and the projection probability at each step. We show that in many cases this approach can significantly improve the distillation efficiency in comparison to the present methods.

T. Opatrny; G. Kurizki

1998-11-30T23:59:59.000Z

249

residual fuel oil - U.S. Energy Information Administration (EIA)  

U.S. Energy Information Administration (EIA)

Residual fuel oil: A general classification for the heavier oils, known as No. 5 and No. 6 fuel oils, that remain after the distillate fuel oils and lighter ...

250

U.S. Distillate Inventories  

Gasoline and Diesel Fuel Update (EIA)

average, but 18 percent above last year. The stability of distillate stocks through the heart of this winter, when they usually decline, has virtually eliminated concerns about...

251

Distillate Supply/Demand Balance Reflected in Spreads  

Gasoline and Diesel Fuel Update (EIA)

4 4 Notes: The price spike that initiated the flood of distillate imports last winter can be easily seen in this chart. The distillate supply/demand balance influences the spread between spot distillate and spot crude oil prices. For example, when stocks are higher than normal, the spread will be lower than usual. This spread is the price incentive that encourages or discourages changes in supply. The January/February 2000 price spike was shorter than the one last winter, largely due to the timing. Since last winter's price spike occurred early in the season, it took some time before prices receded substantially. Currently, the distillate fuel refining spread (the difference between the spot heating oil price and the WTI price) is more "typical". But as was

252

A Parametric Reactive Distillation Study: Economic Feasibility and Design Heuristics.  

E-Print Network (OSTI)

??The integration of reaction and distillation into a single column is called reactive distillation or catalytic distillation. Reactive distillation provides many benefits such as reduced… (more)

Hoyme, Craig Alan

2004-01-01T23:59:59.000Z

253

Finished Motor Gasoline Net Production  

Gasoline and Diesel Fuel Update (EIA)

Data Series: Finished Motor Gasoline Finished Motor Gasoline (less Adj.) Reformulated Gasoline Reformulated Gasoline Blenede w/ Fuel Ethanol Reformulated Other Gasoline Conventional Gasoline Conventional Gasoline Blended w/ Fuel Ethanol Conventional Gasoline Blended w/ Fuel Ethanol, Ed55 & Ed55 Other Conventional Gasoline Finished Motor Gasoline Adjustment Kerosene-Type Jet Fuel Kerosene-Type Jet, Commercial Kerosene-Type Jet, Military Distillate Fuel Oil Distillate Fuel Oil, 15 ppm Sulfur and Under Distillate Fuel Oil > 15 ppm to 500 ppm Sulfur Distillate Fuel Oil > 500 ppm Sulfur Residual Fuel Oil Propane/Propylene Period: Weekly 4-Week Average

254

Heat Pumps in Distillation Processes  

Science Conference Proceedings (OSTI)

Both new and retrofit heat pump installations are often economically justifiable for distillation columns with a temperature differential of 50 degrees F or less. However, this study reveals that the near-term demand for electric heat pumps in petroleum and chemical distillation processes appears very limited.

1984-08-01T23:59:59.000Z

255

Word Pro - Untitled1  

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

7 Table 3.8a Heat Content of Petroleum Consumption: Residential and Commercial Sectors (Trillion Btu) Residential Sector Commercial Sector a Distillate Fuel Oil Kerosene Liquefied...

256

Prices of Refiner No. 2 Diesel Fuel Sales for Resale  

U.S. Energy Information Administration (EIA)

... Values shown for kerosene-type jet fuel for the current month at the U.S. and PADD levels are initial estimates calculated using prior history of the series as ...

257

Oil recovery from condensed corn distillers solubles.  

E-Print Network (OSTI)

??Condensed corn distillers solubles (CCDS) contains more oil than dried distillers grains with solubles (DDGS), 20 vs. 12% (dry weight basis). Therefore, significant amount of… (more)

Majoni, Sandra

2009-01-01T23:59:59.000Z

258

EIA Crude Oil Distillation Capacity (Table 36)  

U.S. Energy Information Administration (EIA)

(Important Note on Sources of Crude Oil Distillation Capacity Estimates) Table 3.6 World Crude Oil Distillation Capacity, January 1, 1970 - January 1, 2009

259

Theoretical and experimental investigation of membrane distillation.  

E-Print Network (OSTI)

??Invented in the 1960s, membrane distillation is an emerging technology for water treatment attracting more attention since 1980s. There are four configurations of membrane distillations… (more)

Zhang, Jianhua

2011-01-01T23:59:59.000Z

260

Membrane distillation : module design and modeling.  

E-Print Network (OSTI)

??Membrane distillation (MD) is an emerging technology for seawater desalination that is traditionally accomplished by conventional separation processes such as thermal distillation or reverse osmosis.… (more)

Yang, Xing.

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

American Distillation Inc | Open Energy Information  

Open Energy Info (EERE)

Distillation Inc Jump to: navigation, search Name American Distillation Inc. Place Leland, North Carolina Zip 28451 Product Biodiesel producer in North Carolina. References...

262

Production of biocomponent containing jet fuels  

Science Conference Proceedings (OSTI)

Recent demands for low aromatic content jet fuels have shown significant increase in the last 20 years. This was generated by the growing of aviation. Further than quality requirements were more aggravated in front of jet fuels. This was generated by ... Keywords: aromatic content, biocomponent, crystallization point, jet fuel, kerosene, vegetable oil

Z. Eller; P. Solymosi; T. Kasza; Z. Varga; J. Hancsók

2011-12-01T23:59:59.000Z

263

About distillability of depolarized states  

E-Print Network (OSTI)

Reduction criteria for distillability is applied to general depolarized states and an explicit condition is found in terms of a characteristic polynomial of the density matrix. 3 × 3 bipartite systems are analyzed in some details. 1

Andrea R. Rossi; Matteo G. A. Paris

2004-01-01T23:59:59.000Z

264

Distillation process using microchannel technology  

Science Conference Proceedings (OSTI)

The disclosed invention relates to a distillation process for separating two or more components having different volatilities from a liquid mixture containing the components. The process employs microchannel technology for effecting the distillation and is particularly suitable for conducting difficult separations, such as the separation of ethane from ethylene, wherein the individual components are characterized by having volatilities that are very close to one another.

Tonkovich, Anna Lee (Dublin, OH); Simmons, Wayne W. (Dublin, OH); Silva, Laura J. (Dublin, OH); Qiu, Dongming (Carbondale, IL); Perry, Steven T. (Galloway, OH); Yuschak, Thomas (Dublin, OH); Hickey, Thomas P. (Dublin, OH); Arora, Ravi (Dublin, OH); Smith, Amanda (Galloway, OH); Litt, Robert Dwayne (Westerville, OH); Neagle, Paul (Westerville, OH)

2009-11-03T23:59:59.000Z

265

Distillate Fuel Oil Sales for Railroad Use  

Gasoline and Diesel Fuel Update (EIA)

3,634,512 3,229,625 2,759,140 2,974,641 3,121,150 3,118,150 3,634,512 3,229,625 2,759,140 2,974,641 3,121,150 3,118,150 1984-2012 East Coast (PADD 1) 580,632 500,071 459,324 482,929 514,418 492,156 1984-2012 New England (PADD 1A) 69,282 47,582 43,763 53,930 51,126 33,306 1984-2012 Connecticut 4,450 3,219 2,219 2,006 2,006 5,195 1984-2012 Maine 126 1,694 7,252 8,284 6,818 5,970 1984-2012 Massachusetts 63,896 40,378 24,852 33,130 32,647 12,307 1984-2012 New Hampshire 119 126 697 86 124 116 1984-2012 Rhode Island 13 72 4 24 3 133 1984-2012 Vermont 678 2,092 8,740 10,400 9,528 9,586 1984-2012 Central Atlantic (PADD 1B) 210,461 177,750 152,309 196,570 233,005 204,527 1984-2012 Delaware 1,404 1,120 1,096 879 126 149 1984-2012 District of Columbia 0 0 0 1,229 6,392 6,770 1984-2012

266

Distillate Fuel Oil Sales for Industrial Use  

Gasoline and Diesel Fuel Update (EIA)

466,906 2,593,750 2,159,428 2,045,164 2,179,953 2,325,503 466,906 2,593,750 2,159,428 2,045,164 2,179,953 2,325,503 1984-2012 East Coast (PADD 1) 846,364 851,906 597,048 560,403 568,024 568,997 1984-2012 New England (PADD 1A) 57,624 56,038 60,994 41,357 42,972 39,708 1984-2012 Connecticut 13,312 10,362 17,414 8,976 7,576 7,427 1984-2012 Maine 16,275 17,536 17,332 14,167 15,981 13,532 1984-2012 Massachusetts 13,617 10,067 6,697 5,071 4,788 6,105 1984-2012 New Hampshire 5,618 6,481 12,393 4,455 4,180 4,239 1984-2012 Rhode Island 2,119 1,906 933 2,176 1,213 1,124 1984-2012 Vermont 6,683 9,687 6,225 6,512 9,234 7,280 1984-2012 Central Atlantic (PADD 1B) 294,847 307,072 185,569 152,730 195,359 190,517 1984-2012 Delaware 2,023 2,176 3,316 2,510 918 943 1984-2012

267

Distillate Fuel Oil Sales for Railroad Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 210,461: 177,750: 152,309: 196,570: 233,005: 204,527: 1984-2012: Delaware: 1,404: 1,120: ... Washington: 105,180: 78,701: ...

268

Distillate Fuel Oil Sales for Residential Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 2,432,099: 2,860,743: 1,824,324: 1,789,144: 1,610,573: 1,716,176: 1984-2012: Delaware: ... Washington: 45,457: 43,662: ...

269

Refinery Net Production of Distillate Fuel Oil  

U.S. Energy Information Administration (EIA)

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

270

Distillate Fuel Oil Sales for Commercial Use  

Gasoline and Diesel Fuel Update (EIA)

2,718,674 2,850,895 2,785,246 2,738,304 2,715,335 2,557,543 2,718,674 2,850,895 2,785,246 2,738,304 2,715,335 2,557,543 1984-2012 East Coast (PADD 1) 1,796,285 1,741,268 1,565,353 1,528,778 1,433,828 1,286,053 1984-2012 New England (PADD 1A) 468,464 414,174 401,527 487,480 415,642 314,646 1984-2012 Connecticut 107,555 105,372 80,709 84,370 85,400 71,696 1984-2012 Maine 120,883 114,227 85,876 88,529 95,962 74,902 1984-2012 Massachusetts 134,184 104,471 129,062 219,929 143,938 94,217 1984-2012 New Hampshire 45,883 41,254 42,557 39,671 43,292 32,389 1984-2012 Rhode Island 28,361 24,752 34,745 27,984 21,136 19,533 1984-2012 Vermont 31,598 24,098 28,579 26,998 25,914 21,910 1984-2012 Central Atlantic (PADD 1B) 1,014,960 1,013,141 839,545 725,332 727,755 634,029 1984-2012

271

Distillate Fuel Oil Sales for Farm Use  

Gasoline and Diesel Fuel Update (EIA)

,202,847 3,744,936 2,660,024 2,928,175 2,942,436 3,031,878 ,202,847 3,744,936 2,660,024 2,928,175 2,942,436 3,031,878 1984-2012 East Coast (PADD 1) 370,159 395,566 333,748 454,160 375,262 382,639 1984-2012 New England (PADD 1A) 24,850 30,839 13,909 13,140 16,967 16,070 1984-2012 Connecticut 2,164 2,469 1,671 1,920 2,182 2,134 1984-2012 Maine 10,710 14,479 3,256 4,430 4,902 5,944 1984-2012 Massachusetts 3,474 1,424 1,664 1,123 1,510 1,920 1984-2012 New Hampshire 3,114 5,412 2,375 948 1,554 1,439 1984-2012 Rhode Island 87 103 20 16 23 44 1984-2012 Vermont 5,301 6,951 4,925 4,704 6,797 4,589 1984-2012 Central Atlantic (PADD 1B) 102,108 119,028 94,862 101,211 108,924 104,831 1984-2012 Delaware 5,839 4,762 5,904 6,821 8,548 6,767 1984-2012 District of Columbia 0 0 0 0 0 0 1984-2012

272

Distillate Fuel Oil Sales for Military Use  

Gasoline and Diesel Fuel Update (EIA)

63,145 270,975 243,728 243,242 246,243 142,696 1984-2012 63,145 270,975 243,728 243,242 246,243 142,696 1984-2012 East Coast (PADD 1) 65,650 67,961 71,878 63,847 74,030 44,821 1984-2012 New England (PADD 1A) 12,611 17,229 5,915 5,174 6,420 3,359 1984-2012 Connecticut 1,660 997 385 533 622 501 1984-2012 Maine 5,349 8,059 1,487 2,852 1,506 1,071 1984-2012 Massachusetts 2,382 3,182 500 343 3,101 466 1984-2012 New Hampshire 1,390 3,220 1,480 490 253 104 1984-2012 Rhode Island 1,735 1,403 1,643 903 900 1,091 1984-2012 Vermont 93 368 420 53 38 124 1984-2012 Central Atlantic (PADD 1B) 28,387 22,436 31,857 28,351 28,047 14,109 1984-2012 Delaware 180 128 122 75 168 70 1984-2012 District of Columbia 598 291 165 265 693 300 1984-2012 Maryland 6,441 6,448 4,234 4,686 4,831 2,114 1984-2012

273

U.S. Distillate Fuel Oil Imports  

U.S. Energy Information Administration (EIA)

Singapore: 0 : 1999-2007: Spain: 1: 1 : 0 : 2001-2011: Sweden: 2: 0: 0 : 0: 2000-2012: Syria: 1: 1: 0 : 2006-2009: Taiwan : 2 : 2: 0 : 2001-2011: Trinidad and Tobago ...

274

Distillate Fuel Oil Imports from Puerto Rico  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

275

Distillate Fuel Oil Imports from Persian Gulf  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

276

Distillate Fuel Oil Imports from Peru  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

277

Product Supplied for Distillate Fuel Oil  

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

Weekly 4-Week Average Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area 101813 102513...

278

Distillate Fuel Oil Days of Supply  

Annual Energy Outlook 2012 (EIA)

Weekly Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area 101813 102513 110113 110813...

279

Total Adjusted Sales of Distillate Fuel Oil  

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

End Use: Total Residential Commercial Industrial Oil Company Farm Electric Power Railroad Vessel Bunkering On-Highway Military Off-Highway All Other Period: Annual Download Series...

280

Total Sales of Distillate Fuel Oil  

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

End Use: Total Residential Commercial Industrial Oil Company Farm Electric Power Railroad Vessel Bunkering On-Highway Military Off-Highway All Other Period: Annual Download Series...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Distillate Fuel Oil Exports - 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: Crude oil exports are ...

282

Product Supplied for Distillate Fuel Oil  

U.S. Energy Information Administration (EIA)

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

283

,,,,"Reasons that Made Distillate Fuel Oil Unswitchable"  

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

311,"Food",13.1,15.4,17.4,2.9,61.8,1.9,96.2,32.9,"X","X",38.6 3112," Grain and Oilseed Milling",2.1,2.2,1.7,10.8,"X","X",96.2,"X","X","X",0.3 311221," Wet Corn...

284

Distillation Column Flooding Predictor  

SciTech Connect

The Flooding Predictor™ is a patented advanced control technology proven in research at the Separations Research Program, University of Texas at Austin, to increase distillation column throughput by over 6%, while also increasing energy efficiency by 10%. The research was conducted under a U. S. Department of Energy Cooperative Agreement awarded to George Dzyacky of 2ndpoint, LLC. The Flooding Predictor™ works by detecting the incipient flood point and controlling the column closer to its actual hydraulic limit than historical practices have allowed. Further, the technology uses existing column instrumentation, meaning no additional refining infrastructure is required. Refiners often push distillation columns to maximize throughput, improve separation, or simply to achieve day-to-day optimization. Attempting to achieve such operating objectives is a tricky undertaking that can result in flooding. Operators and advanced control strategies alike rely on the conventional use of delta-pressure instrumentation to approximate the column’s approach to flood. But column delta-pressure is more an inference of the column’s approach to flood than it is an actual measurement of it. As a consequence, delta pressure limits are established conservatively in order to operate in a regime where the column is never expected to flood. As a result, there is much “left on the table” when operating in such a regime, i.e. the capacity difference between controlling the column to an upper delta-pressure limit and controlling it to the actual hydraulic limit. The Flooding Predictor™, an innovative pattern recognition technology, controls columns at their actual hydraulic limit, which research shows leads to a throughput increase of over 6%. Controlling closer to the hydraulic limit also permits operation in a sweet spot of increased energy-efficiency. In this region of increased column loading, the Flooding Predictor is able to exploit the benefits of higher liquid/vapor traffic that produce increased contact area and lead to substantial increases in separation efficiency – which translates to a 10% increase in energy efficiency on a BTU/bbl basis. The Flooding Predictor™ operates on the principle that between five to sixty minutes in advance of a flooding event, certain column variables experience an oscillation, a pre-flood pattern. The pattern recognition system of the Flooding Predictor™ utilizes the mathematical first derivative of certain column variables to identify the column’s pre-flood pattern(s). This pattern is a very brief, highly repeatable, simultaneous movement among the derivative values of certain column variables. While all column variables experience negligible random noise generated from the natural frequency of the process, subtle pre-flood patterns are revealed among sub-sets of the derivative values of column variables as the column approaches its hydraulic limit. The sub-set of column variables that comprise the pre-flood pattern is identified empirically through in a two-step process. First, 2ndpoint’s proprietary off-line analysis tool is used to mine historical data for pre-flood patterns. Second, the column is flood-tested to fine-tune the pattern recognition for commissioning. Then the Flooding Predictor™ is implemented as closed-loop advanced control strategy on the plant’s distributed control system (DCS), thus automating control of the column at its hydraulic limit.

George E. Dzyacky

2010-11-23T23:59:59.000Z

285

Hydrogen isotope distillation for the Tritium Systems Test Assembly  

DOE Green Energy (OSTI)

A system of four, interlinked, cryogenic fractional distillation columns has been designed as a prototype for fuel processing for fusion power reactors. The distillation system will continuously separate a feedstream of 360 g moles/day of roughly 50-50 deuterium-tritium containing approximately 1% H into four product streams: (1) a tritium-free stream of HD for waste disposal; (2) a stream of high-purity D/sub 2/ for simulated neutral beam injection; (3) a stream of DT for simulated reactor refueling; and (4) a stream of high purity T/sub 2/ for refueling and studies on properties of tritium and effects of tritium on materials.

Bartlit, J.R.; Denton, W.H.; Sherman, R.H.

1978-01-01T23:59:59.000Z

286

Petroleum Gasoline & Distillate Needs Including the Energy ...  

U.S. Energy Information Administration (EIA)

Home > Petroleum > Analysis > Petroleum Gasoline & Distillate Needs Including the Energy Independence and Security Act (EISA) ...

287

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)

288

Isotropic non-locality cannot be distilled  

E-Print Network (OSTI)

We investigate non-locality distillation protocols for isotropic correlations. These correlations are the hardest instances which respect to distillability and only partial results are known about their behaviour under non-locality distillation protocols. We completely resolve this issue by proving that non-locality distillation is impossible for all non-local isotropic correlations.

Dejan D. Dukaric

2011-08-02T23:59:59.000Z

289

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)

290

Petroleum Gasoline & Distillate Needs Including the Energy ...  

U.S. Energy Information Administration (EIA)

Petroleum Gasoline & Distillate Needs Including the Energy Independence and Security Act (EISA) Impacts

291

Distillate Imports Surged to Meet Supply/Demand Imbalance  

Gasoline and Diesel Fuel Update (EIA)

receded when weather moderated and new supply began to receded when weather moderated and new supply began to arrive. Imports were the largest source of new supply that arrived to relieve the imbalance that was behind the price spike. This graph shows the dramatic increase on a calendar monthly average basis. During the three weeks ending February 25, distillate fuel oil imports averaged 566 thousand barrels per day. During the prior four weeks, imports only averaged 162 thousand barrels per day. Refinery production on the East Coast also increased. For the three weeks ending February 25, East Coast distillate production averaged 478 thousand barrels per day, which was an increase of about 91 thousand barrels per day or 24% over the prior four weeks. (During the same time period, national distillate production only rose 7 percent.)

292

FRACTIONAL DISTILLATION SEPARATION OF PLUTONIUM VALUES FROM LIGHT ELEMENT VALUES  

DOE Patents (OSTI)

A process is described for removing light element impurities from plutonium. It has been found that plutonium contaminated with impurities may be purified by converting the plutonium to a halide and purifying the halide by a fractional distillation whereby impurities may be distilled from the plutonium halide. A particularly effective method includes the step of forming a lower halide such as the trior tetrahalide and distilling the halide under conditions such that no decomposition of the halide occurs. Molecular distillation methods are particularly suitable for this process. The apparatus may comprise an evaporation plate with means for heating it and a condenser surface with means for cooling it. The condenser surface is placed at a distance from the evaporating surface less than the mean free path of molecular travel of the material being distilled at the pressure and temperature used. The entire evaporating system is evacuated until the pressure is about 10/sup -4/ millimeters of mercury. A high temperuture method is presented for sealing porous materials such as carbon or graphite that may be used as a support or a moderator in a nuclear reactor. The carbon body is subjected to two surface heats simultaneously in an inert atmosphere; the surface to be sealed is heated to 1500 degrees centigrade; and another surface is heated to 300 degrees centigrade, whereupon the carbon vaporizes and flows to the cooler surface where it is deposited to seal that surface. This method may be used to seal a nuclear fuel in the carbon structure.

Cunningham, B.B.

1957-12-17T23:59:59.000Z

293

PPMCSA Presentation on Winter Distillate Outlook  

Gasoline and Diesel Fuel Update (EIA)

PPMCSA Presentation on Winter Distillate Outlook PPMCSA Presentation on Winter Distillate Outlook 09/15/2000 Click here to start Table of Contents Winter Distillate Outlook Distillate Prices Increasing With Crude Oil Factors Driving Prices & Forecast First Factor Impacting Distillate Prices: Crude Oil Prices High Crude Prices Go With Low Inventories Second Price Component: Spread Impacted by Distillate Supply/Demand Balance Distillate Stocks are Low – Especially on the East Coast Distillate Stocks Are Important Part of East Coast Winter Supply Winter Demand Impacted by Weather Warm Winters Held Heating Oil Demand Down While Diesel Grew Distillate Demand Strong in December 1999 Dec 1999 & Jan 2000 Production Fell, But Rebounded with Price Higher Yields Can Be Achieved Unusual Net Imports May Only Be Available at a High Price

294

Collocation Methods For Distillation Design  

E-Print Network (OSTI)

In this third paper on collocation methods for distillation design, we explore the use of the collocation models for design of simple distillation columns as well as flexible columns. Solvent recovery plants must deal with a wide range of feeds and still return pure solvents. The design problem we address is a single flexible column within the overall solvent recovery plant. We have developed the models and algorithms in the ASCEND system. We discuss the attributes and use of the ASCEND system. With ASCEND we can create complex models with simple building blocks and interactively learn to solve them. We found the collocation model an excellent tool for distillation design, allowing us to develop new concepts in design strategies. We designed a single column as would exist in a flexible solvent recovery plant for an azeotropic system. It was designed to handle three possible feeds, each with a distinct separation task. For each possible feed to a column, we approximate the operation of ...

Flexible Column; Robert S. Huss; Arthur W. Westerberg

1995-01-01T23:59:59.000Z

295

Optimal protocols for nonlocality distillation  

Science Conference Proceedings (OSTI)

Forster et al. recently showed that weak nonlocality can be amplified by giving the first protocol that distills a class of nonlocal boxes (NLBs) [Phys. Rev. Lett. 102, 120401 (2009)] We first show that their protocol is optimal among all nonadaptive protocols. We next consider adaptive protocols. We show that the depth-2 protocol of Allcock et al. [Phys. Rev. A 80, 062107 (2009)] performs better than previously known adaptive depth-2 protocols for all symmetric NLBs. We present a depth-3 protocol that extends the known region of distillable NLBs. We give examples of NLBs for which each of the Forster et al., the Allcock et al., and our protocols perform best. The understanding we develop is that there is no single optimal protocol for NLB distillation. The choice of which protocol to use depends on the noise parameters for the NLB.

Hoeyer, Peter; Rashid, Jibran [Department of Computer Science, University of Calgary, 2500 University Drive N.W., Calgary, Alberta, 2N 1N4 (Canada)

2010-10-15T23:59:59.000Z

296

Ethanol production by vapor compression distillation  

DOE Green Energy (OSTI)

The goal of this project is to develop and demonstrate a one gallon per hour vapor compression distillation unit for fuel ethanol production that can be profitably manufactured and economically operated by individual family units. Vapor compression distillation is already an industrially accepted process and this project's goal is to demonstrate that it can be done economically on a small scale. Theoretically, the process is independent of absolute pressure. It is only necessary that the condenser be at higher pressure than the evaporator. By reducing the entire process to a pressure of approximately 0.1 atmosphere, the evaporation and condensation can occur at near ambient temperature. Even though this approach requires a vacuum pump, and thus will not represent the final cost effective design, it does not require preheaters, high temperature materials, or as much insulation as if it were to operate a near ambient pressure. Therefore, the operation of the ambient temperature unit constitutes the first phase of this project. Presently, the ambient temperature unit is fully assembled and has begun testing. So far it has successfully separated ethanol from a nine to one diluted input solution. However the production rate has been very low.

Ellis, G.S.

1981-01-01T23:59:59.000Z

297

Bounds for nonlocality distillation protocols  

Science Conference Proceedings (OSTI)

Nonlocality can be quantified by the violation of a Bell inequality. Since this violation may be amplified by local operations, an alternative measure has been proposed--distillable nonlocality. The alternative measure is difficult to calculate exactly due to the double exponential growth of the parameter space. In this paper, we give a way to bound the distillable nonlocality of a resource by the solutions to a related optimization problem. Our upper bounds are exponentially easier to compute than the exact value and are shown to be meaningful in general and tight in some cases.

Forster, Manuel [Computer Science Department, ETH Zuerich, CH-8092 Zuerich (Switzerland)

2011-06-15T23:59:59.000Z

298

Olefin production via reactive distillation based Olefin metathesis.  

E-Print Network (OSTI)

??Reactive distillation is a combination of a traditional multi-stage distillation column with a chemical reaction. The primary benefits of a reactive distillation process are reduced… (more)

Morrison, Ryan Frederick

2012-01-01T23:59:59.000Z

299

Purification of Indium by Vacuum Distillation - Programmaster.org  

Science Conference Proceedings (OSTI)

The two-step vacuum distillation were carried out to study the influence of distillation temperature, distillation time on the impurities. At the first step the content of ...

300

Crude Distillation Unit Heat Recovery Study  

E-Print Network (OSTI)

Baytown's Pipe Still 3 is a 95,000 barrel per day crude distillation unit. A comprehensive heat recovery and energy utilization study was done on Pipe Still 3 after a preliminary cursory study had indicated that an overall look at the total picture could produce much better results than a series of improvements done piecemeal. The study did meet its objective by identifying the maximum heat recovery that is technically and economically feasible. It showed a potential for dramatic improvement - a 39 percent reduction in fuel, plus a 43 percent increase in the quantity of process steam generated, equivalent to a 48 percent reduction in net energy consumed. Techniques employed included a Source/Sink Profile (which is described later); a combining of oil heating, steam generation, and air preheat to best advantage; and a computer program to design the required heat exchanger trains.

John, P.

1979-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane...  

Gasoline and Diesel Fuel Update (EIA)

- W 73.5 See footnotes at end of table. A2. RefinerReseller Prices of Aviation Fuels, Propane, and Kerosene, by PAD District, 1983-Present Energy Information Administration ...

302

Entanglement preservation by continuous distillation  

Science Conference Proceedings (OSTI)

We study the two-qubit entanglement preservation for a system in the presence of independent thermal baths. We use a combination of filtering operations and distillation protocols as a series of frequent measurements on the system. It is shown that a small fraction of the total amount of available copies of the system preserves or even improves its initial entanglement during the evolution.

Mundarain, D. [Departmento de Fisica, Seccion de Fenomenos Opticos, Universidad Simon Bolivar, Apartado Postal 89000, Caracas 1080A (Venezuela, Bolivarian Republic of); Orszag, M. [Facultad de Fisica, Pontificia Universidad Catolica de Chile, Casilla 306, Santiago 22 (Chile)

2009-05-15T23:59:59.000Z

303

Optimal Control of Distillation Systems  

E-Print Network (OSTI)

The optimum performance of a distillation system can be evaluated by examining the product purities, the product recoveries, and the system's capability to respond to small or large, expected or unexpected, plant disturbances. An optimal control system should include accurate instrumentation, closed loop purity control, and a computer system to execute direct digital control with appropriate feed-forward algorithms.

Chatterjee, N.; Suchdeo, S. R.

1984-01-01T23:59:59.000Z

304

Corrosion inhibition for distillation apparatus  

DOE Patents (OSTI)

Tower material corrosion in an atmospheric or sub-atmospheric distillation tower in a coal liquefaction process is reduced or eliminated by subjecting chloride-containing tray contents to an appropriate ion-exchange resin to remove chloride from such tray contents materials.

Baumert, Kenneth L. (Emmaus, PA); Sagues, Alberto A. (Lexington, KY); Davis, Burtron H. (Georgetown, KY); Schweighardt, Frank K. (Upper Macungie, PA)

1985-01-01T23:59:59.000Z

305

Distillate Prices Increasing With Crude Oil  

Gasoline and Diesel Fuel Update (EIA)

8 Notes: This slide shows the strong influence crude oil prices have on retail distillate prices. Distillate tracks the crude price increases seen in 1996 and the subsequent fall...

306

Binary distillation column design using mathematica  

Science Conference Proceedings (OSTI)

The accurate design of distillation columns is a very important topic in chemical industry. In this paper, we describe a Mathematica program for the design of distillation columns for binary mixtures. For simplicity, it is assumed that the columns are ...

Akemi Gálvez; Andrés Iglesias

2003-06-01T23:59:59.000Z

307

"Characteristic(a)","Total","Electricity(b)","Fuel Oil","Fuel...  

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

Net","Residual","Distillate",,"LPG and",,"Coke and"," " "Characteristic(a)","Total","Electricity(b)","Fuel Oil","Fuel Oil(c)","Natural Gas(d)","NGL(e)","Coal","Breeze","Other(f)"...

308

Intermediate Vapor Expansion Distillation and Nested Enrichment Cascade Distillation  

E-Print Network (OSTI)

Although it is known that incorporating an intermediate reboiler or reflux condenser in a distillation column will improve column efficiency by 15 to 100%, there has been little use of this technique to date." Intermediate vapor compression heat pumping was recently introduced as one practical means of achieving this benefit. Introduced in this paper are two new means having added advantages over compression: intermediate vapor expansion heat pumping, and nested enrichment cascades. In both cases the efficiency advantage is obtained without requiring import of shaft work. With intermediate vapor expansion, the expander is more efficient and less costly than the compressor which achieves comparable improvement in distillation efficiency. With the "nested enrichment" technique, the increased efficiency is obtained without requiring either compressors or expanders.

Erickson, D. C.

1986-06-01T23:59:59.000Z

309

Effect of Narrow Cut Oil Shale Distillates on HCCI Engine Performance  

Science Conference Proceedings (OSTI)

In this investigation, oil shale crude obtained from the Green River Formation in Colorado using Paraho Direct retorting was mildly hydrotreated and distilled to produce 7 narrow boiling point fuels of equal volumes. The resulting derived cetane numbers ranged between 38.3 and 43.9. Fuel chemistry and bulk properties strongly correlated with boiling point.

Eaton, Scott J [ORNL; Bunting, Bruce G [ORNL; Lewis Sr, Samuel Arthur [ORNL; Fairbridge, Craig [National Centre for Upgrading Technology, Canada

2009-01-01T23:59:59.000Z

310

Multiple Steady States in Azeotropic and Reactive Distillation  

E-Print Network (OSTI)

Introduction . Motivation Overview on the Contributions MSS in Reactive Distillation Conclusions Outline Multiple Steady States (MSS) Overview on the Contributions . The Starting Point . Consolidation . Industrial Applications . Incorporating Reactions MSS in Reactive Distillation Conclusions Outline Multiple Steady States (MSS) Overview on the Contributions MSS in Reactive Distillation . Prediction Method . MTBE Process Conclusions Outline Multiple Steady States (MSS) Overview on the Contributions MSS in Reactive Distillation Conclusions Distillation Overview . Ideal binary / multicomponent distillation . Homogeneous azeotropic distillation -- Heavy entrainer (extractive distillation) -- Intermediate entrainer -- "Boundary scheme" (ligh

Thomas E. Güttinger

1998-01-01T23:59:59.000Z

311

Word Pro - Untitled1  

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

Sales, 1984-2010 Total by Fuel Distillate Fuel Oil by Selected End Use Residual Fuel Oil by Major End Use Kerosene by Major End Use 154 U.S. Energy Information Administration...

312

AMMONIA DISTILLATION FOR DEUTERIUM SEPARATION  

SciTech Connect

The relative volatility or separation factor for deuterium enrichment in ammonia distillation was measured at several pressures and deuterium concentrations. The knowledge of this ingormation is very helpful in predicting costs of heawy water production by the ammonia distillation process. It hss been stated by others, that the ammonia distillation process of heawy water production would be competitive with other developed methods only if the actusl separation factor was at least 1.062 at low deuterium concentration. Ungortunately, the measurements do not indicate that the separation factor at low deuterium composition differs greatly from the vapor pressure pre diction ( alpha = 1.042). Deutero-ammonia was synthesized by isotopic exchange between natural ammonia and heavy water. Equilibrium determinations were made using an Othmer still, modified for low temperature operation, and a concentric tube fractionating column. The arnmonia samples were analyzed for deuterium content by converting them to water by flow torough hot copper oxide, followed by a differential density determination using the falling drop method. ( auth)

Petersen, G.T.; Benedict, M.

1960-05-16T23:59:59.000Z

313

The Northeast heating fuel market: Assessment and options  

SciTech Connect

In response to a Presidential request, this study examines how the distillate fuel oil market (and related energy markets) in the Northeast behaved in the winter of 1999-2000, explains the role played by residential, commercial, industrial, and electricity generation sector consumers in distillate fuel oil markets and describes how that role is influenced by the structure of tie energy markets in the Northeast. In addition, this report explores the potential for nonresidential users to move away from distillate fuel oil and how this might impact future prices, and discusses conversion of distillate fuel oil users to other fuels over the next 5 years. Because the President's and Secretary's request focused on converting factories and other large-volume users of mostly high-sulfur distillate fuel oil to other fuels, transportation sector use of low-sulfur distillate fuel oil is not examined here.

None

2000-07-01T23:59:59.000Z

314

Distributive Distillation Enabled by Microchannel Process Technology  

SciTech Connect

The application of microchannel technology for distributive distillation was studied to achieve the Grand Challenge goals of 25% energy savings and 10% return on investment. In Task 1, a detailed study was conducted and two distillation systems were identified that would meet the Grand Challenge goals if the microchannel distillation technology was used. Material and heat balance calculations were performed to develop process flow sheet designs for the two distillation systems in Task 2. The process designs were focused on two methods of integrating the microchannel technology â?? 1) Integrating microchannel distillation to an existing conventional column, 2) Microchannel distillation for new plants. A design concept for a modular microchannel distillation unit was developed in Task 3. In Task 4, Ultrasonic Additive Machining (UAM) was evaluated as a manufacturing method for microchannel distillation units. However, it was found that a significant development work would be required to develop process parameters to use UAM for commercial distillation manufacturing. Two alternate manufacturing methods were explored. Both manufacturing approaches were experimentally tested to confirm their validity. The conceptual design of the microchannel distillation unit (Task 3) was combined with the manufacturing methods developed in Task 4 and flowsheet designs in Task 2 to estimate the cost of the microchannel distillation unit and this was compared to a conventional distillation column. The best results were for a methanol-water separation unit for the use in a biodiesel facility. For this application microchannel distillation was found to be more cost effective than conventional system and capable of meeting the DOE Grand Challenge performance requirements.

Arora, Ravi

2013-01-22T23:59:59.000Z

315

Distillate Stocks are Low - Especially on the East Coast  

Gasoline and Diesel Fuel Update (EIA)

8 8 Notes: Distillate stocks are normally built during the summer for use during the winter as shown by the normal band. Currently, stocks are very low for this time of year. This graph shows East Coast inventories, which at the end of August, were well below the normal band (over 9 million barrels or 19% below the low end of the band). The East Coast is about 31% lower than its 10-year average level for this time of year. We focus on the East Coast (PADD 1 ) because this a region in which heating oil is a major winter fuel. Furthermore, the East Coast consumes almost 2/3 of the nation's heating oil (high sulfur distillate). December 1999 was the turning point. Stocks were well within the normal range through November 1999, but in December, they dropped below the

316

Entanglement distillation from quasifree Fermions  

E-Print Network (OSTI)

We develop a scheme to distill entanglement from bipartite Fermionic systems in an arbitrary quasifree state. It can be applied if either one system containing infinite one-copy entanglement is available or if an arbitrary amount of equally prepared systems can be used. We show that the efficiency of the proposed scheme is in general very good and in some cases even optimal. Furthermore we apply it to Fermions hopping on an infinite lattice and demonstrate in this context that an efficient numerical analysis is possible for more then 10^6 lattice sites.

Zoltan Kadar; Michael Keyl; Dirk Schlingemann

2010-03-14T23:59:59.000Z

317

Table 7.4b Consumption of Combustible Fuels for Electricity ...  

U.S. Energy Information Administration (EIA)

and Useful Thermal Output: Electric Power Sector (Subset of Table 7.4a) Coala Petroleum Natural Gasf Other Gasesg Biomass Otherj Distillate Fuel Oilb Residual Fuel Oilc

318

South Dakota Residual Fuel Oil Adj Sales/Deliveries to Oil Company ...  

U.S. Energy Information Administration (EIA)

Referring Pages: Adjusted Sales of Residual Fuel Oil for Oil Company Use ; Adjusted Sales of Residual Fuel Oil for Oil Company Use ; South Dakota Adjusted Distillate ...

319

Reactive Distillation for Esterification of Bio-based Organic Acids  

DOE Green Energy (OSTI)

The following is the final report of the three year research program to convert organic acids to their ethyl esters using reactive distillation. This report details the complete technical activities of research completed at Michigan State University for the period of October 1, 2003 to September 30, 2006, covering both reactive distillation research and development and the underlying thermodynamic and kinetic data required for successful and rigorous design of reactive distillation esterification processes. Specifically, this project has led to the development of economical, technically viable processes for ethyl lactate, triethyl citrate and diethyl succinate production, and on a larger scale has added to the overall body of knowledge on applying fermentation based organic acids as platform chemicals in the emerging biorefinery. Organic acid esters constitute an attractive class of biorenewable chemicals that are made from corn or other renewable biomass carbohydrate feedstocks and replace analogous petroleum-based compounds, thus lessening U.S. dependence on foreign petroleum and enhancing overall biorefinery viability through production of value-added chemicals in parallel with biofuels production. Further, many of these ester products are candidates for fuel (particularly biodiesel) components, and thus will serve dual roles as both industrial chemicals and fuel enhancers in the emerging bioeconomy. The technical report from MSU is organized around the ethyl esters of four important biorenewables-based acids: lactic acid, citric acid, succinic acid, and propionic acid. Literature background on esterification and reactive distillation has been provided in Section One. Work on lactic acid is covered in Sections Two through Five, citric acid esterification in Sections Six and Seven, succinic acid in Section Eight, and propionic acid in Section Nine. Section Ten covers modeling of ester and organic acid vapor pressure properties using the SPEAD (Step Potential Equilibrium and Dynamics) method.

Fields, Nathan; Miller, Dennis J.; Asthana, Navinchandra S.; Kolah, Aspi K.; Vu, Dung; Lira, Carl T.

2008-09-23T23:59:59.000Z

320

Distillation of Bell states in open systems.  

E-Print Network (OSTI)

In this work we review the entire classification of 2 × 2 distillable states for protocols with a finite numbers of copies. We show a distillation protocol that allows to distill Bell states with non zero probability at any time for an initial singlet in vacuum. It is shown that the same protocol used in non zero thermal baths yields a considerable recovering of entanglement. 1

E. Isasi; D. Mundarain

2009-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Distillation of Bell states in open systems  

E-Print Network (OSTI)

In this work we review the entire classification of 2x2 distillable states for protocols with a finite numbers of copies. We show a distillation protocol that allows to distill Bell states with non zero probability at any time for an initial singlet in vacuum. It is shown that the same protocol used in non zero thermal baths yields a considerable recovering of entanglement.

E. Isasi; D. Mundarain

2009-08-14T23:59:59.000Z

322

Separating lignite hydrogenation sludge by vacuum distillation  

SciTech Connect

Vacuum distillation was studied as a means to separate coal hydrogenation sludge. Additives containing mainly aromatic hydrocarbons intensified the process. 4 refs., 2 figs., 5 tabs.

Gorlov, E.G.; Grobanova, L.T.; Belyavtseva, N.V. [Rossiskaya Akademiya, Nauk (Russian Federation)

1994-12-31T23:59:59.000Z

323

Distillate Demand Strong in December 1999  

U.S. Energy Information Administration (EIA)

Total distillate demand includes both diesel and heating oil. These are similar products. Physically, diesel can be used in the heating oil market, but low sulfur ...

324

Total Atmospheric Crude Oil Distillation Capacity Former ...  

U.S. Energy Information Administration (EIA)

Former Corporation/Refiner Total Atmospheric Crude Oil Distillation Capacity (bbl/cd)a New Corporation/Refiner Date of Sale Table 14. Refinery Sales During 2005

325

Total Organic Carbon Rejection in Osmotic Distillation.  

E-Print Network (OSTI)

?? The osmotic distillation (OD) system is a spacecraft wastewater recycling system designed to produce potable water from human urine and humidity condensate. The OD… (more)

Shaw, Hali Laraelizabeth

2012-01-01T23:59:59.000Z

326

Conceptual Design for Pressure Swing Distillation.  

E-Print Network (OSTI)

??The separation of homogenous azeotropic mixtures is a common task in the chemical industry. In the literature, pressure swing distillation is often mentioned as an… (more)

Bozzacco, Carmen

2006-01-01T23:59:59.000Z

327

Intelligent fuzzy supervisory control for distillation columns.  

E-Print Network (OSTI)

??Distillation as a separation technique is widely used in the chemical and petroleum industries. With the growth of these industries and the availability of cheap… (more)

Santhanam, Srinivasan

2012-01-01T23:59:59.000Z

328

Tritium Removal Facility High Tritium Distillation Simulation.  

E-Print Network (OSTI)

??A dynamic model was developed for the distillation mechanism of the Darlington Tritium Removal Facility. The model was created using the commercial software package MATLAB/Simulink.… (more)

Zahedi, Polad

2013-01-01T23:59:59.000Z

329

Vacuum Distillation Refining of Crude Tin - Thermodynamics ...  

Science Conference Proceedings (OSTI)

Presentation Title, Vacuum Distillation Refining of Crude Tin - Thermodynamics Analysis and Experiments on the Removal of Arsenic from the Crude Tin.

330

Locally Accessible Information and Distillation of Entanglement  

E-Print Network (OSTI)

A new type of complementary relation is found between locally accessible information and final average entanglement for given ensemble. It is also shown that in some well known distillation protocol, this complementary relation is optimally satisfied. We discuss the interesting trade-off between locally accessible information and distillable entanglement for some states.

Sibasish Ghosh; Pramod Joag; Guruprasad Kar; Samir Kunkri; Anirban Roy

2004-03-18T23:59:59.000Z

331

Distillation of Bell states in open systems  

Science Conference Proceedings (OSTI)

In this work we show that the distillation protocol proposed by P. Chen et al. [Phys. Rev. A 54, 3824 (1996)] allows one to distill Bell states at any time for a system evolving in vacuum and prepared in an initial singlet. It is also shown that the same protocol, applied in nonzero temperature thermal baths, yields a considerable recovering of entanglement.

Isasi, E.; Mundarain, D. [Departamento de Fisica, Seccion de Fenomenos Opticos, Universidad Simon Bolivar, Apartado Postal 89000, Caracas 1080A (Venezuela, Bolivarian Republic of)

2010-04-15T23:59:59.000Z

332

Rank three bipartite entangled states are distillable  

E-Print Network (OSTI)

We prove that the bipartite entangled state of rank three is distillable. So there is no rank three bipartite bound entangled state. By using this fact, We present some families of rank four states that are distillable. We also analyze the relation between the low rank state and the Werner state.

Lin Chen; Yi-Xin Chen

2008-03-07T23:59:59.000Z

333

www.eia.gov  

U.S. Energy Information Administration (EIA)

Table 10 FIG_CO2IDX1 FIG_CO2IDX2 FIG_CO2SEC GRAF Petroleum LPG Distillate Fuel Kerosene Coal Natural Gas Total Motor Gasoline Residual Fuel Lubricants Asphalt & Road Oil

334

Workbook Contents  

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

Refinery Yield of Kerosene (Percent)","U.S. Refinery Yield of Distillate Fuel Oil (Percent)","U.S. Refinery Yield of Residual Fuel Oil (Percent)","U.S. Refinery Yield...

335

Georgia, Republic of Exports of Crude Oil and Petroleum Products ...  

U.S. Energy Information Administration (EIA)

Distillate Fuel Oil : 0 : 2011-2011: Greater than 15 to 500 ppm Sulfur : 0 : 2011-2011: Kerosene-Type Jet Fuel : 475: 1: 2011-2012: Special Naphthas : 2 : 2005-2008:

336

Low Distillate Stocks Set Stage for Price Volatility  

U.S. Energy Information Administration (EIA)

This distillate price spike is a classic response to a local supply and demand imbalance that began as a result of low distillate stocks. Low distillate stocks in the ...

337

Distillate and Crude Oil Price  

Gasoline and Diesel Fuel Update (EIA)

fuel and residential heating oil prices on the East Coast is being driven by higher crude oil prices than last year and higher spreads. Crude oil is projected to average almost...

338

Fuels  

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

Goals > Fuels Goals > Fuels XMAT for nuclear fuels XMAT is ideally suited to explore all of the radiation processes experienced by nuclear fuels.The high energy, heavy ion accleration capability (e.g., 250 MeV U) can produce bulk damage deep in the sample, achieving neutron type depths (~10 microns), beyond the range of surface sputtering effects. The APS X-rays are well matched to the ion beams, and are able to probe individual grains at similar penetrations depths. Damage rates to 25 displacements per atom per hour (DPA/hr), and doses >2500 DPA can be achieved. MORE» Fuels in LWRs are subjected to ~1 DPA per day High burn-up fuel can experience >2000 DPA. Traditional reactor tests by neutron irradiation require 3 years in a reactor and 1 year cool down. Conventional accelerators (>1 MeV/ion) are limited to <200-400 DPAs, and

339

GeneDistiller—Distilling Candidate Genes from Linkage Intervals  

E-Print Network (OSTI)

Background: Linkage studies often yield intervals containing several hundred positional candidate genes. Different manual or automatic approaches exist for the determination of the gene most likely to cause the disease. While the manual search is very flexible and takes advantage of the researchers ’ background knowledge and intuition, it may be very cumbersome to collect and study the relevant data. Automatic solutions on the other hand usually focus on certain models, remain ‘‘black boxes’ ’ and do not offer the same degree of flexibility. Methodology: We have developed a web-based application that combines the advantages of both approaches. Information from various data sources such as gene-phenotype associations, gene expression patterns and protein-protein interactions was integrated into a central database. Researchers can select which information for the genes within a candidate interval or for single genes shall be displayed. Genes can also interactively be filtered, sorted and prioritised according to criteria derived from the background knowledge and preconception of the disease under scrutiny. Conclusions: GeneDistiller provides knowledge-driven, fully interactive and intuitive access to multiple data sources. It displays maximum relevant information, while saving the user from drowning in the flood of data. A typical query takes less than two seconds, thus allowing an interactive and explorative approach to the hunt for the candidate gene.

Dominik Seelow; Jana Marie Schwarz; Markus Schuelke

2008-01-01T23:59:59.000Z

340

Predicting the products of crude oil distillation columns.  

E-Print Network (OSTI)

??Crude oil distillation systems, consisting of crude oil distillation columns and the associated heat recovery systems, are highly energy intensive. Heat-integrated design of crude oil… (more)

Liu, Jing

2012-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Vacuum distillation is a key part of the petroleum refining ...  

U.S. Energy Information Administration (EIA)

About 80% of the refineries operating in the United States have a vacuum distillation unit (VDU), a secondary processing unit consisting of vacuum distillation columns.

342

EIA/NASEO Winter Fuels Conference - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Heating Fuel Stock Cycles. ... Retail Heating Oil Prices Should Be Lower This Year. Heating Degree-Days. Normal Weather Will Bring Higher Demand. Distillate Production.

343

Distillation: Present Status and Future Directions  

E-Print Network (OSTI)

Distillation will undoubtedly continue to be the most-used method for separating liquid mixtures, at any scale of operation. For this reason, and also because of its recognized energy intensiveness, distillation commands continued scrutiny with respect to cost-effective improvements. In this paper, the authors suggest fruitful areas of research that can lead to lower cost distillation separations. The areas of research are classified under the headings of phase equilibrium, material and energy balances, mass transfer efficiencies, equipment design, and system energy consumption. For each of the categories, a summary is given of the present status of the technology as well as directions that improvement-type investigations might take.

Fair, J. R.; Humphrey, J. L.

1984-01-01T23:59:59.000Z

344

On two-distillable Werner states  

E-Print Network (OSTI)

We consider bipartite mixed states in a d x d quantum system with d at least 3. We say that such a state is PPT if its partial transpose is positive semidefinite, and otherwise that it is NPT. The well-known Werner states are partitioned into three types: a) the separable states (same as the PPT states), b) the 1-distillable states (necessarily NPT), and c) the NPT states which are not 1-distillable. We give several different formulations and provide further evidence for validity of the conjecture that the type c) Werner states are not 2-distillable.

Dragomir Z. Djokovic

2010-03-23T23:59:59.000Z

345

"Characteristic(a)","Total","Fuel Oil","Fuel Oil(b)","Natural...  

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

ual","Distillate",,"LPG and",,"Coke and"," " "Characteristic(a)","Total","Fuel Oil","Fuel Oil(b)","Natural Gas(c)","NGL(d)","Coal","Breeze","Other(e)" ,"Total United States" "Value...

346

Emergency fuels utilization guidebook. Alternative Fuels Utilization Program  

DOE Green Energy (OSTI)

The basic concept of an emergency fuel is to safely and effectively use blends of specification fuels and hydrocarbon liquids which are free in the sense that they have been commandeered or volunteered from lower priority uses to provide critical transportation services for short-duration emergencies on the order of weeks, or perhaps months. A wide variety of liquid hydrocarbons not normally used as fuels for internal combustion engines have been categorized generically, including limited information on physical characteristics and chemical composition which might prove useful and instructive to fleet operators. Fuels covered are: gasoline and diesel fuel; alcohols; solvents; jet fuels; kerosene; heating oils; residual fuels; crude oils; vegetable oils; gaseous fuels.

Not Available

1980-08-01T23:59:59.000Z

347

Winter Fuels Outlook Conference 2010  

Reports and Publications (EIA)

This presentation at the 2010 Winter Fuels Outlook Conference in Washington, DC, outlined EIA's current forecast for U.S. crude oil, distillate, natural gas, propane and gasoline supply, demand, and markets over the coming winter season.

2010-10-13T23:59:59.000Z

348

U.S. Distillate Market Testimony  

Gasoline and Diesel Fuel Update (EIA)

5 Notes: The Northeast distillate market is experiencing some difficulties that are being reflected in prices. Residential heating oil prices on January 24 were up 35-60 cents per...

349

Distillate Stocks Expected to Remain Low  

Gasoline and Diesel Fuel Update (EIA)

8 Notes: When EIA's demand forecast is combined with its outlook for production and net imports, distillate stocks are projected to remain low for the rest of the year. - Stocks...

350

Distillate Stocks Expected to Remain Low  

U.S. Energy Information Administration (EIA)

When EIA’s demand forecast is combined with its outlook for production and net imports, distillate stocks are projected to remain low for the rest of the year.

351

Minimizing corrosion in coal liquid distillation  

DOE Patents (OSTI)

In an atmospheric distillation tower of a coal liquefaction process, tower materials corrosion is reduced or eliminated by introduction of boiling point differentiated streams to boiling point differentiated tower regions.

Baumert, Kenneth L. (Emmaus, PA); Sagues, Alberto A. (Lexington, KY); Davis, Burtron H. (Georgetown, KY)

1985-01-01T23:59:59.000Z

352

Distillers Grains: Production, Properties, and Utilization  

Science Conference Proceedings (OSTI)

During the past several years, distillers dried grains with solubles (known as DDGS) has become a major feed ingredient in North America, and its use is increasing globally. This book provides a comprehensive summary of the research conducted to determine

353

Forecast U.S. Distillate Stocks  

Gasoline and Diesel Fuel Update (EIA)

EIA is not projecting a large recovery over the summer, but because refineries are forecast to run at high utilization rates, they may produce more distillate than expected and...

354

Entanglement of Distillation and Conditional Mutual Information  

E-Print Network (OSTI)

In previous papers, we expressed the Entanglement of Formation in terms of Conditional Mutual Information (CMI). In this brief paper, we express the Entanglement of Distillation in terms of CMI.

Robert R. Tucci

2002-02-25T23:59:59.000Z

355

Development of energy efficient membrane distillation systems  

E-Print Network (OSTI)

Membrane distillation (MD) has shown potential as a means of desalination and water purification. As a thermally driven membrane technology which runs at relatively low pressure, which can withstand high salinity feed ...

Summers, Edward K

2013-01-01T23:59:59.000Z

356

INTERIM VALIDATION REPORT MIDDLE DISTILLATE PRICE MONITORING SYSTEM  

E-Print Network (OSTI)

on the price of home heating oil may also be obtained byincluding kerosene, home heating oil, range oil, stove oil,to most marketers of home heating oil. Consequently, during

Hopelain, D.G.

2011-01-01T23:59:59.000Z

357

Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes  

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

33,033.1 32,893.1 32,452.7 33,281.4 32,532.8 30,000.3 1983-2013 33,033.1 32,893.1 32,452.7 33,281.4 32,532.8 30,000.3 1983-2013 East Coast (PADD 1) 8,170.7 7,484.8 7,317.4 7,494.1 7,085.1 5,550.5 1983-2013 New England (PADD 1A) W W W 337.4 390.2 279.7 1983-2013 Connecticut W W W W W W 1984-2013 Maine W W W W W W 1984-2013 Massachusetts W W W W W W 1984-2013 New Hampshire - - - W - - 1984-2013 Rhode Island W W W W W W 1984-2013 Vermont - - - - - - 1984-2013 Central Atlantic (PADD 1B) 4,254.7 4,171.6 4,469.2 4,834.6 4,713.8 3,787.7 1983-2013 Delaware - - - - - - 1984-2013 District of Columbia - - - - - - 1984-2013 Maryland W W W W W W 1984-2013 New Jersey 2,477.5 2,444.1 2,660.1 2,524.8 2,448.5 1,789.9 1984-2013 New York 1,435.8 1,430.6 1,480.5 W W W 1984-2013

358

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane, and Kerosene,  

Gasoline and Diesel Fuel Update (EIA)

PAD District I 1983 ...................................... 127.8 123.0 87.0 87.8 91.3 52.8 94.5 90.1 1984 ...................................... 124.7 119.5 83.5 85.0 93.3 50.9 106.0 92.2 1985 ...................................... 121.4 115.3 78.5 82.2 91.5 44.9 104.9 88.1 1986 ...................................... 100.6 91.8 52.8 52.2 86.0 32.7 81.0 61.6 1987 ...................................... 90.9 85.0 54.1 55.6 82.3 31.0 78.1 58.9 1988 ...................................... 89.5 82.9 51.2 51.3 84.8 29.8 73.3 55.3 1989 ...................................... 99.2 92.2 59.1 60.1 75.8 29.2 69.3 67.2 1990 ...................................... 112.3 105.3 75.9 78.3 91.8 45.0 86.4 84.4 1991 ...................................... 105.6 100.3 65.3 67.2 W 40.5 81.0 74.0 1992 ......................................

359

Prices of Refiner Kerosene-Type Jet Fuel Sales to End Users  

Gasoline and Diesel Fuel Update (EIA)

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History U.S. 2.165 3.052 1.704 2.201 3.054 3.104 1978-2012 East Coast (PADD 1) 2.161 3.068 1.707 2.201 3.064 3.126 1983-2012 New England (PADD 1A) 2.224 3.113 1.737 2.216 3.098 3.179 1983-2012 Connecticut 2.222 W W W W W 1983-2012 Maine W W W W W W 1983-2012 Massachusetts W W W W 3.088 3.154 1983-2012 New Hampshire W W W W W - 1983-2012 Rhode Island W W W W W W 1983-2012 Vermont W W - - - W 1983-2012 Central Atlantic (PADD 1B) 2.158 3.080 1.694 2.192 3.060 3.116 1983-2012 Delaware W - - W - - 1983-2012 District of Columbia - - - - - - 1983-2012 Maryland 2.151 2.962 1.645 2.198 3.039 W 1983-2012 New Jersey 2.106 3.014 1.684 2.182 3.050 3.105 1983-2012

360

East Coast (PADD 1) Product Supplied of Kerosene-Type Jet Fuel ...  

U.S. Energy Information Administration (EIA)

456: 507: 447: 462: 433: 511: 459: 457: 482: 491: 1991: 557: 487: 490: 401: 389: 420: 500: 477: 423: 424: 433: 487: 1992: 462: 456: 384: 441: 386: 465: 463: 472: 432 ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

U.S. Exports to Panama of Kerosene-Type Jet Fuel (Thousand ...  

U.S. Energy Information Administration (EIA)

456: 90: 389: 627: 503: 300: 411-= No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data.

362

Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes  

Gasoline and Diesel Fuel Update (EIA)

2007 2008 2009 2010 2011 2012 View 2007 2008 2009 2010 2011 2012 View History U.S. 40,136.3 39,913.9 37,954.6 34,775.2 33,272.0 32,545.7 1983-2012 East Coast (PADD 1) 9,039.8 9,693.3 9,041.1 8,730.4 7,785.9 6,813.2 1983-2012 New England (PADD 1A) 606.3 930.0 766.0 790.7 679.4 373.7 1983-2012 Connecticut 171.1 W W W W W 1983-2012 Maine W W W W W W 1983-2012 Massachusetts W W W W 495.6 189.3 1983-2012 New Hampshire W W W W W - 1983-2012 Rhode Island W W W W W W 1983-2012 Vermont W W - - - W 1983-2012 Central Atlantic (PADD 1B) 4,645.2 4,946.6 5,127.5 4,696.7 3,983.7 3,569.8 1983-2012 Delaware W - - W - - 1983-2012 District of Columbia - - - - - - 1983-2012 Maryland W 209.8 210.3 190.8 177.5 W 1983-2012 New Jersey 1,463.5 1,555.6 2,006.2 1,922.4 1,913.2 1,646.2 1983-2012

363

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane, and Kerosene,  

Gasoline and Diesel Fuel Update (EIA)

PAD District I 1983 ...................................... 127.8 123.0 87.0 87.8 91.3 52.8 94.5 90.1 1984 ...................................... 124.7 119.5 83.5 85.0 93.3 50.9 106.0 92.2 1985 ...................................... 121.4 115.3 78.5 82.2 91.5 44.9 104.9 88.1 1986 ...................................... 100.6 91.8 52.8 52.2 86.0 32.7 81.0 61.6 1987 ...................................... 90.9 85.0 54.1 55.6 82.3 31.0 78.1 58.9 1988 ...................................... 89.5 82.9 51.2 51.3 84.8 29.8 73.3 55.3 1989 ...................................... 99.2 92.2 59.1 60.1 75.8 29.2 69.3 67.2 1990 ...................................... 112.3 105.3 75.9 78.3 91.8 45.0 86.4 84.4 1991 ...................................... 105.6 100.3 65.3 67.2 W 40.5 81.0 74.0 1992 ......................................

364

Prices of Refiner Kerosene-Type Jet Fuel Sales to End Users  

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

2.922 2.787 2.813 2.908 3.002 3.040 1975-2013 2.922 2.787 2.813 2.908 3.002 3.040 1975-2013 East Coast (PADD 1) 2.907 2.783 2.825 2.919 3.028 3.055 1983-2013 New England (PADD 1A) W W W 2.973 3.085 3.129 1983-2013 Connecticut W W W W W W 1984-2013 Maine W W W W W W 1984-2013 Massachusetts W W W W W W 1984-2013 New Hampshire - - - W - - 1984-2013 Rhode Island W W W W W W 1984-2013 Vermont - - - - - - 1984-2013 Central Atlantic (PADD 1B) 2.899 2.763 2.816 2.904 3.011 3.043 1983-2013 Delaware - - - - - - 1984-2013 District of Columbia - - - - - - 1984-2013 Maryland W W W W W W 1984-2013 New Jersey 2.881 2.748 2.805 2.895 3.003 3.038 1984-2013 New York 2.930 2.788 2.830 W W W 1984-2013 Pennsylvania 2.906 2.766 2.852 2.908 3.018 3.020 1984-2013

365

Table A2. Refiner/Reseller Prices of Aviation Fuels, Propane, and Kerosene,  

Gasoline and Diesel Fuel Update (EIA)

PAD District I 1983 ...................................... 127.8 123.0 87.0 87.8 91.3 52.8 94.5 90.1 1984 ...................................... 124.7 119.5 83.5 85.0 93.3 50.9 106.0 92.2 1985 ...................................... 121.4 115.3 78.5 82.2 91.5 44.9 104.9 88.1 1986 ...................................... 100.6 91.8 52.8 52.2 86.0 32.7 81.0 61.6 1987 ...................................... 90.9 85.0 54.1 55.6 82.3 31.0 78.1 58.9 1988 ...................................... 89.5 82.9 51.2 51.3 84.8 29.8 73.3 55.3 1989 ...................................... 99.2 92.2 59.1 60.1 75.8 29.2 69.3 67.2 1990 ...................................... 112.3 105.3 75.9 78.3 91.8 45.0 86.4 84.4 1991 ...................................... 105.6 100.3 65.3 67.2 W 40.5 81.0 74.0 1992 ......................................

366

U.S. Imports from Singapore of Kerosene-Type Jet Fuel (Thousand ...  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2004: 308: 101: 358: 292: 418: 465: 295: 252: 2005: 840: 27: 550: 249: 300: 314: 2006: 304: 314: 660: 329: 331 ...

367

Weekly East Coast (PADD 1) Ending Stocks of Kerosene-Type Jet Fuel ...  

U.S. Energy Information Administration (EIA)

9,977 : 04/20 : 9,525 : 04/27 : 8,585 : 2012-May: 05/04 : 8,884 : 05/11 : 8,607 : 05/18 : 10,044 : 05/25 : 10,075 : 2012-Jun: 06/01 : 9,465 : 06/08 : 10,058 : 06/15 :

368

Refining District Texas Gulf Coast Kerosene-Type Jet Fuel Stocks ...  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1993: 3,029: 3,968: 3,482: 3,284: 3,543: 3,978: 3,501: 3,707: 2,993: 2,931: 3,003: 2,636: 1994: 3,924: 3,273 ...

369

Cat. Hydro.. Kerosene/Jet Fuel Downstream Charge Capacity (B/SD)  

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 ...

370

Michigan Kerosene-Type Jet Fuel All Sales/Deliveries by Prime ...  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's: 276.4: 475.2: 567.8: 603.9: 716.4: 715.9: 785.3: 1990's: 887.4: 869.1: 917.2 ...

371

U.S. Exports to Nigeria of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2008: 276: 586: 551: 241: 2009: 313: 592: 594: 2010: 276: 249: 300: 751: 328: 295: 285: 276: 303: 2011: 277: 563 ...

372

U.S. Product Supplied of Kerosene-Type Jet Fuel (Thousand Barrels ...  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1965: 316: 285: 316: 312: 335: 330: 349: 345: 371: 334: 334: 372: 1966: 364: 401: 391: 426: 369: 421: 291: 306 ...

373

Table 5.15 Fuel Oil and Kerosene Sales, 1984-2010 (Thousand ...  

U.S. Energy Information Administration (EIA)

Short-Term Energy Outlook › Annual Energy Outlook ... Sources: - 1984-U.S. Energy Information Administration (EIA), Petroleum Marketing Annual 1988

374

Cat. Hydro.. Kerosene/Jet Fuel Downstream Charge Capacity (B/SD)  

U.S. Energy Information Administration (EIA)

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

375

West Coast (PADD 5) Refinery Yield of Kerosene-Type Jet Fuel (Percent)  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1990's: 15.1: 15.7: 16.1: 17.9: 17.3: 16.5: 15.8: 2000's: 16.2: 16.0: 16.0: 16.0: 16.2 ...

376

Weekly U.S. Product Supplied of Kerosene-Type Jet Fuel (Thousand ...  

U.S. Energy Information Administration (EIA)

Year-Month Week 1 Week 2 Week 3 Week 4 Week 5; End Date Value End Date Value End Date Value End Date Value End Date Value; 1991-Feb : 02/08 : 1,466 : 02/15 : 1,226

377

U.S. Refinery Yield of Kerosene-Type Jet Fuel (Percent)  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1990's: 9.2: 9.8: 9.7: 10.4: 10.3: 9.9: 10.2: 2000's: 10.3: 9.8: 9.8: 9.5: 9.7: 9.8: 9.3 ...

378

Weekly U.S. Ending Stocks of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

Year-Month Week 1 Week 2 Week 3 Week 4 Week 5; End Date Value End Date Value End Date Value End Date Value End Date Value; 1982-Aug : 08/20 : 33,523 : 08/27

379

Kerosene-Type Jet Fuel Sales to End Users Refiner Sales Volumes  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: Values shown for the ...

380

U.S. Product Supplied of Kerosene-Type Jet Fuel (Thousand Barrels ...  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1970's: 842: 771: 791: 789: 831: 858: 876: 1980's: 851: 809: 804: 839: 953: 1,005: 1,105 ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Net Imports of Kerosene-Type Jet Fuel into the U.S. by Country  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

382

Alabama Kerosene-Type Jet Fuel Retail Sales by Refiners (Thousand ...  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's: 81.5: 89.7: 79.0: 75.4: 74.1: 79.3: 84.2: 1990's: 100.4: 96.7: W: 105.9: 108.2 ...

383

U.S. Imports from Malaysia of Kerosene-Type Jet Fuel (Thousand ...  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 2004: 311: 2005: 200: 2008: 301: 2010: 30: 212: 301: 2012: 310-

384

Kerosene-Type Jet Fuel Imports from OPEC - U.S. Energy Information ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

385

Kerosene-Type Jet Fuel Movements by Pipeline between PAD Districts  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: RBOB with Ether and RBOB ...

386

Weekly U.S. Exports of Kerosene-Type Jet Fuel (Thousand Barrels ...  

U.S. Energy Information Administration (EIA)

Year-Month Week 1 Week 2 Week 3 Week 4 Week 5; End Date Value End Date Value End Date Value End Date Value End Date Value; 2010-Jun: 06/04 : 59 : 06/11 : 59 : 06/18

387

Weekly U.S. Imports of Kerosene-Type Jet Fuel (Thousand Barrels ...  

U.S. Energy Information Administration (EIA)

Year-Month Week 1 Week 2 Week 3 Week 4 Week 5; End Date Value End Date Value End Date Value End Date Value End Date Value; 1982-Aug : 08/20 : 24 : 08/27 : 0

388

U.S. Exports of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec; 1981: 28: 21: 10: 18: 16: 12: 19: 22: 20: 14: 23: 222: 1982: 255: 245: 80: 44: 27: 38: 32: 32: 41: 35: 269: 692 ...

389

U.S. Exports to Haiti of Kerosene-Type Jet Fuel (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 2000's: 0: 2: 2010's: 0-

390

Weekly West Coast (PADD 5) Imports of Kerosene-Type Jet Fuel ...  

U.S. Energy Information Administration (EIA)

Year-Month Week 1 Week 2 Week 3 Week 4 Week 5; End Date Value End Date Value End Date Value End Date Value End Date Value; 2004-Apr : 04/09 : NA : 04/16 : NA : 04/23

391

U.S. Imports of Kerosene-Type Jet Fuel (Thousand Barrels per Day)  

U.S. Energy Information Administration (EIA)

Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9; 1980's: 29: 48: 30: 48: 64: 87: 102: 1990's: 100: 55: 74: 90: 107: 96: 109: 91: 124: 128 ...

392

Kerosene-Type Jet Fuel Movements by Tanker and Barge between PAD ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: RBOB with Ether and RBOB ...

393

Price of Motor Gasoline Through Retail Outlets  

Gasoline and Diesel Fuel Update (EIA)

Prices, Sales Volumes & Stocks by State Prices, Sales Volumes & Stocks by State (Dollars per Gallon Excluding Taxes) Data Series: Retail Price - Motor Gasoline Retail Price - Regular Gasoline Retail Price - Midgrade Gasoline Retail Price - Premium Gasoline Retail Price - Aviation Gasoline Retail Price - Kerosene-Type Jet Fuel Retail Price - Propane Retail Price - Kerosene Retail Price - No. 1 Distillate Retail Price - No. 2 Distillate Retail Price - No. 2 Fuel Oil Retail Price - No. 2 Diesel Fuel Retail Price - No. 4 Fuel Oil Prime Supplier Sales - Motor Gasoline Prime Supplier Sales - Regular Gasoline Prime Supplier Sales - Midgrade Gasoline Prime Supplier Sales - Premium Gasoline Prime Supplier Sales - Aviation Gasoline Prime Supplier Sales - Kerosene-Type Jet Fuel Prime Supplier Sales - Propane (Consumer Grade) Prime Supplier Sales - Kerosene Prime Supplier Sales - No. 1 Distillate Prime Supplier Sales - No. 2 Distillate Prime Supplier Sales - No. 2 Fuel Oil Prime Supplier Sales - No. 2 Diesel Fuel Prime Supplier Sales - No. 4 Fuel Oil Prime Supplier Sales - Residual Fuel Oil Stocks - Finished Motor Gasoline Stocks - Reformulated Gasoline Stocks - Conventional Gasoline Stocks - Motor Gasoline Blending Components Stocks - Kerosene Stocks - Distillate Fuel Oil Stocks - Distillate F.O., 15 ppm and under Sulfur Stocks - Distillate F.O., Greater than 15 to 500 ppm Sulfur Stocks - Distillate F.O., Greater 500 ppm Sulfur Stocks - Residual Fuel Oil Stocks - Propane/Propylene Period: Monthly Annual

394

Energy Recovery in Industrial Distillation Processes  

E-Print Network (OSTI)

Distillation processes are energy intensive separation processes which present attractive opportunities for energy conservation. Through the use of multistage vapor recompression, heat which is normally unavailable can be delivered at suitably high temperatures resulting in significant energy savings. The distillation process will be reviewed as it relates to both vapor recompression and heat pumping techniques and case study examples of these energy recovery methods will be discussed.

Paul, D. B.

1983-01-01T23:59:59.000Z

395

Multipartite secret key distillation and bound entanglement  

Science Conference Proceedings (OSTI)

Recently it has been shown that quantum cryptography beyond pure entanglement distillation is possible and a paradigm for the associated protocols has been established. Here we systematically generalize the whole paradigm to the multipartite scenario. We provide constructions of new classes of multipartite bound entangled states, i.e., those with underlying twisted Greenberger-Horne-Zeilinger (GHZ) structure and nonzero distillable cryptographic key. We quantitatively estimate the key from below with the help of the privacy squeezing technique.

Augusiak, Remigiusz; Horodecki, Pawel [Faculty of Applied Physics and Mathematics, Gdansk University of Technology, Narutowicza 11/12, 80-952 Gdansk (Poland) and ICFO-Institute Ciencies Fotoniques, Mediterranean Technology Park, 08860 Castelldefels (Barcelona) (Spain); Faculty of Applied Physics and Mathematics, Gdansk University of Technology, Narutowicza 11/12, 80-952 Gdansk (Poland)

2009-10-15T23:59:59.000Z

396

MECS Fuel Oil Figures  

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

: Percentage of Total Purchased Fuels by Type of Fuel : Percentage of Total Purchased Fuels by Type of Fuel Figure 1. Percent of Total Purchased Fuel Sources: Energy Information Administration. Office of Energy Markets and End Use, Manufacturing Energy Consumption Survey (MECS): Consumption of Energy; U.S. Department of Commerce, Bureau of the Census, Annual Survey of Manufactures (ASM): Statistics for Industry Groups and Industries: Statistical Abstract of the United States. Note: The years below the line on the "X" Axis are interpolated data--not directly from the Manufacturing Energy Consumption Survey or the Annual Survey of Manufactures. Figure 2: Changes in the Ratios of Distillate Fuel Oil to Natural Gas Figure 2. Changes in the Ratios of Distillate Fuel Oil to Natural Gas Sources: Energy Information Administration. Office of

397

INTERIM VALIDATION REPORT MIDDLE DISTILLATE PRICE MONITORING SYSTEM  

E-Print Network (OSTI)

GLOSSARY. • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .for LBL by EIA staff. V. GLOSSARY "Middle distillate" means

Hopelain, D.G.

2011-01-01T23:59:59.000Z

398

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)

399

Weekly Rocky Mountains (PADD 4) Operable Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

Weekly Rocky Mountains (PADD 4) Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)

400

Weekly West Coast (PADD 5) Operable Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

Weekly West Coast (PADD 5) Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)

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


401

Texas Inland Refining District Operable Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

Texas Inland Refining District Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)

402

Weekly East Coast (PADD 1) Operable Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

Weekly East Coast (PADD 1) Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)

403

East Coast Refining District Operable Crude Oil Distillation ...  

U.S. Energy Information Administration (EIA)

East Coast Refining District Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)

404

Respiratory symptoms in Indian women using domestic cooking fuels  

SciTech Connect

The effect of domestic cooking fuels producing various respiratory symptoms was studied in 3,701 women. Of these, 3,608 were nonsmoking women who used four different types of cooking fuels: biomass, LPG, kerosene, and mixed fuels. The overall respiratory symptoms were observed in 13 percent of patients. Mixed fuel users experienced more respiratory symptoms (16.7 percent), followed by biomass (12.6 percent), stove (11.4 percent), and LPG (9.9 percent). Chronic bronchitis in chulla users was significantly higher than that in kerosene and LPG users (p less than 0.05). Dyspnea and postnasal drip were significantly higher in the women using mixed fuels. Smoking women who are also exposed to cooking fuels experienced respiratory symptoms more often than nonsmokers (33.3 percent vs 13 percent).

Behera, D.; Jindal, S.K. (Postgraduate Institute of Medical Education and Research, Chandigarh (India))

1991-08-01T23:59:59.000Z

405

Distillate Stocks on the East Coast Were Very Low Entering Last Winter  

Gasoline and Diesel Fuel Update (EIA)

4 4 Notes: So, what happened last winter? At last year's SHOPP conference, my renowned colleague, Joanne Shore, warned of the potential for high prices. At this time last year, distillate stocks were very low. This graph shows East Coast inventories, which at the end of July 2000, were well below the normal band. We focus on the East Coast (PADD 1) because this is a region in which heating oil is a major winter fuel. Furthermore, the East Coast consumes almost 2/3 of the nation's heating oil (high sulfur distillate). East Coast stocks were well below normal last year from July through December, but then actually increased in January, when they typically decline. In fact, the increase was only the 2nd time East Coast distillate stocks have increased in January since EIA has kept PADD level data (1981)!

406

Fuel  

E-Print Network (OSTI)

heavy-water-moderated, light-water-moderated and liquid-metal cooled fast breeder reactors fueled with natural or low-enriched uranium and containing thorium mixed with the uranium or in separate target channels. U-232 decays with a 69-year half-life through 1.9-year half-life Th-228 to Tl-208, which emits a 2.6 MeV gamma ray upon decay. We find that pressurized light-water-reactors fueled with LEU-thorium fuel at high burnup (70 MWd/kg) produce U-233 with U-232 contamination levels of about 0.4 percent. At this contamination level, a 5 kg sphere of U-233 would produce a gammaray dose rate of 13 and 38 rem/hr at 1 meter one and ten years after chemical purification respectively. The associated plutonium contains 7.5 percent of the undesirable heat-generating 88-year half-life isotope Pu-238. However, just as it is possible to produce weapon-grade plutonium in low-burnup fuel, it is also practical to use heavy-water reactors to produce U-233 containing only a few ppm of U-232 if the thorium is segregated in “target ” channels and discharged a few times more frequently than the natural-uranium “driver ” fuel. The dose rate from a 5-kg solid sphere of U-233 containing 5 ppm U-232 could be reduced by a further factor of 30, to about 2 mrem/hr, with a close-fitting lead sphere weighing about 100 kg. Thus the proliferation resistance of thorium fuel cycles depends very much upon how they are implemented. The original version of this manuscript was received by Science & Global Security on

Jungmin Kang A

2001-01-01T23:59:59.000Z

407

Local purity distillation with bounded classical communication  

E-Print Network (OSTI)

Local pure states are an important resource for quantum computing. The problem of distilling local pure states from mixed ones can be cast in an information theoretic paradigm. The bipartite version of this problem where local purity must be distilled from an arbitrary quantum state shared between two parties, Alice and Bob, is closely related to the problem of separating quantum and classical correlations in the state and in particular, to a measure of classical correlations called the one-way distillable common randomness. In Phys. Rev. A 71, 062303 (2005), the optimal rate of local purity distillation is derived when many copies of a bipartite quantum state are shared between Alice and Bob, and the parties are allowed unlimited use of a unidirectional dephasing channel. In the present paper, we extend this result to the setting in which the use of the channel is bounded. We demonstrate that in the case of a classical-quantum system, the expression for the local purity distilled is efficiently computable and provide examples with their tradeoff curves.

Hari Krovi; Igor Devetak

2007-05-28T23:59:59.000Z

408

Table 3.3 Fuel Consumption, 2002  

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

3 Fuel Consumption, 2002;" 3 Fuel Consumption, 2002;" " Level: National and Regional Data; " " Row: Values of Shipments and Employment Sizes;" " Column: Energy Sources;" " Unit: Trillion Btu." " "," "," "," "," "," "," "," "," "," "," " " "," ",," "," ",," "," ",," ","RSE" "Economic",,"Net","Residual","Distillate","Natural ","LPG and",,"Coke and"," ","Row" "Characteristic(a)","Total","Electricity(b)","Fuel Oil","Fuel Oil(c)","Gas(d)","NGL(e)","Coal","Breeze","Other(f)","Factors"

409

Spot Distillate & Crude Oil Prices  

Gasoline and Diesel Fuel Update (EIA)

5 5 Notes: Retail distillate prices follow the spot distillate markets, and crude oil prices have been the main driver behind distillate spot price increases until recently. Crude oil rose about 36 cents per gallon from its low point in mid February 1999 to the middle of January 2000. Over this same time period, New York Harbor spot heating oil had risen about 42 cents per gallon, reflecting both the crude price rise and a return to a more usual seasonal spread over the price of crude oil. The week ending January 21, heating oil spot prices in the Northeast spiked dramatically to record levels, closing on Friday at $1.26 per gallon -- up 50 cents from the prior week. Gulf Coast prices were not spiking, but were probably pulled slightly higher as the New York Harbor market began to

410

Distillation of local purity from quantum states  

E-Print Network (OSTI)

Recently Horodecki et al. [Phys. Rev. Lett. 90, 100402 (2003)] introduced an important quantum information processing paradigm, in which two parties sharing many copies of the same bipartite quantum state distill local pure states, by means of local unitary operations assisted by a one-way (two-way) completely dephasing channel. Local pure states are a valuable resource from a thermodynamical point of view, since they allow thermal energy to be converted into work by local quantum heat engines. We give a simple information-theoretical characterization of the one-way distillable local purity, which turns out to be closely related to a previously known operational measure of classical correlations, the one-way distillable common randomness.

I. Devetak

2004-06-30T23:59:59.000Z

411

Entanglement Distillation Protocols and Number Theory  

E-Print Network (OSTI)

We show that the analysis of entanglement distillation protocols for qudits of arbitrary dimension $D$ benefits from applying basic concepts from number theory, since the set $\\zdn$ associated to Bell diagonal states is a module rather than a vector space. We find that a partition of $\\zdn$ into divisor classes characterizes the invariant properties of mixed Bell diagonal states under local permutations. We construct a very general class of recursion protocols by means of unitary operations implementing these local permutations. We study these distillation protocols depending on whether we use twirling operations in the intermediate steps or not, and we study them both analitically and numerically with Monte Carlo methods. In the absence of twirling operations, we construct extensions of the quantum privacy algorithms valid for secure communications with qudits of any dimension $D$. When $D$ is a prime number, we show that distillation protocols are optimal both qualitatively and quantitatively.

H. Bombin; M. A. Martin-Delgado

2005-03-01T23:59:59.000Z

412

Advanced Distillation: Programs Proposed to DOE  

E-Print Network (OSTI)

EPRI has provided proposal preparation assistance and offered cost share funding assistance for two projects proposed in 2000. EPRI is highly interested, since this technology is applicable in all distillation systems, and since it will increase electric load in capacity increase revamps, probably the best economic targets in the U.S., since capital savings are best here. The approach can typically reduce energy use requirements, cooling (water) requirements, and environmental emissions per pound of distillate by 50%, while substantially reducing capital requirements for capacity increase revamps and new construction. If just 20% of all U.S. distillation were revamped by this approach as apposed to conventional, about 5x10^14 BTUs per year in energy use could be avoided, while increasing production by about 20%. Both the proposed petroleum refining (not awarded) and chemical industry programs and participants are described. As of this writing (1/31/01), chemical industry award selections have not yet been made.

Woinsky, S. G.

2001-05-01T23:59:59.000Z

413

PROCEDURE FOR THE DETERMINATION OF DISTILLATION POINTS OF LIQUID FUELS BY AUTOMATED DISTILLATION  

E-Print Network (OSTI)

This report has been reviewed by the staff of the California Air Resources Board and approved for publication. Approval does not signify that the contents necessarily reflect the views and policies of the Air Resources Board, nor does mention of trade names or commercial products constitute endorsement or recommendation for use. SOP MLD No. 128

Sop No. Mld; Southern Laboratory Branch

2002-01-01T23:59:59.000Z

414

Electric Driven Heat Pumps in Distillation Processes  

E-Print Network (OSTI)

Radian Corporation, under contract to the Electric Power Research Institute, has recently completed a study of the potential range of application for retrofitting electric driven heat pumps to existing distillation columns. A computerized evaluation program was developed, consisting of simulation, cost estimation, and economics analysis. The simulations were done using the PROCESS simulation package, while the cost and economics analysis routines were developed by Radian. This paper summarizes the results of the evaluations of retrofits to four generic distillation processes. In addition, the bases of the evaluation programs and the results of several peripheral tasks are described briefly.

Harris, G. E.

1983-01-01T23:59:59.000Z

415

Northeast Heating Fuel Market The, Assessment and Options  

Reports and Publications (EIA)

In response to the President's request, this study examineshow the distillate fuel oil market (and related energy markets) in the Northeast behaved in the winter of 1999-2000, explains the role played by residential,commercial, industrial, and electricity generation sectorconsumers in distillate fuel oil markets and describes how that role is influenced by the structure of the energy markets in the Northeast

Joan Heinkel

2000-05-01T23:59:59.000Z

416

www.eia.gov  

U.S. Energy Information Administration (EIA)

Table 8 FIG_CO2IDX1 FIG_CO2IDX2 FIG_CO2SEC GRAF Petroleum LPG Distillate Fuel Kerosene Coal Natural Gas Total aShare of total electric power sector carbon dioxide ...

417

Heat integrated distillation in a plate-packing HIDiC.  

E-Print Network (OSTI)

??Distillation is an energy intensive separation method. To improve the exergetic efficiency of a distillation column, it can be designed as a heat integrated distillation… (more)

Krikken, T.

2011-01-01T23:59:59.000Z

418

Energy Conservation Options in Distillation Processes  

E-Print Network (OSTI)

This paper summarizes the results of a survey of energy conservation options applicable to distillation processes. Over twenty such options were identified, and eight of these were selected for detailed presentation. These options were chosen on the basis of good economics, applicability to retrofit situations, and/or the use of novel technology.

Harris, G. E.; Hearn, W. R.; Blythe, G. M.; Stuart, J. M.

1980-01-01T23:59:59.000Z

419

Winters fuels report  

SciTech Connect

The outlook for distillate fuel oil this winter is for increased demand and a return to normal inventory patterns, assuming a resumption of normal, cooler weather than last winter. With industrial production expected to grow slightly from last winter`s pace, overall consumption is projected to increase 3 percent from last winter, to 3.4 million barrels per day during the heating season (October 1, 1995-March 31, 1996). Much of the supply win come from stock drawdowns and refinery production. Estimates for the winter are from the Energy Information Administration`s (EIA) 4th Quarter 1995 Short-Tenn Energy Outlook (STEO) Mid-World Oil Price Case forecast. Inventories in place on September 30, 1995, of 132 million barrels were 9 percent below the unusually high year-earlier level. Inventories of high-sulfur distillate fuel oil, the principal type used for heating, were 13 percent lower than a year earlier. Supply problems are not anticipated because refinery production and the ready availability of imports should be adequate to meet demand. Residential heating off prices are expected to be somewhat higher than last winter`s, as the effects of lower crude oil prices are offset by lower distillate inventories. Heating oil is forecast to average $0.92 per gallon, the highest price since the winter of 1992-93. Diesel fuel (including tax) is predicted to be slightly higher than last year at $1.13 per gallon. This article focuses on the winter assessment for distillate fuel oil, how well last year`s STEO winter outlook compared to actual events, and expectations for the coming winter. Additional analyses include regional low-sulfur and high-sulfur distillate supply, demand, and prices, and recent trends in distillate fuel oil inventories.

1995-10-27T23:59:59.000Z

420

U.S. Distillate Stocks - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Slide 5 of 27. Distillate Stocks. This slide shows the average U.S. distillate stock pattern -- building in the summer and fall, then being drawn down through the ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Distillate in Depth – The Supply, Demand, and Price Picture  

U.S. Energy Information Administration (EIA)

Distillate in Depth – The Supply, Demand, and Price Picture John Hackworth Joanne Shore Energy Information Administration ... In Response to Price, ...

422

U.S. Distillate Inventory Outlook - Energy Information Administration  

U.S. Energy Information Administration (EIA)

U.S. Distillate Inventory Outlook. Sources: History: EIA; Projections: Short-Term Energy Outlook, January 2001.

423

U.S. Distillate Inventory Outlook - Energy Information Administration  

U.S. Energy Information Administration (EIA)

U.S. Distillate Inventory Outlook. Sources: History: EIA; Projections: Short-Term Energy Outlook, December 2000

424

Distilling one-qubit magic states into Toffoli states  

E-Print Network (OSTI)

For certain quantum architectures and algorithms, most of the required resources are consumed during the distillation of one-qubit magic states for use in performing Toffoli gates. I show that the overhead for magic-state distillation can be reduced by merging distillation with the implementation of Toffoli gates. The resulting routine distills 8 one-qubit magic states directly to a Toffoli state, which can be used without further magic to perform a Toffoli gate.

Bryan Eastin

2012-12-19T23:59:59.000Z

425

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)

426

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)

427

Interpolation of recurrence and hashing entanglement distillation protocols  

E-Print Network (OSTI)

We construct new entanglement distillation protocols by interpolating between the recurrence and hashing protocols. This leads to asymptotic two-way distillation protocols, resulting in an improvement of the distillation rate for all mixed Bell diagonal entangled states, even for the ones with very high fidelity. We also present a method how entanglement-assisted distillation protocols can be converted into non-entanglement-assisted protocols with the same yield.

Karl Gerd H. Vollbrecht; Frank Verstraete

2004-04-20T23:59:59.000Z

428

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)

429

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)

430

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)

431

Interpolation of recurrence and hashing entanglement distillation protocols  

Science Conference Proceedings (OSTI)

We construct interesting entanglement distillation protocols by interpolating between the recurrence and hashing protocols. This leads to asymptotic two-way distillation protocols, resulting in an improvement of the distillation rate for all mixed Bell diagonal entangled states, even for the ones with very high fidelity. We also present a method for how entanglement-assisted distillation protocol can be converted into nonentanglement-assisted protocols with the same yield.

Vollbrecht, Karl Gerd H.; Verstraete, Frank [Max-Planck-Institut fuer Quantenoptik, Hans-Kopfermann-Str. 1, D-85748 Garching (Germany)

2005-06-15T23:59:59.000Z

432

Multiple copy distillation and purification of phase diffused squeezed states  

E-Print Network (OSTI)

We provide a detailed theoretical analysis of multiple copy purification and distillation protocols for phase diffused squeezed states of light. The standard iterative distillation protocol is generalized to a collective purification of an arbitrary number of N copies. We also derive a semi-analytical expression for the asymptotic limit of the iterative distillation and purification protocol and discuss its properties.

Petr Marek; Jaromir Fiurasek; Boris Hage; Alexander Franzen; James DiGugliemo; Roman Schnabel

2007-08-10T23:59:59.000Z

433

Control of binary distillation column using fuzzy PI controllers  

Science Conference Proceedings (OSTI)

In this paper the automatic control of a binary distillation column is described. This control is done with fuzzy logic controllers. After a short explanation of the function and dynamic of a binary distillation column, it's operating and control strategies ... Keywords: binary distillation column, fuzzy inference system, simulation

Shahram Javadi; Jabber Hosseini

2009-08-01T23:59:59.000Z

434

Application for testing control configurations of binary distillation columns  

Science Conference Proceedings (OSTI)

The paper addresses the problem of testing various control configurations for binary distillation columns. Analyzing from plantwide control point of view the place of distillation column within the plant, the result will be the best control configuration. ... Keywords: composition control, distillation columns, dynamic simulations, plantwide control

Sanda Mihalache; Marian Popescu

2007-08-01T23:59:59.000Z

435

Distillate Fuel Oil Sales for Oil Company Use  

Gasoline and Diesel Fuel Update (EIA)

774,984 1,066,688 760,877 951,322 1,381,127 1,710,513 1984-2012 774,984 1,066,688 760,877 951,322 1,381,127 1,710,513 1984-2012 East Coast (PADD 1) 31,154 32,115 58,098 27,778 44,556 101,246 1984-2012 New England (PADD 1A) 332 26 12 2,369 1,203 892 1984-2012 Connecticut 332 26 12 2 0 3 1984-2012 Maine 0 0 0 438 238 0 1984-2012 Massachusetts 0 0 0 871 965 887 1984-2012 New Hampshire 0 0 0 997 0 2 1984-2012 Rhode Island 0 0 0 0 0 0 1984-2012 Vermont 0 0 0 60 0 0 1984-2012 Central Atlantic (PADD 1B) 14,850 12,350 27,638 13,528 24,570 67,199 1984-2012 Delaware 7,100 3,210 10,694 3 4 5 1984-2012 District of Columbia 0 0 0 0 0 0 1984-2012 Maryland 0 129 87 48 36 70 1984-2012 New Jersey 0 399 11,892 1,391 355 450 1984-2012 New York 10 960 2,281 1,225 382 205 1984-2012

436

Hawaii Adjusted Sales of Distillate Fuel Oil by End Use  

U.S. Energy Information Administration (EIA)

Railroad: 3: 5: 4: 33: 4: 4: 1984-2012: Vessel Bunkering: 126,454: 52,243: 61,814: 56,944: 89,341: 81,167: 1984-2012: On-Highway: 52,692: 56,394: ...

437

Adjusted Distillate Fuel Oil Sales for Residential Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 2,352,140: 2,431,656: 1,926,574: 1,750,150: 1,639,069: 1,570,785: 1984-2012: Delaware: ... Washington: 44,304: 38,803: ...

438

Distillate Fuel Oil Sales for Total Transportation Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 4,590,435: 4,264,384: 3,885,905: 4,061,266: 4,192,950: 4,177,091: 1984-2012: Delaware: 68,290: ... Washington: 877,916: ...

439

Distillate Fuel Oil Sales for Electric Power Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 132,685: 103,962: 118,357: 94,785: 78,650: 53,968: 1984-2012: Delaware: 2,166: 2,715: 7,619: ... Washington: 817: 6,427: ...

440

Alaska Adjusted Sales of Distillate Fuel Oil by End Use  

U.S. Energy Information Administration (EIA)

Railroad: 6,256: 5,439: 5,100: 4,822: 5,799: 5,211: 1984-2012: Vessel Bunkering: 124,379: 106,165: 90,025: 102,827: 119,825: 128,012: 1984-2012: ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Georgia Sales of Distillate Fuel Oil by End Use  

U.S. Energy Information Administration (EIA)

Railroad: 78,927: 69,710: 62,072: 63,770: 71,374: 63,902: 1984-2012: Vessel Bunkering: 14,016: 10,831: 10,765: 12,904: 12,387: 11,300: 1984-2012: ...

442

Distillate Fuel Oil Sales for Off-Highway Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 226,685: 252,027: 186,785: 187,163: 213,795: 208,407: 1984-2012: Delaware: 3,149: 3,210: ... Washington: 81,488: 83,550: ...

443

Adjusted Distillate Fuel Oil Sales for Farm Use  

U.S. Energy Information Administration (EIA)

Central Atlantic (PADD 1B) 98,751: 101,175: 100,179: 99,005: 110,851: 95,950: 1984-2012: Delaware: 5,647: 4,048: 6,235: ... Washington: 58,256: ...

444

North Dakota Sales of Distillate Fuel Oil by End Use  

U.S. Energy Information Administration (EIA)

Railroad: 124,832: 58,667: 12,849: 8,983: 9,839: 43,907: 1984-2012: Vessel Bunkering: 0: 0: 0: 0: 0: 0: 1984-2012: On-Highway: 177,467: 193,615: ...

445

Product Supplied for Distillate Fuel Oil, Greater than 500 ppm ...  

U.S. Energy Information Administration (EIA)

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

446

Refinery & Blender Net Production of Distillate Fuel Oil  

U.S. Energy Information Administration (EIA)

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

447

East Coast (PADD 1) Product Supplied of Distillate Fuel Oil ...  

U.S. Energy Information Administration (EIA)

456: 302: 387: 408: 475: 588: 487: 820: 2006: 712: 977: 806: 474: 442: 286: 440: 364: 436: 504: 533: 728: 2007: 860: 1,059: 779: 565: 422: 319: 277: 347: 416: 294 ...

448

Distillate Fuel Oil Sales for Off-Highway Use  

Annual Energy Outlook 2012 (EIA)

1A) 92,754 113,790 81,453 102,263 102,751 75,212 1984-2012 Connecticut 21,159 19,948 14,456 16,124 16,435 10,683 1984-2012 Maine 12,193 15,262 14,483 15,495 16,622 18,373...

449

Gulf Coast (PADD 3) Product Supplied of Distillate Fuel Oil ...  

U.S. Energy Information Administration (EIA)

456: 404: 556: 527: 489: 553: 553: 486: 518: 590: 442: 510: 1988: 497: 488: 515: 538: 592: 530: 554: 486: 445: 547: 504: 516: 1989: 457: 438: 544: 485: 556: 585: 504 ...

450

U.S. Product Supplied of Distillate Fuel Oil (Thousand ...  

U.S. Energy Information Administration (EIA)

1954: 74,697: 52,729: 54,051: 38,105: 28,895: 27,217: 26,864: 29,203: 32,593: 34,893: 51,279: 75,843: 1955: 73,778: 68,525: 58,259: 36,973: 31,762: ...

451

U.S. Exports of Distillate Fuel Oil (Thousand Barrels)  

U.S. Energy Information Administration (EIA)

1954: 1,780: 1,468: 1,652: 2,114: 2,176: 2,430: 2,018: 1,546: 1,646: 2,342: 2,911: 2,118: 1955: 1,993: 1,051: 1,761: 1,632: 2,319: 2,469: 2,379: ...

452

U.S. Product Supplied of Distillate Fuel Oil (Thousand ...  

U.S. Energy Information Administration (EIA)

1954: 2,410: 1,883: 1,744: 1,270: 932: 907: 867: 942: 1,086: 1,126: 1,709: 2,447: 1955: 2,380: 2,447: 1,879: 1,232: 1,025: 998: 915: 1,088: 1,244: ...

453

Distillate Fuel Oil Sales for All Other Uses  

Gasoline and Diesel Fuel Update (EIA)

0 0 0 0 0 0 1984-2012 0 0 0 0 0 0 1984-2012 East Coast (PADD 1) 0 0 0 0 0 0 1984-2012 New England (PADD 1A) 0 0 0 0 0 0 1984-2012 Connecticut 0 0 0 0 0 0 1984-2012 Maine 0 0 0 0 0 0 1984-2012 Massachusetts 0 0 0 0 0 0 1984-2012 New Hampshire 0 0 0 0 0 0 1984-2012 Rhode Island 0 0 0 0 0 0 1984-2012 Vermont 0 0 0 0 0 0 1984-2012 Central Atlantic (PADD 1B) 0 0 0 0 0 0 1984-2012 Delaware 0 0 0 0 0 0 1984-2012 District of Columbia 0 0 0 0 0 0 1984-2012 Maryland 0 0 0 0 0 0 1984-2012 New Jersey 0 0 0 0 0 0 1984-2012 New York 0 0 0 0 0 0 1984-2012 Pennsylvania 0 0 0 0 0 0 1984-2012 Lower Atlantic (PADD 1C) 0 0 0 0 0 0 1984-2012 Florida 0 0 0 0 0 0 1984-2012 Georgia 0 0 0 0 0 0 1984-2012 North Carolina

454

Distillate Fuel Oil Sales for Vessel Bunkering Use  

Gasoline and Diesel Fuel Update (EIA)

1,923,981 1,983,422 1,912,984 2,002,834 2,133,395 1,768,324 1,923,981 1,983,422 1,912,984 2,002,834 2,133,395 1,768,324 1984-2012 East Coast (PADD 1) 466,132 461,533 276,013 259,319 296,947 283,254 1984-2012 New England (PADD 1A) 43,014 69,102 45,147 30,589 32,414 38,891 1984-2012 Connecticut 6,654 5,683 3,914 1,898 1,502 2,838 1984-2012 Maine 8,298 6,815 15,611 4,207 4,128 13,349 1984-2012 Massachusetts 21,336 48,094 19,193 17,529 17,132 13,612 1984-2012 New Hampshire 2,740 2,552 2,327 1,110 1,395 1,815 1984-2012 Rhode Island 3,987 5,958 4,101 5,824 8,257 7,243 1984-2012 Vermont 0 0 0 21 0 35 1984-2012 Central Atlantic (PADD 1B) 147,629 129,789 104,487 67,726 76,446 74,154 1984-2012 Delaware 615 919 582 485 1,658 615 1984-2012 District of Columbia 11 7 5 13 15 17 1984-2012

455

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 ...

456

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 ...

457

U.S. Distillate Fuel Oil Imports - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Singapore : 2 : 1999-2013: Spain : 2001-2011: Sweden : 2000-2012: Syria : 2006-2009: Taiwan : 2001-2011: Trinidad and Tobago : 1993-2012: Tunisia : 2001-2001:

458

U.S. Distillate Fuel Oil Imports - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Singapore : 48 : 1999-2013: Spain : 2001-2011: Sweden : 2000-2012: Syria : 2006-2009: Taiwan : 2001-2011: Trinidad and Tobago : 1993-2012: Tunisia : 2001-2001:

459

Distillate Fuel Oil, Greater than 500 ppm Sulfur Imports from ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

460

U.S. Distillate Fuel Oil Imports - Energy Information Administration  

U.S. Energy Information Administration (EIA)

Singapore: 139 : 1999-2007: Spain: 183: 350 : 95 : 2001-2011: Sweden: 869: 24: 64 : 2: 2000-2012: Syria: 389: 303: 121 : 2006-2009: Taiwan : 699 : 710: 32 : 2001-2011 ...

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Distillate Fuel Oil, Greater than 2000 ppm Sulfur Imports from ...  

U.S. Energy Information Administration (EIA)

... Iran, Iraq, Kuwait, Qatar, Saudi Arabia, and United Arab Emirates. Totals may not equal sum of components due to independent rounding.

462

Distillate Fuel Oil, Greater than 500 ppm Sulfur Imports from ...  

U.S. Energy Information Administration (EIA)

... Iran, Iraq, Kuwait, Qatar, Saudi Arabia, and United Arab Emirates. Totals may not equal sum of components due to independent rounding.

463

Imports of Distillate Fuel Oil - 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: RBOB with Ether and RBOB ...

464

Stocks of Distillate Fuel Oil - 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: Retail prices and Prime ...

465

Stocks of Distillate Fuel Oil 15 ppm Sulfur and Under  

U.S. Energy Information Administration (EIA)

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

466

Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils...  

Gasoline and Diesel Fuel Update (EIA)

- 2,146.5 June ... 5.4 - 330.3 W W 1,905.5 2,235.7 - 2,241.1 July ... 3.6 - 319.3 1,516.8 237.5 1,754.3 2,073.6 -...

467

Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils...  

Gasoline and Diesel Fuel Update (EIA)

July ... W W 332.2 832.2 62.7 895.0 1,227.2 W 1,241.1 August ... 13.8 W 374.0 849.3 65.3 914.6 1,288.6 W...

468

Stocks of Distillate Fuel Oil 15 ppm Sulfur and Under  

U.S. Energy Information Administration (EIA)

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

469

Stocks of Distillate Fuel Oil - 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: Stocks include those ...

470

Refiner and Blender Net Production of Distillate Fuel Oil > 500...  

Gasoline and Diesel Fuel Update (EIA)

Weekly 4-Week Average Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area 101813 102513...

471

Distillate Fuel Oil, Greater than 500 ppm Sulfur Exports  

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 exports are ...

472

Distillate Fuel Oil, 15 ppm and under Sulfur Exports  

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 exports are ...

473

Midwest Gasoline and Distillate Fuel Near-Term Outlook  

Reports and Publications (EIA)

The Energy Information Administration (EIA) reviewed the potential Midwest petroleum supply-demand balance and its implications for price behavior in the fourth quarter of 2001.

Information Center

2001-10-05T23:59:59.000Z

474

"Table A2. Total Consumption of LPG, Distillate Fuel Oil,...  

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

,32,1688,378,0,58,0,15.7 3274," Lime","Q",657,"W","Q",657,"W",0,0,0,33.9 3296," Mineral Wool","W","W","W",113,34,"W","W","W",0,2 33,"Primary Metal Industries","W",5117,"W",2433,494...

475

Distillate Fuel Oil Imports from Brazil - U.S. Energy ...  

U.S. Energy Information Administration (EIA)

-No Data Reported; --= Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Notes: *Countries listed under ...

476

Distillate Fuel Oil, Greater than 500 ppm Sulfur  

U.S. Energy Information Administration (EIA)

Working Storage Capacity at Operable Refineries ... Working storage capacity is the difference in volume between the maximum safe fill capacity and ta ...

477

Midwest (PADD 2) Product Supplied of Distillate Fuel Oil (Thousand ...  

U.S. Energy Information Administration (EIA)

930: 1,014: 1,003: 1,061: 1,018: 1,005: 972: 1,018: 1,009: 1,199: 1,048: 941: 1997: 1,019: 946: 1,019: 1,082: 1,086: 1,052: 1,098: 1,018: 1,119: 1,224: 1,023: 1,077 ...

478

Contact structure for use in catalytic distillation  

DOE Patents (OSTI)

A method and apparatus for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

Jones, Jr., Edward M. (Friendswood, TX)

1985-01-01T23:59:59.000Z

479

Contact structure for use in catalytic distillation  

DOE Patents (OSTI)

A method is described for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor, contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

Jones, E.M. Jr.

1984-03-27T23:59:59.000Z

480

Contact structure for use in catalytic distillation  

DOE Patents (OSTI)

A method for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catatlyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

Jones, Jr., Edward M. (Friendswood, TX)

1984-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "fuel kerosene distillate" 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

Contact structure for use in catalytic distillation  

DOE Patents (OSTI)

A method and apparatus are disclosed for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

Jones, E.M. Jr.

1985-08-20T23:59:59.000Z

482

Iterative entanglement distillation for finite resources  

E-Print Network (OSTI)

We discuss a specific entanglement distillation scheme under the constraint of finite samples of entangled qubit pairs. It is shown that an iterative process can be explicitly formulated. The average fidelity of this process can be enhanced by introducing conditional storing of entangled qubit pairs in each step of the iteration. We investigate the corresponding limitations on the size and the initial fidelity of the sample.

Stefan Probst-Schendzielorz; Thorsten Bschorr; Matthias Freyberger

2005-06-20T23:59:59.000Z

483

Distillation of vacuum entanglement to EPR pairs  

E-Print Network (OSTI)

It is shown that by means of local interactions between a quantized relativistic field and a pair of non-entangled atoms, entanglement can be extracted from the vacuum and delivered to the atoms. The resulting mixed state of the atoms can be further distilled to EPR pairs. Therefore, in principle, teleportation and other entanglement assisted quantum communication tasks can rely on the vacuum alone as a resource for entanglement.

Benni Reznik

2000-08-01T23:59:59.000Z

484

Secret key distillation from shielded two-qubit states  

Science Conference Proceedings (OSTI)

The quantum states corresponding to a secret key are characterized using the so-called private states, where the key part consisting of a secret key is shielded by the additional systems. Based on the construction, it was shown that a secret key can be distilled from bound entangled states. In this work, I consider the shielded two-qubit states in a key-distillation scenario and derive the conditions under which a secret key can be distilled using the recurrence protocol or the two-way classical distillation, advantage distillation together with one-way postprocessing. From the security conditions, it is shown that a secret key can be distilled from bound entangled states in a much wider range. In addition, I consider the case that in which white noise is added to quantum states and show that the classical distillation protocol still works despite a certain amount of noise although the recurrence protocol does not.

Bae, Joonwoo [School of Computational Sciences, Korea Institute for Advanced Study, Seoul 130-722 (Korea, Republic of)

2010-05-15T23:59:59.000Z

485

Secret key distillation from shielded two-qubit states  

E-Print Network (OSTI)

The quantum states corresponding to a secret key are characterized using the so-called private states, where the key part consisting of a secret key is shielded by the additional systems. Based on the construction, it was shown that a secret key can be distilled from bound entangled states. In this work, I consider the shielded two-qubit states in a key-distillation scenario and derive the conditions under which a secret key can be distilled using the recurrence protocol or the two-way classical distillation, advantage distillation together with one-way postprocessing. From the security conditions, it is shown that a secret key can be distilled from bound entangled states in a much wider range. In addition, I consider the case that in which white noise is added to quantum states and show that the classical distillation protocol still works despite a certain amount of noise although the recurrence protocol does not.

Joonwoo Bae

2008-03-03T23:59:59.000Z

486

The attractor mechanism as a distillation procedure  

E-Print Network (OSTI)

In a recent paper it has been shown that for double extremal static spherically symmetric BPS black hole solutions in the STU model the well-known process of moduli stabilization at the horizon can be recast in a form of a distillation procedure of a three-qubit entangled state of GHZ-type. By studying the full flow in moduli space in this paper we investigate this distillation procedure in more detail. We introduce a three-qubit state with amplitudes depending on the conserved charges the warp factor, and the moduli. We show that for the recently discovered non-BPS solutions it is possible to see how the distillation procedure unfolds itself as we approach the horizon. For the non-BPS seed solutions at the asymptotically Minkowski region we are starting with a three-qubit state having seven nonequal nonvanishing amplitudes and finally at the horizon we get a GHZ state with merely four nonvanishing ones with equal magnitudes. The magnitude of the surviving nonvanishing amplitudes is proportional to the macroscopic black hole entropy. A systematic study of such attractor states shows that their properties reflect the structure of the fake superpotential. We also demonstrate that when starting with the very special values for the moduli corresponding to flat directions the uniform structure at the horizon deteriorates due to errors generalizing the usual bit flips acting on the qubits of the attractor states.

Péter Lévay; Szilárd Szalay

2010-04-14T23:59:59.000Z

487

Absorptive Recycle of Distillation Waste Heat  

E-Print Network (OSTI)

When the heat source available to a distillation process is at a significantly higher temperature than the reboiler temperature, there is unused availability (ability to perform work) in the heat supplied to the reboiler. Similarly, if the reflux condenser operates above ambient temperature, the rejected heat also contains unused availability. By incorporating an absorption heat pump (AHP) into the distillation process, these sources of unused availability can be tapped so as to recycle (and hence, conserve) up to 50% of the required distillation energy. In contrast to compressor driven heat pumps, this savings is accomplished without need for a separate substantial input of mechanical power. A different AHP configuration is used depending on whether the excess availability is in the source heat or reject heat. In the excessive source temperature case, the higher temperature source heat is applied to the AHP, which then supplies the total reboiler requirement and recycles half the reject heat, with the remainder being rejected conventionally. In the excessive reject temperature case, all the reject heat is supplied to a reverse absorption heat pump (HAHP) which recycles half to reboiler temperature while reducing the remainder to ambient temperature.

Erickson, D. C.; Lutz, E. J., Jr.

1982-01-01T23:59:59.000Z

488

Attractor mechanism as a distillation procedure  

Science Conference Proceedings (OSTI)

In a recent paper it was shown that for double extremal static spherical symmetric BPS black hole solutions in the STU model the well-known process of moduli stabilization at the horizon can be recast in a form of a distillation procedure of a three-qubit entangled state of a Greenberger-Horne-Zeilinger type. By studying the full flow in moduli space in this paper we investigate this distillation procedure in more detail. We introduce a three-qubit state with amplitudes depending on the conserved charges, the warp factor, and the moduli. We show that for the recently discovered non-BPS solutions it is possible to see how the distillation procedure unfolds itself as we approach the horizon. For the non-BPS seed solutions at the asymptotically Minkowski region we are starting with a three-qubit state having seven nonequal nonvanishing amplitudes and finally at the horizon we get a Greenberger-Horne-Zeilinger state with merely four nonvanishing ones with equal magnitudes. The magnitude of the surviving nonvanishing amplitudes is proportional to the macroscopic black hole entropy. A systematic study of such attractor states shows that their properties reflect the structure of the fake superpotential. We also demonstrate that when starting with the very special values for the moduli corresponding to flat directions the uniform structure at the horizon deteriorates due to errors generalizing the usual bit flips acting on the qubits of the attractor states.

Levay, Peter; Szalay, Szilard [Department of Theoretical Physics, Institute of Physics, Budapest University of Technology and Economics, H-1521 Budapest (Hungary)

2010-07-15T23:59:59.000Z

489

RECS Fuel Oil Usage Form_v1 (Draft).xps  

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

fuel oil usage for this delivery address between fuel oil usage for this delivery address between September 2008 and April 2010. Delivery Number Enter the Delivery Date for each delivery 1 2 3 4 5 6 7 8 9 10 Enter the Total Dollar Amount including taxes [Exclude late fees, merchandise, repairs, and service charges] 11 12 13 14 15 16 17 18 19 20 Form EIA 457G OMB No. 1905-0092 Expires 1/31/13 2009 RECS Fuel Oil and Kerosene Usage Form Delivery Address: Account Number: $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / / Enter the Amount Delivered in Gallons XXXX Type of Fuel Sold was: 1=Fuel Oil #1 2=Fuel Oil #2 3=Kerosene 4=Other Enter the Price per Gallon $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ $ XXX.XX $ X.XX (select one) 1 2 3 4 MM/DD/YY Page 1 of 2 U.S. Energy Information Administration Independent Statistics & Analysis

490

SRC Residual fuel oils  

DOE Patents (OSTI)

Coal solids (SRC) and distillate oils are combined to afford single-phase blends of residual oils which have utility as fuel oils substitutes. The components are combined on the basis of their respective polarities, that is, on the basis of their heteroatom content, to assure complete solubilization of SRC. The resulting composition is a fuel oil blend which retains its stability and homogeneity over the long term.

Tewari, Krishna C. (Whitehall, PA); Foster, Edward P. (Macungie, PA)

1985-01-01T23:59:59.000Z

491

Crude oil steam distillation in steam flooding. Final report  

SciTech Connect

Steam distillation yields of sixteen crude oils from various parts of the United States have been determined at a saturated steam pressure of 200 psig. Study made to investigate the effect of steam pressure (200 to 500 psig) on steam distillation yields indicates that the maximum yields of a crude oil may be obtained at 200 psig. At a steam distillation correlation factor (V/sub w//V/sub oi/) of 15, the determined steam distillation yields range from 12 to 56% of initial oil volume for the sixteen crude oils with gravity ranging from 12 to 40/sup 0/API. Regression analysis of experimental steam distillation yields shows that the boiling temperature (simulated distillation temperature) at 20% simulated distillation yield can predict the steam distillation yields reasonably well: the standard error ranges from 2.8 to 3.5% (in yield) for V/sub w//V/sub oi/ < 5 and from 3.5 to 4.5% for V/sub w//V/sub oi/ > 5. The oil viscosity (cs) at 100/sup 0/F can predict the steam distillation yields with standard error from 3.1 to 4.3%. The API gravity can predict the steam distillation yields with standard error from 4.4 to 5.7%. Characterization factor is an unsatisfactory correlation independent variable for correlation purpose.

Wu, C.H.; Elder, R.B.

1980-08-01T23:59:59.000Z

492

Apparatus for distilling shale oil from oil shale  

Science Conference Proceedings (OSTI)

An apparatus for distilling shale oil from oil shale comprises: a vertical type distilling furnace which is divided by two vertical partitions each provided with a plurality of vent apertures into an oil shale treating chamber and two gas chambers, said oil shale treating chamber being located between said two gas chambers in said vertical type distilling furnace, said vertical type distilling furnace being further divided by at least one horizontal partition into an oil shale distilling chamber in the lower part thereof and at least one oil shale preheating chamber in the upper part thereof, said oil shale distilling chamber and said oil shale preheating chamber communication with each other through a gap provided at an end of said horizontal partition, an oil shale supplied continuously from an oil shale supply port provided in said oil shale treating chamber at the top thereof into said oil shale treating chamber continuously moving from the oil shale preheating chamber to the oil shale distilling chamber, a high-temperature gas blown into an oil shale distilling chamber passing horizontally through said oil shale in said oil shale treating chamber, thereby said oil shale is preheated in said oil shale preheating chamber, and a gaseous shale oil is distilled from said preheated oil shale in said oil shale distilling chamber; and a separator for separating by liquefaction a gaseous shale oil from a gas containing the gaseous shale oil discharged from the oil shale preheating chamber.

Shishido, T.; Sato, Y.

1984-02-14T23:59:59.000Z

493

Comparison of Selected EIA-782 Data With Other Data Sources  

Reports and Publications (EIA)

This article compares annual average prices reported from the EIA-782 survey series for residential No. 2 distillate, on-highway diesel fuel, retail regular motor gasoline, refiner No. 2 fuel oil for resale, refiner No. 2 diesel fuel for resale, refiner regular motor gasoline for resale, and refiner kerosene-type jet fuel for resale with annual average prices reported by other sources. In terms of volume, it compares EIA-782C Prime Supplier annual volumes for motor gasoline (all grades), distillate fuel oil, kerosene-type jet fuel and residual fuel oil with annual volumes from other sources.

Carol Joyce Blumberg

2012-12-12T23:59:59.000Z

494

Retail Diesel Fuel Oil Prices  

Gasoline and Diesel Fuel Update (EIA)

Along with heating oil prices, the distillate supply squeeze has Along with heating oil prices, the distillate supply squeeze has severely impacted diesel fuel prices, especially in the Northeast. Diesel fuel is bascially the same product as home heating oil. The primary difference is that diesel has a lower sulfur content. When heating oil is in short supply, low sulfur diesel fuel can be diverted to heating oil supply. Thus, diesel fuel prices rise with heating heating oil prices. Retail diesel fuel prices nationally, along with those of most other petroleum prices, increased steadily through most of 1999. But prices in the Northeast jumped dramatically in the third week of January. Diesel fuel prices in New England rose nearly 68 cents per gallon, or 47 percent, between January 17 and February 7. While EIA does not have

495

Methods of producing transportation fuel  

DOE Patents (OSTI)

Systems, methods, and heaters for treating a subsurface formation are described herein. At least one method for producing transportation fuel is described herein. The method for producing transportation fuel may include providing formation fluid having a boiling range distribution between -5.degree. C. and 350.degree. C. from a subsurface in situ heat treatment process to a subsurface treatment facility. A liquid stream may be separated from the formation fluid. The separated liquid stream may be hydrotreated and then distilled to produce a distilled stream having a boiling range distribution between 150.degree. C. and 350.degree. C. The distilled liquid stream may be combined with one or more additives to produce transportation fuel.

Nair, Vijay (Katy, TX); Roes, Augustinus Wilhelmus Maria (Houston, TX); Cherrillo, Ralph Anthony (Houston, TX); Bauldreay, Joanna M. (Chester, GB)

2011-12-27T23:59:59.000Z

496

Unifying classical and quantum key distillation  

E-Print Network (OSTI)

Assume that two distant parties, Alice and Bob, as well as an adversary, Eve, have access to (quantum) systems prepared jointly according to a tripartite state. In addition, Alice and Bob can use local operations and authenticated public classical communication. Their goal is to establish a key which is unknown to Eve. We initiate the study of this scenario as a unification of two standard scenarios: (i) key distillation (agreement) from classical correlations and (ii) key distillation from pure tripartite quantum states. Firstly, we obtain generalisations of fundamental results related to scenarios (i) and (ii), including upper bounds on the key rate. Moreover, based on an embedding of classical distributions into quantum states, we are able to find new connections between protocols and quantities in the standard scenarios (i) and (ii). Secondly, we study specific properties of key distillation protocols. In particular, we show that every protocol that makes use of pre-shared key can be transformed into an equally efficient protocol which needs no pre-shared key. This result is of practical significance as it applies to quantum key distribution (QKD) protocols, but it also implies that the key rate cannot be locked with information on Eve's side. Finally, we exhibit an arbitrarily large separation between the key rate in the standard setting where Eve is equipped with quantum memory and the key rate in a setting where Eve is only given classical memory. This shows that assumptions on the nature of Eve's memory are important in order to determine the correct security threshold in QKD.

Matthias Christandl; Artur Ekert; Michal Horodecki; Pawel Horodecki; Jonathan Oppenheim; Renato Renner

2006-08-25T23:59:59.000Z

497

Unifying classical and quantum key distillation  

E-Print Network (OSTI)

Assume that two distant parties, Alice and Bob, as well as an adversary, Eve, have access to (quantum) systems prepared jointly according to a tripartite state ?ABE. In addition, Alice and Bob can use local operations and authenticated public classical communication. Their goal is to establish a key which is unknown to Eve. We initiate the study of this scenario as a unification of two standard scenarios: (i) key distillation (agreement) from classical correlations and (ii) key distillation from pure tripartite quantum states. Firstly, we obtain generalisations of fundamental results related to scenarios (i) and (ii), including upper bounds on the key rate, i.e., the number of key bits that can be extracted per copy of ?ABE. Moreover, based on an embedding of classical distributions into quantum states, we are able to find new connections between protocols and quantities in the standard scenarios (i) and (ii). Secondly, we study specific properties of key distillation protocols. In particular, we show that every protocol that makes use of pre-shared key can be transformed into an equally efficient protocol which needs no pre-shared key. This result is of practical significance as it applies to quantum key distribution (QKD) protocols, but it also implies that the key rate cannot be locked with information on Eve’s side. Finally, we exhibit an arbitrarily large separation between the key rate in the standard setting where Eve is equipped with quantum memory and the key rate in a setting where Eve is only given classical memory. This shows that assumptions on the nature of Eve’s memory are important in order to determine the correct security threshold in QKD. 1

Matthias Christ; Renato Renner

2008-01-01T23:59:59.000Z

498

Heat Exchanger Technologies for Distillation Columns  

E-Print Network (OSTI)

In this paper we look at the challenges that improvements in energy efficiency of distillation systems presents the heat exchanger designer. We examine each type of exchanger in turn. Heat exchanger size is minimized if the temperature driving force is maximized. The design should therefore seek to minimize the temperature changes during phase change. So, streams that are being condensed are kept as hot as possible. Streams that are being vaporized are kept as cool as possible. With one noted exception, this also leads to maximization of the thermodynamic efficiency and maximizes the scope for use of these streams in integrated systems.

Polley, G. T.

2002-04-01T23:59:59.000Z

499

Distillation by repeated measurements: Continuous spectrum case  

Science Conference Proceedings (OSTI)

Repeated measurements on one part of a bipartite system strongly affect the other part that is not measured, the dynamics of which is regulated by an effective contracted evolution operator. When the spectrum of this operator is discrete, the nonmeasured system is driven into a pure state, irrespective of the initial state, provided that the spectrum satisfies certain conditions. We show here that, even in the case of continuous spectrum, an effective distillation can occur under rather general conditions. We confirm it by applying our formalism to a simple model.

Bellomo, Bruno; Compagno, Giuseppe [CNISM and Dipartimento di Scienze Fisiche ed Astronomiche, Universita di Palermo, via Archirafi 36, IT-90123 Palermo (Italy); Nakazato, Hiromichi [Department of Physics, Waseda University, Tokyo 169-8555 (Japan); Yuasa, Kazuya [Waseda Institute for Advanced Study, Waseda University, Tokyo 169-8050 (Japan)

2010-12-15T23:59:59.000Z

500

Surface code implementation of block code state distillation  

E-Print Network (OSTI)

State distillation is the process of taking a number of imperfect copies of a particular quantum state and producing fewer better copies. Until recently, the lowest overhead method of distilling states |A>=(|0>+e^{i\\pi/4}|1>)/\\sqrt{2} produced a single improved |A> state given 15 input copies. New block code state distillation methods can produce k improved |A> states given 3k+8 input copies, potentially significantly reducing the overhead associated with state distillation. We construct an explicit surface code implementation of block code state distillation and quantitatively compare the overhead of this approach to the old. We find that, using the best available techniques, for parameters of practical interest, block code state distillation does not always lead to lower overhead, and, when it does, the overhead reduction is typically less than a factor of three.

Austin G. Fowler; Simon J. Devitt; Cody Jones

2013-01-29T23:59:59.000Z