National Library of Energy BETA

Sample records for liquor working gas

  1. System for removing solids from a used lime or limestone slurry scrubbing liquor in flue gas desulfurization

    SciTech Connect (OSTI)

    Randolph, A.D.

    1981-10-13

    The flue gas desulfurization process using a lime or limestone slurry scrubbing solution produces used liquor containing calcium sulfite or sulfate (Typically gypsum). Precipitated particles are removed by feeding the used scrubbing liquor to an agitated crystallization zone to grow crystals and directing part of the used scrubbing liquor from that zone to a quiescent crystallization zone, in which particles are settled back into the agitated zone. An underflow stream from the agitated zone containing large crystals is combined with an overflow stream from the quiescent zone, which combined stream is clarified with the fines being returned to the scrubber and the large crystals being removed as a waste product. Apparatus for performing the above process in which the agitated and quiescent crystallization zones form part of a single crystallization vessel, and the two zones are separated by a baffle.

  2. Gasification of black liquor

    DOE Patents [OSTI]

    Kohl, Arthur L.

    1987-07-28

    A concentrated aqueous black liquor containing carbonaceous material and alkali metal sulfur compounds is treated in a gasifier vessel containing a relatively shallow molten salt pool at its bottom to form a combustible gas and a sulfide-rich melt. The gasifier vessel, which is preferably pressurized, has a black liquor drying zone at its upper part, a black liquor solids gasification zone located below the drying zone, and a molten salt sulfur reduction zone which comprises the molten salt pool. A first portion of an oxygen-containing gas is introduced into the gas space in the gasification zone immediatley above the molten salt pool. The remainder of the oxygen-containing gas is introduced into the molten salt pool in an amount sufficient to cause gasification of carbonaceous material entering the pool from the gasification zone but not sufficient to create oxidizing conditions in the pool. The total amount of the oxygen-containing gas introduced both above the pool and into the pool constitutes between 25 and 55% of the amount required for complete combustion of the black liquor feed. A combustible gas is withdrawn from an upper portion of the drying zone, and a melt in which the sulfur content is predominantly in the form of alkali metal sulfide is withdrawn from the molten salt sulfur reduction zone.

  3. Gasification of black liquor

    DOE Patents [OSTI]

    Kohl, A.L.

    1987-07-28

    A concentrated aqueous black liquor containing carbonaceous material and alkali metal sulfur compounds is treated in a gasifier vessel containing a relatively shallow molten salt pool at its bottom to form a combustible gas and a sulfide-rich melt. The gasifier vessel, which is preferably pressurized, has a black liquor drying zone at its upper part, a black liquor solids gasification zone located below the drying zone, and a molten salt sulfur reduction zone which comprises the molten salt pool. A first portion of an oxygen-containing gas is introduced into the gas space in the gasification zone immediately above the molten salt pool. The remainder of the oxygen-containing gas is introduced into the molten salt pool in an amount sufficient to cause gasification of carbonaceous material entering the pool from the gasification zone but not sufficient to create oxidizing conditions in the pool. The total amount of the oxygen-containing gas introduced both above the pool and into the pool constitutes between 25 and 55% of the amount required for complete combustion of the black liquor feed. A combustible gas is withdrawn from an upper portion of the drying zone, and a melt in which the sulfur content is predominantly in the form of alkali metal sulfide is withdrawn from the molten salt sulfur reduction zone. 2 figs.

  4. Working Gas in Underground Storage Figure

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

    Working Gas in Underground Storage Figure Working Gas in Underground Storage Figure Working Gas in Underground Storage Compared with 5-Year Range Graph....

  5. Virginia Natural Gas in Underground Storage (Working Gas) (Million...

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

    Working Gas) (Million Cubic Feet) Virginia Natural Gas in Underground Storage (Working ... Underground Working Natural Gas in Storage - All Operators Virginia Underground Natural ...

  6. New Mexico Natural Gas in Underground Storage (Working Gas) ...

    Gasoline and Diesel Fuel Update (EIA)

    Working Gas) (Million Cubic Feet) New Mexico Natural Gas in Underground Storage (Working ... Underground Working Natural Gas in Storage - All Operators New Mexico Underground Natural ...

  7. New York Natural Gas in Underground Storage (Working Gas) (Million...

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

    Working Gas) (Million Cubic Feet) New York Natural Gas in Underground Storage (Working ... Underground Working Natural Gas in Storage - All Operators New York Underground Natural ...

  8. Working Gas in Underground Storage Figure

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

    Gas in Underground Storage Figure Working Gas in Underground Storage Compared with 5-Year Range Graph...

  9. Peak Underground Working Natural Gas Storage Capacity

    Gasoline and Diesel Fuel Update (EIA)

    of capacity that may understate the amount that can actually be stored. Working Gas Design Capacity: This measure estimates a natural gas facility's working gas capacity, as...

  10. Black liquor gasification phase 2D final report

    SciTech Connect (OSTI)

    Kohl, A.L.; Stewart, A.E.

    1988-06-01

    This report covers work conducted by Rockwell International under Amendment 5 to Subcontract STR/DOE-12 of Cooperative Agreement DE-AC-05-80CS40341 between St. Regis Corporation (now Champion International) and the Department of Energy (DOE). The work has been designated Phase 2D of the overall program to differentiate it from prior work under the same subcontract. The overall program is aimed at demonstrating the feasibility of and providing design data for the Rockwell process for gasifying Kraft black liquor. In this process, concentrated black liquor is converted into low-Btu fuel gas and reduced melt by reaction with air in a specially designed gasification reactor.

  11. California Working Natural Gas Underground Storage Capacity ...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) California Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  12. Washington Working Natural Gas Underground Storage Capacity ...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Washington Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  13. Mississippi Working Natural Gas Underground Storage Capacity...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Mississippi Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  14. Pennsylvania Working Natural Gas Underground Storage Capacity...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Pennsylvania Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May...

  15. Equipment Design and Cost Estimation for Small Modular Biomass Systems, Synthesis Gas Cleanup, and Oxygen Separation Equipment; Task 2: Gas Cleanup Design and Cost Estimates -- Black Liquor Gasification

    SciTech Connect (OSTI)

    Nexant Inc.

    2006-05-01

    As part of Task 2, Gas Cleanup and Cost Estimates, Nexant investigated the appropriate process scheme for removal of acid gases from black liquor-derived syngas for use in both power and liquid fuels synthesis. Two 3,200 metric tonne per day gasification schemes, both low-temperature/low-pressure (1100 deg F, 40 psi) and high-temperature/high-pressure (1800 deg F, 500 psi) were used for syngas production. Initial syngas conditions from each of the gasifiers was provided to the team by the National Renewable Energy Laboratory and Princeton University. Nexant was the prime contractor and principal investigator during this task; technical assistance was provided by both GTI and Emery Energy.

  16. Oregon Natural Gas in Underground Storage (Working Gas) (Million...

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

    Working Gas) (Million Cubic Feet) Oregon Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 3,705 2,366 ...

  17. Pennsylvania Natural Gas in Underground Storage (Working Gas...

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

    Working Gas) (Million Cubic Feet) Pennsylvania Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 ...

  18. Oklahoma Natural Gas in Underground Storage (Working Gas) (Million...

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

    Working Gas) (Million Cubic Feet) Oklahoma Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 129,245 ...

  19. Philadelphia Gas Works - Commercial and Industrial Equipment...

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

    Administrator Philadelphia Gas Works Website http:www.pgwenergysense.comdownloads.html State Pennsylvania Program Type Rebate Program Rebate Amount Commercial Boilers: 800 -...

  20. Peak Underground Working Natural Gas Storage Capacity

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

    Capacity Peak Underground Working Natural Gas Storage Capacity Released: September 3, 2010 for data as of April 2010 Next Release: August 2011 References Methodology Definitions...

  1. Peak Underground Working Natural Gas Storage Capacity

    Gasoline and Diesel Fuel Update (EIA)

    Previous Articles Previous Articles Estimates of Peak Underground Working Gas Storage Capacity in the United States, 2009 Update (Released, 8312009) Estimates of Peak Underground...

  2. East Region Natural Gas in Underground Storage (Working Gas)...

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

    East Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 451,335 271,801 167,715 213,475 349,739 ...

  3. How Gas Turbine Power Plants Work | Department of Energy

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

    How Gas Turbine Power Plants Work How Gas Turbine Power Plants Work The combustion (gas) turbines being installed in many of today's natural-gas-fueled power plants are complex ...

  4. West Virginia Working Natural Gas Underground Storage Capacity...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) West Virginia Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May...

  5. Montana Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Montana Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  6. Indiana Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Indiana Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  7. Oregon Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Oregon Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  8. Arkansas Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Arkansas Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  9. Alaska Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Alaska Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  10. Oklahoma Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Oklahoma Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  11. Nebraska Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Nebraska Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  12. Michigan Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Michigan Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  13. Minnesota Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Minnesota Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  14. Utah Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Utah Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  15. Missouri Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Missouri Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  16. Virginia Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Virginia Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  17. Maryland Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Maryland Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  18. Wyoming Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Wyoming Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  19. Ohio Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Ohio Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  20. Illinois Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Illinois Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  1. Iowa Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Iowa Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  2. Kentucky Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Kentucky Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  3. Texas Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Texas Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  4. Louisiana Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Louisiana Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  5. Alabama Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Alabama Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  6. New York Working Natural Gas Underground Storage Capacity (Million...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) New York Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  7. Kansas Working Natural Gas Underground Storage Capacity (Million...

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

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Kansas Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul...

  8. New Mexico Working Natural Gas Underground Storage Capacity ...

    Gasoline and Diesel Fuel Update (EIA)

    Working Natural Gas Underground Storage Capacity (Million Cubic Feet) New Mexico Working Natural Gas Underground Storage Capacity (Million Cubic Feet) Year Jan Feb Mar Apr May Jun...

  9. Louisiana Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Louisiana Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 115,418 117,492 109,383 110,052 117,110 131,282 145,105 158,865 173,570 188,751 197,819 190,747 1991 141,417 109,568 96,781 103,300 122,648 146,143 159,533 169,329 190,953 211,395 197,661 165,940 1992 120,212 91,394 79,753 85,867 106,675 124,940 136,861 152,715 174,544 194,414 187,236 149,775 1993 103,287 66,616

  10. Michigan Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Michigan Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 311,360 252,796 228,986 221,127 269,595 333,981 410,982 481,628 534,303 553,823 542,931 472,150 1991 348,875 285,217 262,424 287,946 315,457 372,989 431,607 478,293 498,086 539,454 481,257 405,327 1992 320,447 244,921 179,503 179,306 224,257 292,516 367,408 435,817 504,312 532,896 486,495 397,280 1993 296,403 194,201

  11. Montana Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Montana Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 184,212 180,918 178,620 181,242 179,235 181,374 183,442 187,348 185,848 181,029 1991 179,697 178,285 176,975 176,918 178,145 179,386 181,094 182,534 182,653 181,271 178,539 174,986 1992 111,256 109,433 109,017 109,150 110,146 110,859 111,885 112,651 112,225 110,868 107,520 101,919 1993 96,819 92,399 89,640 87,930

  12. West Virginia Natural Gas in Underground Storage (Working Gas) (Million

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

    Cubic Feet) Working Gas) (Million Cubic Feet) West Virginia Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 95,718 84,444 80,152 86,360 105,201 122,470 139,486 155,506 168,801 172,513 172,198 155,477 1991 102,542 81,767 79,042 86,494 101,636 117,739 132,999 142,701 151,152 154,740 143,668 121,376 1992 87,088 60,200 32,379 33,725 57,641 75,309 97,090 115,537 128,969 141,790 135,853 143,960 1993 112,049 69,593

  13. Pacific Region Natural Gas in Underground Storage (Working Gas) (Million

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

    Cubic Feet) Working Gas) (Million Cubic Feet) Pacific Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 197,953 115,235 104,941 144,268 200,453 249,196 274,725 302,752 318,020 345,640 339,201 322,520 2015 275,977 273,151 275,677 293,557 325,456 335,995 344,215 347,827 358,941 379,501 368,875 319,740 2016 276,196 262,566 265,792 286,993 305,681 315,790 - = No Data Reported; -- = Not Applicable; NA = Not

  14. Alabama Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Alabama Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1995 499 497 233 233 260 302 338 556 1,148 1,075 886 485 1996 431 364 202 356 493 971 1,164 1,553 1,891 2,008 1,879 1,119 1997 588 404 429 559 830 923 966 1,253 1,515 1,766 1,523 1,523 1998 773 585 337 582 727 1,350 1,341 1,540 1,139 1,752 1,753 1,615 1999 802 688 376 513 983 1,193 1,428 1,509 1,911 1,834 1,968 1,779 2000

  15. AGA Producing Region Natural Gas in Underground Storage (Working Gas)

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

    (Million Cubic Feet) Working Gas) (Million Cubic Feet) AGA Producing Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1994 393,598 297,240 289,617 356,360 461,202 516,155 604,504 678,168 747,928 783,414 775,741 673,670 1995 549,759 455,591 416,294 457,969 533,496 599,582 638,359 634,297 713,319 766,411 700,456 552,458 1996 369,545 263,652 195,447 224,002 279,731 339,263 391,961 474,402 578,991 638,500 562,097

  16. California Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) California Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 125,898 106,575 111,248 132,203 157,569 170,689 174,950 177,753 182,291 196,681 196,382 153,841 1991 132,323 132,935 115,982 136,883 163,570 187,887 201,443 204,342 199,994 199,692 193,096 168,789 1992 125,777 109,000 93,277 107,330 134,128 156,158 170,112 182,680 197,049 207,253 197,696 140,662 1993 106,890 87,612

  17. Illinois Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Illinois Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 234,149 182,982 149,826 145,903 177,193 210,075 239,633 275,310 309,341 328,106 329,864 292,842 1991 224,217 175,723 150,281 152,048 183,462 213,723 242,377 276,319 309,328 336,048 317,183 283,100 1992 214,872 167,256 140,681 132,922 166,585 198,351 228,870 267,309 302,100 328,395 310,252 264,393 1993 163,300 114,381

  18. Tennessee Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Tennessee Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1997 0 0 0 0 0 0 0 0 0 0 0 0 1998 459 343 283 199 199 199 333 467 579 682 786 787 1999 656 532 401 321 318 462 569 645 749 854 911 855 2000 691 515 452 389 371 371 371 371 371 420 534 619 2001 623 563 490 421 525 638 669 732 778 840 598 597 2002 647 648 650 650 625 622 609 605 602 600 512 512 2003 404 294 226 179 214 290

  19. South Central Region Natural Gas in Underground Storage (Working Gas)

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

    (Million Cubic Feet) Working Gas) (Million Cubic Feet) South Central Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 668,540 452,778 337,592 426,793 560,429 666,015 755,579 806,418 929,012 1,090,604 1,084,413 1,044,833 2015 831,268 576,019 574,918 749,668 920,727 1,002,252 1,050,004 1,095,812 1,206,329 1,321,297 1,332,421 1,303,737 2016 1,097,870 1,022,966 1,080,000 1,159,089 1,236,456 1,235,649 - = No

  20. Mountain Region Natural Gas in Underground Storage (Working Gas...

    Gasoline and Diesel Fuel Update (EIA)

    Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 137,378 102,507 83,983 82,058 98,717 121,623 140,461 157,716 174,610 187,375...

  1. Maryland Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Maryland Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 4,303 1,142 2,247 2,979 5,536 6,593 8,693 11,353 13,788 15,025 12,900 11,909 1991 8,772 5,481 3,859 4,780 6,264 7,917 9,321 11,555 13,665 14,339 14,626 14,529 1992 9,672 4,736 2,075 1,178 4,484 7,172 8,993 11,380 13,446 14,695 15,205 13,098 1993 9,826 5,478 3,563 3,068 5,261 6,437 7,528 9,247 11,746 14,426 14,826

  2. Minnesota Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Minnesota Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 1,708 1,141 1,211 1,688 2,017 2,129 2,261 2,309 2,370 2,397 2,395 2,007 1991 1,551 1,313 1,207 1,362 1,619 1,931 2,222 2,214 2,307 2,273 2,191 2,134 1992 1,685 1,556 1,228 1,019 1,409 1,716 2,013 2,193 2,319 2,315 2,307 2,104 1993 1,708 1,290 872 824 1,141 1,485 1,894 2,022 2,260 2,344 2,268 1,957 1994 1,430 1,235

  3. Mississippi Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Mississippi Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 33,234 33,553 34,322 39,110 43,935 47,105 53,425 58,298 62,273 65,655 66,141 60,495 1991 43,838 39,280 39,196 45,157 48,814 50,833 52,841 54,954 60,062 64,120 56,034 50,591 1992 40,858 39,723 37,350 37,516 41,830 46,750 51,406 51,967 58,355 59,621 59,164 52,385 1993 46,427 38,859 32,754 35,256 42,524 46,737 51,884

  4. Missouri Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Missouri Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 8,081 5,796 6,047 7,156 7,151 7,146 7,140 7,421 7,927 8,148 8,157 7,869 1991 7,671 5,875 4,819 6,955 7,638 7,738 8,033 8,335 8,547 8,765 8,964 8,952 1992 7,454 6,256 5,927 7,497 7,924 8,071 8,337 8,555 8,763 8,954 8,946 8,939 1993 7,848 6,037 4,952 6,501 7,550 8,001 8,104 8,420 8,627 8,842 8,720 8,869 1994 7,602 7,073

  5. Nebraska Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Nebraska Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 55,226 54,179 53,869 54,783 56,160 57,690 56,165 56,611 57,708 58,012 57,606 54,005 1991 52,095 51,060 50,341 51,476 54,531 56,673 56,409 56,345 57,250 56,941 56,535 54,163 1992 52,576 51,568 51,525 52,136 53,768 56,396 58,446 59,656 60,842 60,541 57,948 54,512 1993 51,102 49,136 48,100 49,069 52,016 55,337 57,914

  6. Washington Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Washington Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 8,882 5,257 3,304 2,365 1,893 5,005 7,942 10,880 11,949 12,154 12,235 9,008 1991 6,557 6,453 3,509 6,342 7,864 10,580 12,718 12,657 12,652 14,112 15,152 14,694 1992 12,765 9,785 9,204 8,327 9,679 10,854 11,879 13,337 14,533 13,974 13,312 9,515 1993 6,075 2,729 3,958 4,961 9,491 10,357 12,505 13,125 15,508 13,348

  7. Wyoming Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Wyoming Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 53,604 51,563 52,120 53,225 54,581 56,980 58,990 61,428 62,487 60,867 1991 54,085 53,423 53,465 53,581 54,205 56,193 58,416 60,163 61,280 61,366 59,373 57,246 1992 30,371 28,356 27,542 27,461 27,843 28,422 29,588 29,692 30,555 29,505 27,746 23,929 1993 20,529 18,137 17,769 18,265 19,253 21,322 23,372 24,929 26,122

  8. Alaska Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Alaska Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 8,956 13,913 13,743 14,328 15,277 16,187 17,087 18,569 20,455 22,149 21,244 19,819 2014 20,043 19,668 20,566 20,447 20,705 22,252 22,508 23,254 23,820 23,714 24,272 24,997 2015 24,811 24,626 24,391 24,208 24,279 24,357 24,528 24,635 24,543 24,595 24,461 24,319 2016 24,295 24,790 25,241 26,682 28,639 29,961 - = No Data

  9. Arkansas Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Arkansas Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 8,676 8,646 8,608 8,644 8,745 9,217 9,744 10,226 10,505 10,532 10,454 10,227 1991 8,296 7,930 7,609 7,414 7,545 7,884 8,371 8,385 8,385 8,385 7,756 7,093 1992 6,440 5,922 5,569 5,501 5,499 6,009 6,861 7,525 7,959 7,883 7,656 7,166 1993 6,541 5,752 5,314 5,204 4,696 4,969 4,969 4,969 4,969 4,897 4,421 3,711 1994 2,383

  10. Colorado Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Colorado Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 27,491 22,694 17,504 13,313 17,552 23,767 28,965 33,972 35,196 34,955 34,660 1991 26,266 24,505 17,544 16,115 17,196 21,173 25,452 30,548 35,254 36,813 37,882 36,892 1992 33,082 29,651 22,962 18,793 18,448 20,445 24,593 30,858 36,770 38,897 35,804 33,066 1993 28,629 23,523 21,015 17,590 20,302 24,947 28,113 31,946

  11. Indiana Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Indiana Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 22,371 18,661 17,042 17,387 20,796 23,060 26,751 30,924 33,456 34,200 30,588 1991 24,821 19,663 16,425 15,850 17,767 18,744 22,065 26,710 31,199 37,933 35,015 30,071 1992 23,328 18,843 14,762 14,340 15,414 17,948 23,103 27,216 32,427 35,283 32,732 29,149 1993 23,702 18,626 15,991 17,160 18,050 20,109 24,565 29,110

  12. Kansas Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Kansas Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 65,683 55,509 49,604 47,540 48,128 53,233 64,817 76,933 92,574 99,253 115,704 93,290 1991 59,383 54,864 49,504 47,409 53,752 61,489 64,378 67,930 78,575 89,747 80,663 82,273 1992 76,311 63,152 53,718 48,998 51,053 53,700 57,987 69,653 79,756 82,541 73,094 61,456 1993 44,893 33,024 27,680 26,796 46,806 58,528 64,198

  13. Kentucky Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) Kentucky Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 58,567 62,011 60,735 61,687 66,432 71,791 79,578 86,584 93,785 97,094 92,657 86,693 1991 79,816 76,289 72,654 77,239 79,610 82,915 88,262 91,449 94,895 94,470 87,950 85,249 1992 84,385 83,106 78,213 76,527 75,300 76,861 80,412 82,020 86,208 96,910 95,391 92,376 1993 87,306 76,381 66,748 66,019 72,407 80,245 87,794

  14. Pennsylvania Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Pennsylvania Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -2,863 -1,902 -2,297 -1,134 -1,671 -1,997 -907 -144 629 992 2,290 1,354 1991 30,778 27,964 37,141 36,920 15,424 -18,322 -46,969 -63,245 -61,004 -48,820 -54,587 -34,458 1992 6,870 -8,479 -43,753 -43,739 -33,236 -8,601 3,190 9,732 8,583 15,815

  15. Technical Report Cellulosic Based Black Liquor Gasification and Fuels Plant Final Technical Report

    SciTech Connect (OSTI)

    Fornetti, Micheal; Freeman, Douglas

    2012-10-31

    The Cellulosic Based Black Liquor Gasification and Fuels Plant Project was developed to construct a black liquor to Methanol biorefinery in Escanaba, Michigan. The biorefinery was to be co-located at the existing pulp and paper mill, NewPage’s Escanaba Paper Mill and when in full operation would: • Generate renewable energy for Escanaba Paper Mill • Produce Methanol for transportation fuel of further refinement to Dimethyl Ether • Convert black liquor to white liquor for pulping. Black liquor is a byproduct of the pulping process and as such is generated from abundant and renewable lignocellulosic biomass. The biorefinery would serve to validate the thermochemical pathway and economic models for black liquor gasification. It was a project goal to create a compelling new business model for the pulp and paper industry, and support the nation’s goal for increasing renewable fuels production and reducing its dependence on foreign oil. NewPage Corporation planned to replicate this facility at other NewPage Corporation mills after this first demonstration scale plant was operational and had proven technical and economic feasibility. An overview of the process begins with black liquor being generated in a traditional Kraft pulping process. The black liquor would then be gasified to produce synthesis gas, sodium carbonate and hydrogen sulfide. The synthesis gas is then cleaned with hydrogen sulfide and carbon dioxide removed, and fed into a Methanol reactor where the liquid product is made. The hydrogen sulfide is converted into polysulfide for use in the Kraft pulping process. Polysulfide is a known additive to the Kraft process that increases pulp yield. The sodium carbonate salts are converted to caustic soda in a traditional recausticizing process. The caustic soda is then part of the white liquor that is used in the Kraft pulping process. Cellulosic Based Black Liquor Gasification and Fuels Plant project set out to prove that black liquor gasification could

  16. Philadelphia Gas Works: Who’s on First?

    Broader source: Energy.gov [DOE]

    Presentation—given at the Fall 2011 Federal Utility Partnership Working Group (FUPWG) meeting—about the Philadelphia Gas Works (PGW) and its federal projects.

  17. Pennsylvania Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Percent) Percent) Pennsylvania Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 18.8 22.4 37.0 33.4 9.7 -8.5 -17.7 -19.9 -17.0 -13.4 -15.2 -11.2 1992 3.5 -5.5 -31.8 -29.7 -19.1 -4.4 1.5 3.8 2.9 5.0 9.1 6.0 1993 8.3 -16.5 -29.1 -13.2 -5.0 -0.1 5.0 3.1 4.8 0.9 -1.5 -3.3 1994 -21.0 -19.2 13.5 27.9 24.0 18.3 16.9 15.8 5.8 6.1 2.3 5.6 1995 35.1 43.1 48.4 8.5

  18. ,"U.S. Natural Gas Non-Salt Underground Storage - Working Gas...

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

    Natural Gas Non-Salt Underground Storage - Working Gas (MMcf)",1,"Monthly","2...dnavnghistn5510us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, ...

  19. Black liquor combustion validated recovery boiler modeling, five-year report

    SciTech Connect (OSTI)

    Grace, T.M.; Frederick, W.J.; Salcudean, M.; Wessel, R.A.

    1996-08-01

    The objective of this project was to develop a new computer model of a recovery boiler furnace using a computational fluid dynamics (CFD) code specifically tailored to the requirements for solving recovery boiler flows, and using improved submodels for black liquor combustion based on continued laboratory fundamental studies. The project originated in October 1990 and was scheduled to run for four years. At that time, there was considerable emphasis on developing accurate predictions of the physical carryover of macroscopic particles of partially burnt black liquor and smelt droplets out of the furnace, since this was seen as the main cause of boiler plugging. This placed a major emphasis on gas flow patterns within the furnace and on the mass loss rates and swelling and shrinking rates of burning black liquor drops. As work proceeded on developing the recovery boiler furnace model, it became apparent that some recovery boilers encounter serious plugging problems even when physical carryover was minimal. After the original four-year period was completed, the project was extended to address this issue. The objective of the extended project was to improve the utility of the models by including the black liquor chemistry relevant to air emissions predictions and aerosol formation, and by developing the knowledge base and computational tools to relate furnace model outputs to fouling and plugging of the convective sections of the boilers. The work done to date includes CFD model development and validation, acquisition of information on black liquor combustion fundamentals and development of improved burning models, char bed model development, and model application and simplification.

  20. Two-tank working gas storage system for heat engine

    DOE Patents [OSTI]

    Hindes, Clyde J.

    1987-01-01

    A two-tank working gas supply and pump-down system is coupled to a hot gas engine, such as a Stirling engine. The system has a power control valve for admitting the working gas to the engine when increased power is needed, and for releasing the working gas from the engine when engine power is to be decreased. A compressor pumps the working gas that is released from the engine. Two storage vessels or tanks are provided, one for storing the working gas at a modest pressure (i.e., half maximum pressure), and another for storing the working gas at a higher pressure (i.e., about full engine pressure). Solenoid valves are associated with the gas line to each of the storage vessels, and are selectively actuated to couple the vessels one at a time to the compressor during pumpdown to fill the high-pressure vessel with working gas at high pressure and then to fill the low-pressure vessel with the gas at low pressure. When more power is needed, the solenoid valves first supply the low-pressure gas from the low-pressure vessel to the engine and then supply the high-pressure gas from the high-pressure vessel. The solenoid valves each act as a check-valve when unactuated, and as an open valve when actuated.

  1. Washington Natural Gas in Underground Storage - Change in Working...

    Gasoline and Diesel Fuel Update (EIA)

    Percent) Washington Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991...

  2. Washington Natural Gas in Underground Storage - Change in Working...

    Gasoline and Diesel Fuel Update (EIA)

    Million Cubic Feet) Washington Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug...

  3. First AEO2015 Oil and Gas Working Group Meeting Summary

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

    GAS MARKETS TEAMS SUBJECT: First AEO2015 Oil and Gas Working Group Meeting Summary ... The shorter AEO2015 will have 6 cases - Reference case, HighLow Oil Price cases, HighLow ...

  4. Philadelphia Gas Works- Residential and Commercial Construction Incentives Program

    Office of Energy Efficiency and Renewable Energy (EERE)

    Philadelphia Gas Works (PGW) provides incentives to developers, home builders and building owners that build new facilities or undergo gut-rehab projects to conserve gas beyond the level consumed...

  5. Virginia Natural Gas in Underground Storage - Change in Working...

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

    Percent) Virginia Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1997 0.0 ...

  6. New Mexico Natural Gas in Underground Storage - Change in Working...

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

    Percent) New Mexico Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 ...

  7. New Mexico Natural Gas in Underground Storage - Change in Working...

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

    Million Cubic Feet) New Mexico Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug ...

  8. Minnesota Natural Gas in Underground Storage - Change in Working...

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

    Percent) Minnesota Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -9.2 ...

  9. Minnesota Natural Gas in Underground Storage - Change in Working...

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

    Million Cubic Feet) Minnesota Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep ...

  10. Weekly Working Gas in Underground Storage

    Gasoline and Diesel Fuel Update (EIA)

    BOE Reserve Class No 2001 reserves 0.1 - 10 MBOE 10.1 - 100 MBOE 100.1 - 1,000 MBOE 1,000.1 - 10,000 MBOE 10,000.1 - 100,000 MBOE > 100,000 MBOE Appalachian Basin Boundary Appalachian Basin, Southern OH (Panel 4 of 7) Oil and Gas Fields By 2001 BOE Reserve Class Total Total Total Number Liquid Gas BOE of Reserves Reserves Reserves Basin Fields (Mbbl) (MMcf) (Mbbl) Appalachian 3354 79,141 9,550,156 1,670,834 2001 Proved Reserves for Entire Applachian Basin OH WV The mapped oil and gas field

  11. Philadelphia Gas Works- Residential and Small Business Equipment Rebate Program

    Broader source: Energy.gov [DOE]

    Philadelphia Gas Works' (PGW) Residential Heating Equipment rebates are available to all PGW residential or small business customers installing high efficiency boilers and furnaces, and programma...

  12. Federal Utility Partnership Working Group: Atlanta Gas Light Resources

    Broader source: Energy.gov [DOE]

    Presentation—given at the April 2012 Federal Utility Partnership Working Group (FUPWG) meeting—lists Altanta Gas Light (AGL) resources and features a map of its footprint.

  13. Philadelphia Navy Yard: UESC Project with Philadelphia Gas Works

    Broader source: Energy.gov [DOE]

    Presentation—given at the Fall 2011 Federal Utility Partnership Working Group (FUPWG) meeting—provides information on the Philadelphia Navy Yard's utility energy services contract (UESC) project with Philadelphia Gas Works (PGW).

  14. Philadelhia Gas Works (PGW) Doe Furnace Rule | Department of Energy

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

    Philadelhia Gas Works (PGW) Doe Furnace Rule Philadelhia Gas Works (PGW) Doe Furnace Rule DOE Furnace Rule (111.99 KB) More Documents & Publications Focus Series: Philadelphia Energyworks: In the City of Brotherly Love, Sharing Know-How Leads to Sustainability The Better Buildings Neighborhood View -- December 2013 Collaborating With Utilities on Residential Energy Efficiency

  15. Working Together to Address Natural Gas Storage Safety | Department of

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

    Energy Address Natural Gas Storage Safety Working Together to Address Natural Gas Storage Safety April 1, 2016 - 11:15am Addthis Working Together to Address Natural Gas Storage Safety Franklin (Lynn) Orr Franklin (Lynn) Orr Under Secretary for Science and Energy Marie Therese Dominguez Marie Therese Dominguez Administrator, U.S. Department of Transportation's Pipeline and Hazardous Materials Safety Administration As a part of the Administration's ongoing commitment to support state and

  16. ,"U.S. Natural Gas Salt Underground Storage - Working Gas (MMcf...

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

    1","U.S. Natural Gas Salt Underground Storage - Working Gas (MMcf)",1,"Monthly","2...dnavnghistn5410us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, ...

  17. Use of sulfide-containing liquors for removing mercury from flue gases

    SciTech Connect (OSTI)

    Nolan, Paul S.; Downs, William; Bailey, Ralph T.; Vecci, Stanley J.

    2003-01-01

    A method and apparatus for reducing and removing mercury in industrial gases, such as a flue gas, produced by the combustion of fossil fuels, such as coal, adds sulfide ions to the flue gas as it passes through a scrubber. Ideally, the source of these sulfide ions may include at least one of: sulfidic waste water, kraft caustic liquor, kraft carbonate liquor, potassium sulfide, sodium sulfide, and thioacetamide. The sulfide ion source is introduced into the scrubbing liquor as an aqueous sulfide species. The scrubber may be either a wet or dry scrubber for flue gas desulfurization systems.

  18. Use of sulfide-containing liquors for removing mercury from flue gases

    SciTech Connect (OSTI)

    Nolan, Paul S.; Downs, William; Bailey, Ralph T.; Vecci, Stanley J.

    2006-05-02

    A method and apparatus for reducing and removing mercury in industrial gases, such as a flue gas, produced by the combustion of fossil fuels, such as coal, adds sulfide ions to the flue gas as it passes through a scrubber. Ideally, the source of these sulfide ions may include at least one of: sulfidic waste water, kraft caustic liquor, kraft carbonate liquor, potassium sulfide, sodium sulfide, and thioacetamide. The sulfide ion source is introduced into the scrubbing liquor as an aqueous sulfide species. The scrubber may be either a wet or dry scrubber for flue gas desulfurization systems.

  19. AEO2014 Oil and Gas Working Group Meeting Summary

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

    9 August 12, 2013 MEMORANDUM FOR: JOHN CONTI ASSISTANT ADMINISTRATOR FOR ENERGY ANALYSIS FROM: ANGELINA LAROSE TEAM LEAD NATURAL GAS MARKETS TEAM JOHN STAUB TEAM LEAD EXPLORATION AND PRODUCTION ANALYSIS TEAM EXPLORATION AND PRODUCTION and NATURAL GAS MARKETS TEAMS SUBJECT: First AEO2014 Oil and Gas Working Group Meeting Summary (presented on July 25, 2013) Attendees: Anas Alhajji (NGP)* Samuel Andrus (IHS)* Emil Attanasi (USGS)* Andre Barbe (Rice University) David J. Barden (self) Joseph

  20. Second AEO2014 Oil and Gas Working Group Meeting Summary

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

    7 November 12, 2013 MEMORANDUM FOR: JOHN CONTI ASSISTANT ADMINISTRATOR FOR ENERGY ANALYSIS FROM: ANGELINA LAROSE TEAM LEAD NATURAL GAS MARKETS TEAM JOHN STAUB TEAM LEAD EXPLORATION AND PRODUCTION ANALYSIS TEAM EXPLORATION AND PRODUCTION and NATURAL GAS MARKETS TEAMS SUBJECT: Second AEO2014 Oil and Gas Working Group Meeting Summary (presented September 26, 2013) Attendees: Robert Anderson (DOE) Peter Balash (NETL)* David Bardin (self) Joe Benneche (EIA) Philip Budzik (EIA) Kara Callahan

  1. Philadelphia Gas Works- Commercial and Industrial Efficient Building Grant Program

    Broader source: Energy.gov [DOE]

    Philadelphia Gas Works' (PGW) Commercial and Industrial Efficient Building Grant Program is part of PGW's EnergySense program. This program offers incentives up to $75,000 for multifamily,...

  2. Lower 48 States Natural Gas Working Underground Storage (Billion...

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

    Underground Storage (Billion Cubic Feet) Lower 48 States Natural Gas Working Underground Storage (Billion Cubic Feet) Year-Month Week 1 Week 2 Week 3 Week 4 Week 5 End Date Value...

  3. Differences Between Monthly and Weekly Working Gas In Storage

    Weekly Natural Gas Storage Report (EIA)

    Differences Between Monthly and Weekly Working Gas In Storage Latest update: September 8, 2016 Note: The weekly storage estimates are based on a survey sample that does not include all companies that operate underground storage facilities. The sample was selected from the list of storage operators to achieve a target standard error of the estimate of working gas in storage which was no greater than 5 percent for each region. Based on a comparison of weekly estimates and monthly data from January

  4. AGA Eastern Consuming Region Natural Gas in Underground Storage (Working

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

    Gas) (Million Cubic Feet) Working Gas) (Million Cubic Feet) AGA Eastern Consuming Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1994 905,018 584,386 467,210 599,207 831,273 1,086,355 1,342,894 1,578,648 1,775,994 1,885,465 1,819,517 1,589,500 1995 1,206,116 814,626 663,885 674,424 850,290 1,085,760 1,300,439 1,487,188 1,690,456 1,811,013 1,608,177 1,232,901 1996 812,303 520,053 341,177 397,770 612,572 890,243

  5. AGA Western Consuming Region Natural Gas in Underground Storage (Working

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

    Gas) (Million Cubic Feet) Working Gas) (Million Cubic Feet) AGA Western Consuming Region Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1994 280,414 208,968 200,997 216,283 261,894 293,909 326,049 349,274 387,670 405,477 381,931 342,394 1995 288,908 270,955 251,410 246,654 284,291 328,371 362,156 372,718 398,444 418,605 419,849 366,944 1996 280,620 236,878 221,371 232,189 268,812 299,619 312,736 313,747 330,116

  6. Advancement of High Temperature Black Liquor Gasification Technology

    SciTech Connect (OSTI)

    Craig Brown; Ingvar Landalv; Ragnar Stare; Jerry Yuan; Nikolai DeMartini; Nasser Ashgriz

    2008-03-31

    Weyerhaeuser operates the world's only commercial high-temperature black liquor gasifier at its pulp mill in New Bern, NC. The unit was started-up in December 1996 and currently processes about 15% of the mill's black liquor. Weyerhaeuser, Chemrec AB (the gasifier technology developer), and the U.S. Department of Energy recognized that the long-term, continuous operation of the New Bern gasifier offered a unique opportunity to advance the state of high temperature black liquor gasification toward the commercial-scale pressurized O2-blown gasification technology needed as a foundation for the Forest Products Bio-Refinery of the future. Weyerhaeuser along with its subcontracting partners submitted a proposal in response to the 2004 joint USDOE and USDA solicitation - 'Biomass Research and Development Initiative'. The Weyerhaeuser project 'Advancement of High Temperature Black Liquor Gasification' was awarded USDOE Cooperative Agreement DE-FC26-04NT42259 in November 2004. The overall goal of the DOE sponsored project was to utilize the Chemrec{trademark} black liquor gasification facility at New Bern as a test bed for advancing the development status of molten phase black liquor gasification. In particular, project tasks were directed at improvements to process performance and reliability. The effort featured the development and validation of advanced CFD modeling tools and the application of these tools to direct burner technology modifications. The project also focused on gaining a fundamental understanding and developing practical solutions to address condensate and green liquor scaling issues, and process integration issues related to gasifier dregs and product gas scrubbing. The Project was conducted in two phases with a review point between the phases. Weyerhaeuser pulled together a team of collaborators to undertake these tasks. Chemrec AB, the technology supplier, was intimately involved in most tasks, and focused primarily on the design, specification and

  7. Method for improving separation of carbohydrates from wood pulping and wood or biomass hydrolysis liquors

    DOE Patents [OSTI]

    Griffith, William Louis; Compere, Alicia Lucille; Leitten, Jr., Carl Frederick

    2010-04-20

    A method for separating carbohydrates from pulping liquors includes the steps of providing a wood pulping or wood or biomass hydrolysis pulping liquor having lignin therein, and mixing the liquor with an acid or a gas which forms an acid upon contact with water to initiate precipitation of carbohydrate to begin formation of a precipitate. During precipitation, at least one long chain carboxylated carbohydrate and at least one cationic polymer, such as a polyamine or polyimine are added, wherein the precipitate aggregates into larger precipitate structures. Carbohydrate gel precipitates are then selectively removed from the larger precipitate structures. The method process yields both a carbohydrate precipitate and a high purity lignin.

  8. Midwest Region Natural Gas Working Underground Storage (Billion Cubic Feet)

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

    Midwest Region Natural Gas Working Underground Storage (Billion Cubic Feet) Midwest Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 900 01/08 820 01/15 750 01/22 710 01/29 661 2010-Feb 02/05 604 02/12 552 02/19 502 02/26 464 2010-Mar 03/05 433 03/12 422 03/19 419 03/26 410 2010-Apr 04/02 410 04/09 429 04/16 444 04/23 462 04/30 480 2010-May

  9. Mountain Region Natural Gas Working Underground Storage (Billion Cubic

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

    Feet) Mountain Region Natural Gas Working Underground Storage (Billion Cubic Feet) Mountain Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 195 01/08 185 01/15 176 01/22 171 01/29 164 2010-Feb 02/05 157 02/12 148 02/19 141 02/26 133 2010-Mar 03/05 129 03/12 127 03/19 126 03/26 126 2010-Apr 04/02 126 04/09 126 04/16 129 04/23 134 04/30 138

  10. Nonsalt South Central Region Natural Gas Working Underground Storage

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

    (Billion Cubic Feet) Nonsalt South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) Nonsalt South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 826 01/08 763 01/15 702 01/22 687 01/29 671 2010-Feb 02/05 624 02/12 573 02/19 521 02/26 496 2010-Mar 03/05 472 03/12 477 03/19 487 03/26 492 2010-Apr 04/02

  11. Pacific Region Natural Gas Working Underground Storage (Billion Cubic Feet)

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

    Pacific Region Natural Gas Working Underground Storage (Billion Cubic Feet) Pacific Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 268 01/08 257 01/15 246 01/22 235 01/29 221 2010-Feb 02/05 211 02/12 197 02/19 193 02/26 184 2010-Mar 03/05 182 03/12 176 03/19 179 03/26 185 2010-Apr 04/02 189 04/09 193 04/16 199 04/23 209 04/30 220 2010-May

  12. East Region Natural Gas Working Underground Storage (Billion Cubic Feet)

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

    East Region Natural Gas Working Underground Storage (Billion Cubic Feet) East Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 769 01/08 703 01/15 642 01/22 616 01/29 582 2010-Feb 02/05 523 02/12 471 02/19 425 02/26 390 2010-Mar 03/05 349 03/12 341 03/19 334 03/26 336 2010-Apr 04/02 333 04/09 358 04/16 376 04/23 397 04/30 416 2010-May 05/07

  13. Salt South Central Region Natural Gas Working Underground Storage (Billion

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

    Cubic Feet) Salt South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) Salt South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 159 01/08 123 01/15 91 01/22 102 01/29 108 2010-Feb 02/05 95 02/12 85 02/19 71 02/26 70 2010-Mar 03/05 63 03/12 71 03/19 80 03/26 89 2010-Apr 04/02 101 04/09 112 04/16 120

  14. South Central Region Natural Gas Working Underground Storage (Billion Cubic

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

    Feet) South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) South Central Region Natural Gas Working Underground Storage (Billion Cubic Feet) 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-Jan 01/01 985 01/08 886 01/15 793 01/22 789 01/29 779 2010-Feb 02/05 719 02/12 658 02/19 592 02/26 566 2010-Mar 03/05 535 03/12 548 03/19 567 03/26 581 2010-Apr 04/02 612 04/09 649 04/16 679 04/23 710

  15. Lower 48 Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Lower 48 Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 0.1 2.3 -4.6 -11.1 -9.6 -7.7 -6.4 -4.2 -2.6 -1.2 2.0 11.3 2012 36.5 53.4 73.5 61.5 46.1 34.6 25.3 19.5 15.0 11.5 7.7 8.2 2013 -7.6 -14.8 -31.0 -29.5 -21.9 -15.7 -10.0 -6.2 -4.0 -3.4 -5.7 -15.9

  16. Causticizing for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    Scott Sinquefeld; James Cantrell; Xiaoyan Zeng; Alan Ball; Jeff Empie

    2009-01-07

    The cost-benefit outlook of black liquor gasification (BLG) could be greatly improved if the smelt causticization step could be achieved in situ during the gasification step. Or, at a minimum, the increase in causticizing load associated with BLG could be mitigated. A number of chemistries have been proven successful during black liquor combustion. In this project, three in situ causticizing processes (titanate, manganate, and borate) were evaluated under conditions suitable for high temperature entrained flow BLG, and low temperature steam reforming of black liquor. The evaluation included both thermodynamic modeling and lab experimentation. Titanate and manganate were tested for complete direct causticizing (to thus eliminate the lime cycle), and borates were evaluated for partial causticizing (to mitigate the load increase associated with BLG). Criteria included high carbonate conversion, corresponding hydroxide recovery upon hydrolysis, non process element (NPE) removal, and economics. Of the six cases (three chemistries at two BLG conditions), only two were found to be industrially viable: titanates for complete causticizing during high temperature BLG, and borates for partial causticizing during high temperature BLG. These two cases were evaluated for integration into a gasification-based recovery island. The Larsen [28] BLG cost-benefit study was used as a reference case for economic forecasting (i.e. a 1500 tpd pulp mill using BLG and upgrading the lime cycle). By comparison, using the titanate direct causticizing process yielded a net present value (NPV) of $25M over the NPV of BLG with conventional lime cycle. Using the existing lime cycle plus borate autocausticizing for extra capacity yielded a NPV of $16M.

  17. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Jun Wei

    2005-03-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  18. Lower 48 States Total Natural Gas in Underground Storage (Working Gas)

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

    (Million Cubic Feet) Working Gas) (Million Cubic Feet) Lower 48 States Total Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2011 2,305,843 1,721,875 1,577,007 1,788,480 2,186,855 2,529,647 2,775,346 3,019,155 3,415,698 3,803,828 3,842,882 3,462,021 2012 2,910,007 2,448,810 2,473,130 2,611,226 2,887,060 3,115,447 3,245,201 3,406,134 3,693,053 3,929,250 3,799,215 3,412,910 2013 2,690,271 2,085,441 1,706,102 1,840,859

  19. Midwest Region Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Million Cubic Feet) - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Midwest Region Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 -243,074 -255,871 -209,941 -189,692 -156,914 -124,375 -83,035 -47,387 -33,755 -8,053 -11,988 108,104 2015 168,709 107,663 110,005 130,381 120,962 93,959 58,782 43,062 37,218 47,788

  20. Mountain Region Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Million Cubic Feet) - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Mountain Region Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 -32,861 -42,199 -45,053 -42,581 -35,771 -26,278 -21,654 -24,388 -26,437 -26,669 -34,817 -21,557 2015 -6,412 13,374 29,357 34,073 36,475 32,988 31,353 29,400 28,615 27,317 32,540 33,887

  1. U.S. Natural Gas Non-Salt Underground Storage - Working Gas (Million Cubic

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

    Feet) Working Gas (Million Cubic Feet) U.S. Natural Gas Non-Salt Underground Storage - Working Gas (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1994 1,531,928 1,053,730 915,878 1,122,203 1,495,691 1,839,607 2,209,565 2,542,126 2,841,503 3,002,400 2,904,404 2,536,416 1995 1,972,316 1,477,193 1,273,311 1,313,255 1,594,809 1,935,579 2,225,266 2,431,646 2,721,269 2,908,317 2,644,778 2,081,635 1996 1,403,589 973,002 720,077 796,966 1,098,675 1,457,649 1,826,743

  2. U.S. Total Natural Gas in Underground Storage (Working Gas) (Million Cubic

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

    Feet) Working Gas) (Million Cubic Feet) U.S. Total Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1973 NA NA NA NA NA NA NA NA NA NA NA 2,034,000 1974 NA NA NA NA NA NA NA NA NA 2,403,000 NA 2,050,000 1975 NA NA NA NA NA NA NA NA 2,468,000 2,599,000 2,541,000 2,212,000 1976 1,648,000 1,444,000 1,326,000 1,423,000 1,637,000 1,908,000 2,192,000 2,447,000 2,650,000 2,664,000 2,408,000 1,926,000 1977 1,287,000 1,163,000

  3. Pacific Region Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Million Cubic Feet) - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Pacific Region Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 -73,745 -134,228 -151,370 -126,913 -108,676 -88,833 -85,846 -63,506 -59,951 -41,003 -28,478 51,746 2015 78,024 157,916 170,736 149,288 125,002 86,799 69,490 45,075 40,921 33,861 29,674

  4. Texas Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet)

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

    Working Gas) (Million Cubic Feet) Texas Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 321,678 314,918 308,955 347,344 357,995 370,534 383,549 377,753 378,495 396,071 402,265 365,396 1991 279,362 271,469 271,401 289,226 303,895 323,545 327,350 329,102 344,201 347,984 331,821 316,648 1992 284,571 270,262 264,884 267,778 286,318 298,901 320,885 338,320 341,156 345,459 324,873 288,098 1993 165,226 149,367 141,472

  5. Ohio Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet)

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

    Working Gas) (Million Cubic Feet) Ohio Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 100,467 79,364 70,578 73,582 96,173 115,927 135,350 154,385 171,798 182,858 181,763 157,536 1991 120,038 97,180 81,448 90,583 109,886 132,661 147,602 165,801 180,656 188,600 175,740 148,929 1992 105,511 70,674 36,141 38,587 63,604 95,665 121,378 143,128 158,570 169,712 164,562 132,576 1993 93,544 49,298 14,332 16,953 43,536 75,177

  6. Recovery of sugars from ionic liquid biomass liquor by solvent...

    Office of Scientific and Technical Information (OSTI)

    Recovery of sugars from ionic liquid biomass liquor by solvent extraction Citation Details In-Document Search Title: Recovery of sugars from ionic liquid biomass liquor by solvent ...

  7. Big Island Demonstration Project - Black Liquor

    SciTech Connect (OSTI)

    2006-08-01

    Black liquor is a papermaking byproduct that also serves as a fuel for pulp and paper mills. This project involves the design, construction, and operation of a black liquor gasifier that will be integrated into Georgia-Pacific's Big Island facility in Virginia, a mill that has been in operation for more than 100 years.

  8. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Liang; Jun Wei

    2005-04-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  9. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Liang; Alireza Rezaie

    2004-10-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  10. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Liang

    2005-10-01

    The University of Missouri-Rolla identified materials that permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project was to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study attempted to define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials were selected/developed that either react with the gasifier environment to form protective surfaces in-situ; and

  11. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Liang

    2005-07-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  12. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Liang; Jun Wei

    2005-01-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  13. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    William L. Headrick Jr; Alireza Rezaie

    2003-12-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the materials problems encountered during the operation of low-pressure high-temperature (LFHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  14. REFRACTORY FOR BLACK LIQUOR GASIFIERS

    SciTech Connect (OSTI)

    William L. Headrick Jr.; Alireza Rezaie

    2003-12-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the materials problems encountered during the operation of low-pressure high-temperature (LFHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  15. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    William L. Headrick Jr; Alireza Rezaie; Xiaoting Liang; Musa Karakus; Jun Wei

    2005-12-01

    The University of Missouri-Rolla identified materials that permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project was to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study attempted to define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials were selected or developed that reacted with the gasifier environment to form protective surfaces in-situ; and

  16. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    William L. Headrick Jr; Alireza Rezaie

    2003-08-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the materials problems encountered during the operation of low-pressure high-temperature (LFHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  17. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    Robert E. Moore; William L. Headrick; Alireza Rezaie

    2003-03-31

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the materials problems encountered during the operation of low-pressure high-temperature (LFHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  18. Missouri Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Missouri Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -114 -943 -336 775 774 774 773 -107 103 55 -146 1,291 1991 -410 79 -1,227 -201 487 592 893 913 620 617 807 1,083 1992 -216 381 1,107 542 286 333 304 220 216 189 -18 -13 1993 393 -220 -975 -996 -374 -69 -233 -135 -136 -112 -226 -70 1994 -245 1,036 1,842

  19. Alabama Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Alabama Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1996 -67 -133 -30 123 233 669 826 998 743 933 994 633 1997 156 40 226 203 337 -48 -197 -301 -376 -242 -356 405 1998 185 181 -92 24 -103 427 374 288 -376 -14 230 91 1999 29 103 39 -69 257 -156 88 -31 772 82 214 164 2000 63 175 802 599 219 615 462 381 -131 -196

  20. Refractory for Black Liquor Gasifiers

    SciTech Connect (OSTI)

    William L. Headrick Jr; Musa Karakus; Xiaoting Laing

    2005-10-01

    The University of Missouri-Rolla will identify materials that will permit the safe, reliable and economical operation of combined cycle gasifiers by the pulp and paper industry. The primary emphasis of this project will be to resolve the material problems encountered during the operation of low-pressure high-temperature (LPHT) and low-pressure low-temperature (LPLT) gasifiers while simultaneously understanding the materials barriers to the successful demonstration of high-pressure high-temperature (HPHT) black liquor gasifiers. This study will define the chemical, thermal and physical conditions in current and proposed gasifier designs and then modify existing materials and develop new materials to successfully meet the formidable material challenges. Resolving the material challenges of black liquor gasification combined cycle technology will provide energy, environmental, and economic benefits that include higher thermal efficiencies, up to three times greater electrical output per unit of fuel, and lower emissions. In the near term, adoption of this technology will allow the pulp and paper industry greater capital effectiveness and flexibility, as gasifiers are added to increase mill capacity. In the long term, combined-cycle gasification will lessen the industry's environmental impact while increasing its potential for energy production, allowing the production of all the mill's heat and power needs along with surplus electricity being returned to the grid. An added benefit will be the potential elimination of the possibility of smelt-water explosions, which constitute an important safety concern wherever conventional Tomlinson recovery boilers are operated. Developing cost-effective materials with improved performance in gasifier environments may be the best answer to the material challenges presented by black liquor gasification. Refractory materials may be selected/developed that either react with the gasifier environment to form protective surfaces in

  1. Rapid gas hydrate formation processes: Will they work?

    SciTech Connect (OSTI)

    Brown, Thomas D.; Taylor, Charles E.; Bernardo, Mark P.

    2010-06-07

    Researchers at DOEs National Energy Technology Laboratory (NETL) have been investigating the formation of synthetic gas hydrates, with an emphasis on rapid and continuous hydrate formation techniques. The investigations focused on unconventional methods to reduce dissolution, induction, nucleation and crystallization times associated with natural and synthetic hydrates studies conducted in the laboratory. Numerous experiments were conducted with various high-pressure cells equipped with instrumentation to study rapid and continuous hydrate formation. The cells ranged in size from 100 mL for screening studies to proof-of-concept studies with NETLs 15-Liter Hydrate Cell. The results from this work demonstrate that the rapid and continuous formation of methane hydrate is possible at predetermined temperatures and pressures within the stability zone of a Methane Hydrate Stability Curve.

  2. Rapid gas hydrate formation processes: Will they work?

    DOE Public Access Gateway for Energy & Science Beta (PAGES Beta)

    Brown, Thomas D.; Taylor, Charles E.; Bernardo, Mark P.

    2010-06-07

    Researchers at DOE’s National Energy Technology Laboratory (NETL) have been investigating the formation of synthetic gas hydrates, with an emphasis on rapid and continuous hydrate formation techniques. The investigations focused on unconventional methods to reduce dissolution, induction, nucleation and crystallization times associated with natural and synthetic hydrates studies conducted in the laboratory. Numerous experiments were conducted with various high-pressure cells equipped with instrumentation to study rapid and continuous hydrate formation. The cells ranged in size from 100 mL for screening studies to proof-of-concept studies with NETL’s 15-Liter Hydrate Cell. The results from this work demonstrate that the rapid and continuousmore » formation of methane hydrate is possible at predetermined temperatures and pressures within the stability zone of a Methane Hydrate Stability Curve.« less

  3. Assumptions and Expectations for Annual Energy Outlook 2014: Oil and Gas Working Group

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

    4: Oil and Gas Working Group AEO2014 Oil and Gas Supply Working Group Meeting Office of Petroleum, Gas, and Biofuels Analysis July 25, 2013 | Washington, DC http://www.eia.gov/forecasts/aeo/workinggroup/ WORKING GROUP PRESENTATION FOR DISCUSSION PURPOSES DO NOT QUOTE OR CITE AS RESULTS ARE SUBJECT TO CHANGE Introduction/Background Office of Petroleum, Gas, and Biofuels Analysis Working Group Presentation for Discussion Purposes Washington, DC, July 25, 2013 DO NOT QUOTE OR CITE as results are

  4. Physical properties of kraft black liquor. Final report. Phase I

    SciTech Connect (OSTI)

    Fricke, A.L.

    1983-12-01

    Methods were selected, equipment installed, and procedures developed for determining rheological properties; for determining thermal properties (stability, density, thermal expansion, and heat capacity); for purification and characterization of lignin (glass transition, stability, weight average molecular weight, and number average molecular weight); and for performing chemical analyses (negative inorganic ions, positive inorganic ions, acid organic salts, lignin, and total solids). A strategy for pulping to supply test liquors was developed, and a statistically designed pulping experiment was specified for a Southern softwood species. Arrangements were made for performing initial pulping work in an industrial pilot plant, and a preliminary set of pulping experiments were conducted. Liquors from the preliminary pulping experiments were used to test procedures and to determine reproducibility of the experiment. Literature was also surveyed and preliminary selection of designs for a pilot digester, and for equipment to determine surface tension were made.

  5. Utah Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet)

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

    Working Gas) (Million Cubic Feet) Utah Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 12,862 9,993 8,285 7,662 9,184 8,305 17,964 25,464 32,121 35,381 24,204 15,997 1991 19,120 11,915 6,118 7,419 9,193 10,977 15,226 20,591 26,089 27,689 23,281 16,335 1992 12,422 11,379 10,289 10,996 13,431 14,981 17,321 20,674 22,548 22,548 24,443 17,445 1993 11,572 6,509 2,846 1,790 6,910 14,321 17,591 21,416 25,209 30,558 28,654

  6. Iowa Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet)

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

    Working Gas) (Million Cubic Feet) Iowa Natural Gas in Underground Storage (Working Gas) (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 74,086 66,477 61,296 61,444 65,918 70,653 76,309 82,236 85,955 89,866 87,913 73,603 1991 71,390 60,921 57,278 59,014 63,510 74,146 79,723 86,294 97,761 109,281 101,166 86,996 1992 67,167 54,513 50,974 53,944 62,448 70,662 82,259 93,130 103,798 112,898 103,734 83,223 1993 18,126 8,099 5,896 10,189 16,993 25,093 35,988 46,332 58,949

  7. Underground Natural Gas Working Storage Capacity - U.S. Energy Information

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

    Administration Underground Natural Gas Working Storage Capacity With Data for November 2015 | Release Date: March 16, 2016 | Next Release Date: February 2017 Previous Issues Year: 2016 2015 2014 2013 2012 2011 prior issues Go Natural gas storage capacity nearly unchanged nationally, but regions vary U.S. natural gas working storage capacity (in terms of design capacity and demonstrated maximum working gas volumes) as of November 2015 was essentially flat compared to November 2014, with some

  8. Utah Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Utah Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 6,258 1,922 -2,167 -243 10 2,672 -2,738 -4,873 -6,032 -7,692 -923 338 1992 -6,698 -535 4,172 3,577 4,237 4,004 2,095 84 -3,541 -5,140 1,162 1,110 1993 -850 -4,870 -7,443 -9,206 -6,521 -660 270 742 2,661 8,010 4,211 6,489 1994 7,656 4,514 6,002 8,910 9,109 5,722

  9. Indiana Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Indiana Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -3,295 -2,048 303 1,673 2,267 2,054 632 690 1,081 1,169 1,343 2,765 1991 2,450 1,002 -617 -1,537 -1,372 -2,052 -995 -41 274 4,477 815 -517 1992 -1,493 -820 -1,663 -1,510 -2,353 -796 1,038 506 1,229 -2,650 -2,283 -922 1993 374 -217 1,229 2,820 2,636 2,160

  10. Iowa Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Iowa Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -2,696 -5,556 -4,018 -2,430 -2,408 3,493 3,414 4,058 11,806 19,414 13,253 13,393 1992 -4,224 -6,407 -6,304 -5,070 -1,061 -3,484 2,536 6,836 6,037 3,618 2,568 -3,773 1993 -49,040 -46,415 -45,078 -43,755 -45,456 -45,569 -46,271 -46,798 -44,848 -48,360 -45,854

  11. Kansas Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Kansas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -10,362 -8,989 -8,480 -6,853 -3,138 -3,221 -2,686 -2,091 824 166 -307 3,561 1991 -6,300 -645 -100 -132 5,625 8,255 -439 -9,003 -13,999 -9,506 -35,041 -11,017 1992 16,928 8,288 4,215 1,589 -2,700 -7,788 -6,391 1,723 1,181 -7,206 -7,569 -20,817 1993 -31,418

  12. Kentucky Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Kentucky Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -1,772 682 336 86 308 -489 138 -272 -702 -351 130 2,383 1991 21,249 14,278 11,919 15,552 13,179 11,123 8,684 4,865 1,110 -2,624 -4,707 -1,444 1992 4,569 6,818 5,559 -712 -4,310 -6,053 -7,850 -9,429 -8,687 2,440 7,441 7,127 1993 2,921 -6,726 -11,466

  13. Maryland Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Maryland Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -862 -85 724 658 416 -1,091 -1,477 -807 2,724 -222 -1,505 5,333 1991 4,470 4,339 1,613 1,801 727 1,324 628 202 -123 -686 1,727 2,620 1992 900 -745 -1,784 -3,603 -1,779 -745 -328 -176 -219 356 579 -1,431 1993 153 742 1,488 1,891 777 -736 -1,464 -2,133

  14. Michigan Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Michigan Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -46,336 -12,518 16,386 37,537 39,350 53,475 75,155 66,399 51,354 56,272 78,572 103,458 1991 37,515 32,421 33,438 66,819 45,861 39,009 20,626 -3,335 -36,217 -14,370 -61,674 -66,823 1992 -28,428 -40,296 -82,921 -108,640 -91,199 -80,473 -64,200 -42,476

  15. Montana Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Montana Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 705 2,167 1,643 1,813 -2,403 355 272 -26 131 59 561 542 1991 -4,514 -2,633 -2,648 -1,702 -3,097 151 -280 -908 -3,437 -6,076 -7,308 -6,042 1992 -68,442 -68,852 -67,958 -67,769 -67,999 -68,527 -69,209 -69,883 -70,428 -70,404 -71,019 -73,067 1993 -14,437

  16. Wyoming Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Wyoming Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -525 -558 -653 -568 -437 -289 -114 76 566 493 1,000 1,188 1991 482 1,359 1,901 1,461 980 1,611 1,437 1,173 -147 -1,122 -1,494 -1,591 1992 -23,715 -25,067 -25,923 -26,121 -26,362 -27,771 -28,829 -30,471 -30,725 -31,860 -31,627 -33,317 1993 -9,841 -10,219

  17. Nebraska Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Nebraska Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -3,131 -3,119 -3,529 -3,306 -1,630 -1,017 244 -266 -458 -1,071 -1,072 157 1992 482 508 1,184 660 -762 -277 2,037 3,311 3,592 3,600 1,413 350 1993 -1,474 -2,431 -3,424 -3,068 -1,752 -1,058 -532 116 439 -49,834 -49,012 -47,951 1994 -47,626 -48,394 -47,215

  18. New York Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) New York Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -484 -13 300 294 -712 -349 -288 393 1,101 972 1,011 1,114 1991 3,318 2,144 1,258 2,592 3,476 1,343 977 614 2,324 4,252 -55 2,063 1992 11,224 5,214 -1,963 -2,306 527 2,182 5,330 6,430 3,719 2,374 3,894 -4,958 1993 -6,762 -8,650 -7,154 -6,031 -5,432

  19. Ohio Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Ohio Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 1,596 507 381 -2,931 -46 -596 -311 -234 178 167 7,030 9,898 1991 19,571 17,816 10,871 17,001 13,713 16,734 12,252 11,416 8,857 5,742 -6,023 -8,607 1992 -14,527 -26,506 -45,308 -51,996 -46,282 -36,996 -26,224 -22,672 -22,086 -18,888 -11,177 -16,353 1993 -11,967

  20. Oklahoma Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Oklahoma Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -3,932 5,480 7,289 -2,690 234 1,959 -4,575 -3,502 -6,399 723 4,670 1991 -18,020 -11,848 -7,774 9,453 9,540 10,851 1,058 -1,981 846 -1,053 -36,391 -20,972 1992 4,433 1,077 -7,840 -16,283 -22,923 -22,043 -5,431 -2,118 584 4,227 9,780 -10,318 1993 -69,197

  1. Oregon Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Oregon Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -30,641 13,186 6,384 -1,434 1,227 -3,129 3,399 2,573 2,606 1,953 968 1,423 1991 1,986 2,360 1,291 -869 -1,664 -1,353 -659 -203 99 250 317 582 1992 89 -487 -305 231 1,089 1,075 811 730 509 343 -779 -872 1993 -1,222 -1,079 -221 -204 -131 -374 -387 -356 -231 86

  2. Alaska Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Alaska Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 NA NA NA NA NA NA NA NA NA NA NA NA 2014 11,087 5,754 6,824 6,119 5,428 6,065 5,421 4,685 3,365 1,565 3,028 5,179 2015 4,768 4,958 3,824 3,761 3,574 2,105 2,020 1,381 723 881 189 -679 2016 -515 164 850 2,474 4,360 5,604 - = No Data Reported; -- = Not

  3. Alaska Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Alaska Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2013 NA NA NA NA NA NA NA NA NA NA NA NA 2014 123.8 41.4 49.7 42.7 35.5 37.5 31.7 25.2 16.5 7.1 14.3 26.1 2015 23.8 25.2 18.6 18.4 17.3 9.5 9.0 5.9 3.0 3.7 0.8 -2.7 2016 -2.1 0.7 3.5 10.2 18.0 23.0 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of

  4. Arkansas Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Arkansas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -925 -513 -486 -557 -855 -813 -453 -125 98 112 82 297 1991 -381 -716 -999 -1,230 -1,199 -1,333 -1,373 -1,840 -2,119 -2,147 -2,697 -3,134 1992 -1,855 -2,008 -2,040 -1,913 -2,046 -1,875 -1,510 -861 -426 -502 -100 73 1993 100 -170 -256 -297 -803 -1,041

  5. California Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) California Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 13,690 18,121 8,849 5,853 7,132 14,219 18,130 10,561 13,390 31,974 19,181 9,703 1991 6,425 26,360 4,734 4,680 6,001 17,198 26,493 26,589 17,703 3,011 -3,286 14,947 1992 -6,546 -23,935 -22,706 -29,553 -29,442 -31,729 -31,331 -21,662 -2,945 7,561 4,600

  6. Colorado Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Colorado Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 701 995 446 26 639 1,368 2,249 3,219 1,102 2,496 892 1991 -1,225 1,811 40 2,493 3,883 3,621 1,685 1,583 1,282 1,616 2,927 2,233 1992 6,816 5,146 5,417 2,679 1,253 -728 -859 310 1,516 2,085 -2,078 -3,827 1993 -4,453 -6,128 -1,947 -1,204 1,853 4,502 3,520

  7. Illinois Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Illinois Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 9,275 18,043 13,193 1,851 5,255 9,637 5,108 8,495 9,773 7,534 9,475 11,984 1991 -9,933 -7,259 454 6,145 6,270 3,648 2,744 1,010 -13 7,942 -12,681 -9,742 1992 -9,345 -8,466 -9,599 -19,126 -16,878 -15,372 -13,507 -9,010 -7,228 -7,653 -6,931 -18,707 1993

  8. Tennessee Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Million Cubic Feet) Million Cubic Feet) Tennessee Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1997 0 0 0 0 0 0 0 0 0 0 0 0 1998 0 0 0 0 0 0 0 0 0 0 0 184 1999 197 189 118 122 119 262 235 178 169 171 125 68 2000 34 -17 51 68 53 -90 -197 -274 -377 -433 -377 -236 2001 -68 48 38 32 153 266 298 360 407 420 65 -22 2002 24 85 159 228 100 -16 -60 -126 -176

  9. Texas Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Million Cubic Feet) Million Cubic Feet) Texas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 21,315 40,513 43,111 18,628 12,189 2,033 47 -10,549 -21,072 -9,288 -13,355 -8,946 1991 -42,316 -43,449 -37,554 -58,118 -54,100 -46,988 -56,199 -48,651 -34,294 -48,087 -70,444 -48,747 1992 5,209 -1,207 -6,517 -21,448 -17,577 -24,644 -6,465 9,218 -3,044 -2,525

  10. Differences Between Monthly and Weekly Working Gas In Storage

    Weekly Natural Gas Storage Report (EIA)

    levels. These are estimated from volume data provided by a sample of operators that report on Form EIA-912, "Weekly Underground Natural Gas Storage Report." The EIA first...

  11. Direct Causticizing for Black Liquor Gasification in a Circulating Fluidized Bed

    SciTech Connect (OSTI)

    Scott Sinquefield; Xiaoyan Zeng, Alan Ball

    2010-03-02

    Gasification of black liquor (BLG) has distinct advantages over direct combustion in Tomlinson recovery boilers. In this project we seek to resolve causticizing issues in order to make pressurized BLG even more efficient and cost-effective. One advantage of BLG is that the inherent partial separation of sulfur and sodium during gasification lends itself to the use of proven high yield variants to conventional kraft pulping which require just such a separation. Processes such as polysulfide, split sulfidity, ASAQ, and MSSAQ can increase pulp yield from 1% to 10% over conventional kraft but require varying degrees of sulfur/sodium separation, which requires additional [and costly] processing in a conventional Tomlinson recovery process. However during gasification, the sulfur is partitioned between the gas and smelt phases, while the sodium all leaves in the smelt; thus creating the opportunity to produce sulfur-rich and sulfur-lean white liquors for specialty pulping processes. A second major incentive of BLG is the production of a combustible product gas, rich in H2 and CO. This product gas (a.k.a. “syngas”) can be used in gas turbines for combined cycle power generation (which is twice as efficient as the steam cycle alone), or it can be used as a precursor to form liquid fuels, such as dimethyl ether or Fischer Tropsh diesel. There is drawback to BLG, which has the potential to become a third major incentive if this work is successful. The causticizing load is greater for gasification of black liquor than for combustion in a Tomlinson boiler. So implementing BLG in an existing mill would require costly increases to the causticizing capacity. In situ causticizing [within the gasifier] would handle the entire causticizing load and therefore eliminate the lime cycle entirely. Previous work by the author and others has shown that titanate direct causticizing (i.e. in situ) works quite well for high-temperature BLG (950°C), but was limited to pressures below

  12. Assumptions and Expectations for Annual Energy Outlook 2015: Oil and Gas Working Group

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

    Assumptions and Expectations for Annual Energy Outlook 2016: Oil and Gas Working Group AEO2016 Oil and Gas Supply Working Group Meeting Office of Petroleum, Gas, and Biofuels Analysis December 1, 2015| Washington, DC http://www.eia.gov/forecasts/aeo/workinggroup/ WORKING GROUP PRESENTATION FOR DISCUSSION PURPOSES DO NOT QUOTE OR CITE AS RESULTS ARE SUBJECT TO CHANGE We welcome feedback on our assumptions and documentation * The AEO Assumptions report http://www.eia.gov/forecasts/aeo/assumptions/

  13. Utah Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Utah Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 48.7 19.2 -26.2 -3.2 0.1 32.2 -15.2 -19.1 -18.8 -21.7 -3.8 2.1 1992 -35.0 -4.5 68.2 48.2 46.1 36.5 13.8 0.4 -13.6 -18.6 5.0 6.8 1993 -6.8 -42.8 -72.3 -83.7 -48.5 -4.4 1.6 3.6 11.8 35.5 17.2 37.2 1994 66.2 69.4 210.9 497.9 131.8 40.0 34.2 32.4 40.9 25.7 26.4 36.0 1995 28.4 93.2 100.2 78.2 40.9

  14. West Virginia Natural Gas in Underground Storage - Change in Working Gas

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

    from Same Month Previous Year (Percent) Percent) West Virginia Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 7.1 -3.2 -1.4 0.2 -3.4 -3.9 -4.7 -8.2 -10.5 -10.3 -16.6 -21.9 1992 -15.1 -26.4 -59.0 -61.0 -43.3 -36.0 -27.0 -19.0 -14.7 -8.4 -5.4 18.6 1993 28.7 15.6 28.7 37.5 46.9 48.1 35.0 30.1 32.3 24.3 19.9 -9.9 1994 -36.1 -44.0 -50.4 -9.9 -20.6 -12.2 -4.3 -1.7 -1.2 -1.0 2.5 8.2 1995

  15. Indiana Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Indiana Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 11.0 5.4 -3.6 -8.8 -7.2 -9.9 -4.3 -0.2 0.9 13.4 2.4 -1.7 1992 -6.0 -4.2 -10.1 -9.5 -13.2 -4.2 4.7 1.9 3.9 -7.0 -6.5 -3.1 1993 1.6 -1.2 8.3 19.7 17.1 12.0 6.3 7.0 2.7 -1.9 -0.1 3.1 1994 -0.3 7.7 13.2 1.4 -4.7 -2.3 0.9 -0.1 -0.7 3.7 11.3 11.2 1995 17.4 9.6 8.0 8.6 11.8 7.0 -3.4 -5.3 -3.3

  16. Iowa Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Iowa Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -3.6 -8.4 -6.6 -4.0 -3.7 4.9 4.5 4.9 13.7 21.6 15.1 18.2 1992 -5.9 -10.5 -11.0 -8.6 -1.7 -4.7 3.2 7.9 6.2 3.3 2.5 -4.3 1993 -73.0 -85.1 -88.4 -81.1 -72.8 -64.5 -56.2 -50.3 -43.2 -42.8 -44.2 -51.6 1994 21.3 54.4 61.3 12.0 -0.1 -6.4 -6.3 -3.5 -4.3 1.5 5.3 7.2 1995 3.0 -5.8 -21.7 -39.9 -37.4 -20.3

  17. Kansas Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Kansas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -9.6 -1.2 -0.2 -0.3 11.7 15.5 -0.7 -11.7 -15.1 -9.6 -30.3 -11.8 1992 28.5 15.1 8.5 3.4 -5.0 -12.7 -9.9 2.5 1.5 -8.0 -9.4 -25.3 1993 -41.2 -47.7 -48.5 -45.3 -8.3 9.0 10.7 8.6 12.8 12.5 19.4 24.0 1994 18.1 26.1 43.8 52.2 5.8 -5.9 0.7 2.1 -3.5 -1.6 -3.1 -2.4 1995 11.9 13.5 -4.5 -4.2 -1.5 9.2 0.7

  18. Kentucky Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Kentucky Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 36.3 23.0 19.6 25.2 19.8 15.5 10.9 5.6 1.2 -2.7 -5.1 -1.7 1992 5.7 8.9 7.7 -0.9 -5.4 -7.3 -8.9 -10.3 -9.2 2.6 8.5 8.4 1993 3.5 -8.1 -14.7 -13.7 -3.8 4.4 9.2 12.9 14.8 3.2 -1.2 -9.6 1994 -25.7 -31.2 -28.1 -20.1 -13.8 -10.6 -7.3 -4.7 -7.2 -4.8 1.4 4.5 1995 14.0 16.7 18.3 14.2 16.8 12.2

  19. Louisiana Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Louisiana Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 22.5 -6.7 -11.5 -6.1 4.7 11.3 9.9 6.6 10.0 12.0 -0.1 -13.0 1992 -15.0 -16.6 -17.6 -16.9 -13.0 -14.5 -14.2 -9.8 -8.6 -8.0 -5.3 -9.7 1993 -14.1 -27.1 -40.9 -42.3 -18.5 -3.2 9.0 15.5 21.5 17.1 14.1 13.8 1994 8.5 40.4 69.8 104.5 54.4 28.4 23.9 17.6 8.8 5.4 10.4 15.6 1995 29.7 13.7 22.0

  20. Maryland Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Maryland Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 103.9 379.8 71.8 60.5 13.1 20.1 7.2 1.8 -0.9 -4.6 13.4 22.0 1992 10.3 -13.6 -46.2 -75.4 -28.4 -9.4 -3.5 -1.5 -1.6 2.5 4.0 -9.9 1993 1.6 15.7 71.7 160.6 17.3 -10.3 -16.3 -18.7 -12.6 -1.8 -2.5 -8.9 1994 -45.2 -46.8 -3.2 53.1 28.2 27.5 36.9 27.2 13.4 4.6 -3.5 10.5 1995 103.8 130.7 91.8

  1. Michigan Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Michigan Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 12.0 12.8 14.6 30.2 17.0 11.7 5.0 -0.7 -6.8 -2.6 -11.4 -14.2 1992 -8.1 -14.1 -31.6 -37.7 -28.9 -21.6 -14.9 -8.9 1.2 -1.2 1.1 -2.0 1993 -7.5 -20.7 -25.8 -17.2 -1.0 3.7 5.2 7.6 6.1 6.7 6.2 7.4 1994 -4.8 -0.4 22.1 37.4 24.6 15.8 10.2 7.2 6.2 5.4 12.3 21.2 1995 45.7 54.3 51.8 20.6 8.0 3.8

  2. Mississippi Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Mississippi Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 31.9 17.1 14.2 15.5 11.1 7.9 -1.1 -5.7 -3.6 -2.3 -15.3 -16.4 1992 -6.8 1.1 -4.7 -16.9 -14.3 -8.0 -2.7 -5.4 -2.8 -7.0 5.6 3.5 1993 13.6 -2.2 -12.3 -6.0 1.7 0.0 0.9 6.3 4.6 1.9 -35.2 -40.7 1994 -53.0 -55.0 -36.7 -28.8 -29.8 -34.1 -28.0 -22.8 -26.7 -21.5 26.7 39.2 1995 50.8 54.7 11.0

  3. Missouri Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Missouri Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -5.1 1.4 -20.3 -2.8 6.8 8.3 12.5 12.3 7.8 7.6 9.9 13.8 1992 -2.8 6.5 23.0 7.8 3.7 4.3 3.8 2.6 2.5 2.2 -0.2 -0.1 1993 5.3 -3.5 -16.4 -13.3 -4.7 -0.9 -2.8 -1.6 -1.6 -1.3 -2.5 -0.8 1994 -3.1 17.2 37.2 -28.6 -19.3 -6.9 -4.2 -4.1 -3.3 -3.3 0.7 -1.0 1995 7.9 12.0 16.0 64.0 35.0 10.4 5.7 6.0

  4. Montana Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Montana Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -2.5 -1.5 -1.5 -1.0 -1.7 0.1 -0.2 -0.5 -1.8 -3.2 -3.9 -3.3 1992 -38.1 -38.6 -38.4 -38.3 -38.2 -38.2 -38.2 -38.3 -38.6 -38.8 -39.8 -41.8 1993 -13.0 -15.6 -17.8 -19.4 -21.2 -22.4 -22.0 -22.3 -21.6 -20.7 -20.8 -19.6 1994 -19.3 -21.6 -20.5 -19.8 -17.7 -14.9 -14.5 -13.6 -12.0 -10.7 -9.8 -9.5

  5. Wyoming Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Wyoming Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 0.9 2.6 3.7 2.8 1.8 3.0 2.5 2.0 -0.2 -1.8 -2.5 -2.7 1992 -43.8 -46.9 -48.5 -48.7 -48.6 -49.4 -49.4 -50.6 -50.1 -51.9 -53.3 -58.2 1993 -32.4 -36.0 -35.5 -33.5 -30.9 -25.0 -21.0 -16.0 -14.5 -8.3 -12.5 -8.1 1994 4.1 2.9 8.2 10.1 12.7 5.3 0.8 0.6 1.5 1.5 11.2 14.0 1995 3.4 11.3 0.7 -7.6

  6. Nebraska Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Nebraska Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -5.7 -5.8 -6.6 -6.0 -2.9 -1.8 0.4 -0.5 -0.8 -1.8 -1.9 0.3 1992 0.9 1.0 2.4 1.3 -1.4 -0.5 3.6 5.9 6.3 6.3 2.5 0.6 1993 -2.8 -4.7 -6.6 -5.9 -3.3 -1.9 -0.9 0.2 0.7 -82.3 -84.6 -88.0 1994 -93.2 -98.5 -98.2 -96.2 -92.3 -91.2 -88.8 -88.5 -85.3 -7.5 12.8 23.1 1995 74.4 582.5 367.3 113.6 15.1

  7. New York Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) New York Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 9.4 7.6 5.1 9.8 10.8 3.2 1.9 1.0 3.5 6.1 -0.1 3.5 1992 29.1 17.2 -7.6 -7.9 1.5 5.0 10.3 10.6 5.4 3.2 5.6 -8.1 1993 -13.6 -24.4 -30.1 -22.5 -15.0 -8.4 -9.2 -18.9 -12.1 -13.4 -14.1 -5.6 1994 -5.8 -1.8 7.8 29.0 14.9 14.1 9.6 21.1 10.7 9.5 11.2 14.4 1995 15.8 23.8 49.4 1.6 0.9 -1.4 -4.4

  8. Ohio Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Ohio Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 19.5 22.4 15.4 23.1 14.3 14.4 9.1 7.4 5.2 3.1 -3.3 -5.5 1992 -12.1 -27.3 -55.6 -57.4 -42.1 -27.9 -17.8 -13.7 -12.2 -10.0 -6.4 -11.0 1993 -11.3 -30.2 -60.3 -56.1 -31.6 -21.4 -13.8 -8.2 -0.9 -3.4 -7.9 -16.2 1994 -41.7 -61.0 -63.3 24.5 16.2 6.8 8.5 6.1 2.5 4.6 10.6 27.3 1995 67.7 179.6 562.8 43.0

  9. Oklahoma Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Oklahoma Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -13.9 -10.0 -6.5 8.1 7.3 7.8 0.7 -1.3 0.5 -0.6 -20.1 -13.6 1992 4.0 1.0 -7.0 -12.9 -16.3 -14.6 -3.6 -1.4 0.4 2.5 6.8 -7.7 1993 -59.8 -75.3 -81.3 -71.8 -58.1 -47.8 -43.7 -38.0 -33.1 -31.7 -34.3 -29.9 1994 20.6 33.2 68.7 60.2 49.2 29.1 25.2 21.3 11.9 8.6 24.6 27.3 1995 54.1 106.0 91.5

  10. Oregon Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Oregon Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1990 -0.1 1991 53.6 99.8 77.4 -30.5 -38.2 -24.2 -10.4 -2.9 1.3 3.3 4.2 8.6 1992 1.6 -10.3 -10.3 11.6 40.4 25.3 14.2 10.7 6.8 4.4 -9.9 -11.9 1993 -21.1 -25.4 -8.3 -9.2 -3.5 -7.0 -5.9 -4.7 -2.9 1.1 6.4 -1.1 1994 12.9 27.1 26.3 -67.7 -49.1 -32.2 -25.7 -21.5 -18.6 -20.3 -18.4 -14.3 1995 -25.9 -14.7

  11. Alabama Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Alabama Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1996 221.1 244.8 179.6 64.8 86.8 112.2 130.5 1997 36.2 10.9 111.7 57.1 68.4 -5.0 -17.0 -19.4 -19.9 -12.1 -19.0 36.2 1998 31.5 45.0 -21.4 4.3 -12.4 46.2 38.7 23.0 -24.8 -0.8 15.1 6.0 1999 3.8 17.6 11.5 -11.9 35.3 -11.6 6.5 -2.0 67.7 4.7 12.2 10.2 2000 7.9 25.4 213.4 116.8 22.2 51.5 32.4 25.3

  12. Arkansas Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Arkansas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -4.4 -8.3 -11.6 -14.2 -13.7 -14.5 -14.1 -18.0 -20.2 -20.4 -25.8 -30.6 1992 -22.4 -25.3 -26.8 -25.8 -27.1 -23.8 -18.0 -10.3 -5.1 -6.0 -1.3 1.0 1993 1.6 -2.9 -4.6 -5.4 -14.6 -17.3 -27.6 -34.0 -37.6 -37.9 -42.3 -48.2 1994 -63.6 -74.6 -86.5 -87.0 -71.6 -60.3 -47.2 -35.4 -31.0 -29.2 -21.3

  13. California Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) California Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 5.1 24.7 4.3 3.5 3.8 10.1 15.1 15.0 9.7 1.5 -1.7 9.7 1992 -4.9 -18.0 -19.6 -21.6 -18.0 -16.9 -15.6 -10.6 -1.5 3.8 2.4 -16.7 1993 -15.0 -19.6 8.1 2.5 3.1 -2.6 3.4 1.5 1.3 1.5 0.5 17.0 1994 13.4 -12.0 -24.5 -13.5 -10.9 -5.7 -8.4 -8.0 -4.2 -3.3 -6.0 -2.0 1995 7.4 63.0 54.5 20.8 14.6

  14. Colorado Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Colorado Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -4.5 8.0 0.2 18.3 29.2 20.6 7.1 5.5 3.8 4.6 8.4 6.4 1992 25.9 21.0 30.9 16.6 7.3 -3.4 -3.4 1.0 4.3 5.7 -5.5 -10.4 1993 -13.5 -20.7 -8.5 -6.4 10.0 22.0 14.3 3.5 -1.4 -12.0 -15.0 -11.5 1994 -15.3 -17.8 -21.0 -34.7 -16.3 -25.8 -16.1 -9.6 -6.1 0.2 7.4 0.2 1995 2.9 10.9 -0.8 5.3 -17.3 7.8

  15. Illinois Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Illinois Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -4.2 -4.0 0.3 4.2 3.5 1.7 1.1 0.4 0.0 2.4 -3.8 -3.3 1992 -4.2 -4.8 -6.4 -12.6 -9.2 -7.2 -5.6 -3.3 -2.3 -2.3 -2.2 -6.6 1993 -24.0 -31.6 -36.3 -30.7 -24.7 -20.2 -17.4 -16.7 -14.3 -13.7 -11.6 -12.9 1994 -3.7 -1.1 10.0 6.3 -2.8 -4.3 -2.6 -1.9 -1.2 -0.2 0.0 4.9 1995 13.3 6.3 -0.8 -4.1 -24.0

  16. Tennessee Natural Gas in Underground Storage - Change in Working Gas from

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

    Same Month Previous Year (Percent) Percent) Tennessee Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1997 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 1998 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 1999 43.0 55.3 41.7 61.2 59.6 131.5 70.6 38.1 29.2 25.1 16.0 8.6 2000 5.3 -3.2 12.8 21.0 16.7 -19.5 -34.7 -42.4 -50.4 -50.8 -41.4 -27.6 2001 -9.8 9.3 8.4 8.3 41.3 71.7 80.1 97.0 109.6

  17. Texas Natural Gas in Underground Storage - Change in Working Gas from Same

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

    Month Previous Year (Percent) Percent) Texas Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Percent) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 1991 -13.2 -13.8 -12.2 -16.7 -15.1 -12.7 -14.7 -12.9 -9.1 -12.1 -17.5 -13.3 1992 1.9 -0.4 -2.4 -7.4 -5.8 -7.6 -2.0 2.8 -0.9 -0.7 -2.1 -9.0 1993 -41.9 -44.7 -46.6 -41.3 -35.7 -33.7 -35.4 -35.0 -36.7 -35.5 -35.3 -32.7 1994 -13.0 -30.4 -20.9 -13.7 -8.3 -8.3 -0.1 3.0 15.2 17.2 27.0 21.5 1995 49.9 85.3

  18. Generator-Absorber heat exchange transfer apparatus and method using an intermediate liquor

    DOE Patents [OSTI]

    Phillips, Benjamin A.; Zawacki, Thomas S.

    1996-11-05

    Numerous embodiments and related methods for generator-absorber heat exchange (GAX) are disclosed, particularly for absorption heat pump systems. Such embodiments and related methods use the working solution of the absorption system for the heat transfer medium where the working solution has an intermediate liquor concentration.

  19. Western Consuming Region Natural Gas Working Underground Storage (Billion

    Gasoline and Diesel Fuel Update (EIA)

    Proved Reserves (Billion Cubic Feet) West Virginia Shale Proved Reserves (Billion Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 2000's 0 14 688 2010's 2,491 6,043 9,408 18,078 28,311 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 11/19/2015 Next Release Date: 12/31/2016 Referring Pages: Shale Natural Gas Proved Reserves as of Dec. 31 West Virginia Shale Gas Proved

  20. Government works with technology to boost gas output/usage

    SciTech Connect (OSTI)

    Nicoll, H.

    1996-10-01

    Specially treated ethane gas from fields of the Moomba area in the Cooper basin of South Australia now flows freely through 870 mi of interstate gas pipeline to an end-user in Sydney, New South Wales. This unprecedented usage of ethane is the result of a long-term cooperative agreement. The producer sought to provide the end-user with ethane gas for usage as a petrochemical feedstock to manufacture ethylene and plastic goods. The end-user had strict specifications for a low-CO{sub 2}, very dry ethane product with a small percentage of methane. In order to meet these, the producer committed millions of dollars to construct a high-technology, state-of-the-art ethane treatment facility in the Moomba area, and lay an extensive pipeline. Santos also contracted with the amines supplier to provide a high-performance, deep CO{sub 2} removal solvent with good corrosion prevention characteristics. The paper discusses the Moomba field overflow, gas treatment, government cooperation, and project completion.

  1. HIGHLY ENERGY EFFICIENT D-GLU (DIRECTED-GREEN LIQ-UOR UTILIZATION) PULPING

    SciTech Connect (OSTI)

    Lucia, Lucian A

    2013-04-19

    Purpose: The purpose of the project was to retrofit the front end (pulp house) of a commercial kraft pulping mill to accommodate a mill green liquor (GL) impregna-tion/soak/exposure and accrue downstream physical and chemical benefits while prin-cipally reducing the energy footprint of the mill. A major player in the mill contrib-uting to excessive energy costs is the lime kiln. The project was intended to offload the energy (oil or natural gas) demands of the kiln by by-passing the causticization/slaking site in the recovery area and directly using green liquor as a pulping medium for wood. Scope: The project was run in two distinct, yet mutually compatible, phases: Phase 1 was the pre-commercial or laboratory phase in which NC State University and the Insti-tute of Paper Science and Technology (at the Georgia Institute of Technology) ran the pulping and associated experiments, while Phase 2 was the mill scale trial. The first tri-al was run at the now defunct Evergreen Pulp Mill in Samoa, CA and lead to a partial retrofit of the mill that was not completed because it went bankrupt and the work was no longer the low-hanging fruit on the tree for the new management. The second trial was run at the MeadWestvaco Pulp Mill in Evedale, TX which for all intents and pur-poses was a success. They were able to fully retrofit the mill, ran the trial, studied the pulp properties, and gave us conclusions.

  2. Investigation of Pressurized Entrained-Flow Kraft Black Liquor Gasification in an Industrially Relevant Environment

    SciTech Connect (OSTI)

    Kevin Whitty

    2008-06-30

    The University of Utah's project 'Investigation of Pressurized Entrained-Flow Kraft Black Liquor Gasification in an Industrially Relevant Environment' (U.S. DOE Cooperative Agreement DE-FC26-04NT42261) was a response to U.S. DOE/NETL solicitation DE-PS36-04GO94002, 'Biomass Research and Development Initiative' Topical Area 4-Kraft Black Liquor Gasification. The project began September 30, 2004. The objective of the project was to improve the understanding of black liquor conversion in high pressure, high temperature reactors that gasify liquor through partial oxidation with either air or oxygen. The physical and chemical characteristics of both the gas and condensed phase were to be studied over the entire range of liquor conversion, and the rates and mechanisms of processes responsible for converting the liquor to its final smelt and syngas products were to be investigated. This would be accomplished by combining fundamental, lab-scale experiments with measurements taken using a new semi-pilot scale pressurized entrained-flow gasifier. As a result of insufficient availability of funds and changes in priority within the Office of Biomass Programs of the U.S. Department of Energy, the research program was terminated in its second year. In total, only half of the budgeted funding was made available for the program, and most of this was used during the first year for construction of the experimental systems to be used in the program. This had a severe impact on the program. As a consequence, most of the planned research was unable to be performed. Only studies that relied on computational modeling or existing experimental facilities started early enough to deliver useful results by the time to program was terminated Over the course of the program, small scale (approx. 1 ton/day) entrained-flow gasifier was designed and installed at the University of Utah's off-campus Industrial Combustion and Gasification Research Facility. The system is designed to operate at

  3. Novel Pulping Technology: Directed Green Liquor Utilization (D-GLU) Pulping

    SciTech Connect (OSTI)

    Lucian A. Lucia

    2005-11-15

    The general objectives of this new project are the same as those described in the original proposal. Conventional kraft pulping technologies will be modified for significant improvements in pulp production, such as strength, bleachability, and yield by using green liquor, a naturally high, kraft mill-derived sulfidity source. Although split white liquor sulfidity and other high sulfidity procedures have the promise of addressing several of the latter important economic needs of pulp mills, they require considerable engineering/capital retrofits, redesigned production methods, and thus add to overall mill expenditures. Green liquor use, however, possesses the required high sulfidity to obtain in general the benefits attributable to higher sulfidity cooking, without the required capital constraints for implementation. Before introduction of green liquor in our industrial operations, a stronger understanding of its fundamental chemical interaction with the lignin and carbohydrates in US hardwood and softwoods must be obtained. In addition, its effect on bleachability, enhancement of pulp properties, and influence on the overall energy and recovery of the mill requires further exploration before the process witnesses widespread mill use in North America. Thus, proof of principle will be accomplished in this work and the consequent effect of green liquor and other high sulfide sources on the pulping and bleaching operations will be explored for US kraft mills. The first year of this project will generate the pertinent information to validate its ability for implementation in US pulping operations, whereas year two will continue this work while proceeding to analyze pulp bleachability and final pulp/paper properties and develop a general economic and feasibility analysis for its eventual implementation in North America.

  4. South Central Region Natural Gas in Underground Storage - Change in Working

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

    Gas from Same Month Previous Year (Million Cubic Feet) - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) South Central Region Natural Gas in Underground Storage - Change in Working Gas from Same Month Previous Year (Million Cubic Feet) Year Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec 2014 -281,823 -324,789 -326,968 -286,719 -287,056 -272,324 -254,513 -242,345 -212,206 -137,887 -86,360 54,089 2015 162,728 123,241 237,326 322,874 360,298 336,237 294,425 289,394

  5. Regeneration of FGD waste liquors: Production of ammonium and potassium sulfate mixed fertilizer. Quarterly technical report, July 1993--September 1993

    SciTech Connect (OSTI)

    Randolph, A.D.; Kwon, T.M.

    1993-12-01

    Regeneration of the Fe{sup II}-EDTA scrubbing liquors for simultaneous removal of SO{sub 2} and NO{sub x} in flue gas involves removing the nitrogen-sulfur (N-S) compounds accumulated in the liquor. In this paper, the authors investigated a simple regeneration process which selectively precipitates the N-S compounds as potassium salts and then hydrolyzes them to yield ammonium/potassium sulfate as a marketable byproduct. They believe this is the first report on precipitation and hydrolysis characteristics of the N-S compounds in actual waste scrubbing liquor. Precipitation of the N-S compounds was achieved by adding K{sub 2}SO{sub 4} to the scrubbing liquor. Effects of the amount of added K{sub 2}SO{sub 4} on the amount of removed N-S compounds, precipitated crystals, and the potassium left over in the scrubbing liquor were studied. Hydrolysis of the precipitated N-S compounds to ammonium sulfate was performed in a sulfuric acid environment. Effects of acidity, concentration of N-S compounds, and temperature on the hydrolysis are discussed. Analysis of the observed hydrolysis pattern showed that the reaction proceeded following first order kinetics in terms of N-S compound concentration.

  6. Development of advanced technology of coke oven gas drainage treatment

    SciTech Connect (OSTI)

    Higashi, Tadayuki; Yamaguchi, Akikazu; Ikai, Kyozou; Kamiyama, Hisarou; Muto, Hiroshi

    1996-12-31

    In April 1994, commercial-scale application of ozone oxidation to ammonia liquor (which is primarily the water condensing from coke oven gas) to reduce its chemical oxygen demand (COD) was started at the Nagoya Works of Nippon Steel Corporation. This paper deals with the results of technical studies on the optimization of process operating conditions and the enlargement of equipment size and the operating purification system.

  7. U.S. Working Natural Gas Underground Storage Acquifers Capacity (Million

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

    Cubic Feet) Acquifers Capacity (Million Cubic Feet) U.S. Working Natural Gas Underground Storage Acquifers Capacity (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 2000's 396,950 396,092 2010's 364,228 363,521 367,108 453,054 452,044 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 08/31/2016 Next Release Date: 09/30/2016 Referring Pages: Working Gas

  8. Coke oven gas treatment and by-product plant of Magnitogorsk Integrated Iron and Steel Works

    SciTech Connect (OSTI)

    Egorov, V.N.; Anikin, G.J.; Gross, M.

    1995-12-01

    Magnitogorsk Integrated Iron and Steel Works, Russia, decided to erect a new coke oven gas treatment and by-product plant to replace the existing obsolete units and to improve the environmental conditions of the area. The paper deals with the technological concept and the design requirements. Commissioning is scheduled at the beginning of 1996. The paper describes H{sub 2}S and NH{sub 3} removal, sulfur recovery and ammonia destruction, primary gas cooling and electrostatic tar precipitation, and the distributed control system that will be installed.

  9. Proceedings of the black liquor research program review fourth meeting held July 28--30, 1987

    SciTech Connect (OSTI)

    Emerson, D. B.; Whitworth, B. A.

    1987-10-01

    Research programs, presented at the black liquor review meeting are described. Research topics include the following: Cooperative Program in Kraft Recovery; Black Liquor Physical Properties; Viscosity of Strong Black Liquor; Ultrafiltration of Kraft Black Liquor; Molecular Weight Distribution of Kraft Lignin; Black Liquor Droplet Formation Project; Fundamental Studies of Black Liquor Combustion; Black Liquor Combustion Sensors; Flash X-ray Imagining of Black Liquor Sprays; Laser Induced Fluorescence For Process Control In The Pulp and Paper Industry; Recovery Boiler Optimization; Black Liquor Gasification and Use of the Products in Combined-Cycle Cogeneration; Black Liquor Steam Plasma Automization; The B and W Pyrosonic 2000R System; Monsteras Boiler Control System; and Cooperative Program Project Reviews. Individual projects are processed separately for the data bases.

  10. U.S. Working Natural Gas Underground Storage Salt Caverns Capacity (Million

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

    Cubic Feet) Salt Caverns Capacity (Million Cubic Feet) U.S. Working Natural Gas Underground Storage Salt Caverns Capacity (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 2000's 230,456 271,785 2010's 312,003 351,017 488,268 455,729 488,698 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 08/31/2016 Next Release Date: 09/30/2016 Referring Pages: Working

  11. Method and apparatus for removing non-condensible gas from a working fluid in a binary power system

    DOE Patents [OSTI]

    Mohr, Charles M.; Mines, Gregory L.; Bloomfield, K. Kit

    2002-01-01

    Apparatus for removing non-condensible gas from a working fluid utilized in a thermodynamic system comprises a membrane having an upstream side operatively connected to the thermodynamic system so that the upstream side of the membrane receives a portion of the working fluid. The first membrane separates the non-condensible gas from the working fluid. A pump operatively associated with the membrane causes the portion of the working fluid to contact the membrane and to be returned to the thermodynamic system.

  12. Drum drying of black liquor using superheated steam impinging jets

    SciTech Connect (OSTI)

    Shiravi, A.H.; Mujumdar, A.S.; Kubes, G.J. [McGill Univ., Montreal, Quebec (Canada)

    1997-05-01

    A novel drum dryer for black liquor utilizing multiple impinging jets of superheated steam was designed and built to evaluate the performance characteristics and effects of various operating parameters thereon. Appropriate ranges of parameters such as steam jet temperature and velocity were examined experimentally to quantify the optimal operating conditions for the formation of black liquor film on the drum surface as well as the drying kinetics.

  13. U.S. Working Natural Gas Underground Storage Depleted Fields Capacity

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

    (Million Cubic Feet) Depleted Fields Capacity (Million Cubic Feet) U.S. Working Natural Gas Underground Storage Depleted Fields Capacity (Million Cubic Feet) Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 2000's 3,583,786 3,659,968 2010's 3,733,993 3,769,113 3,720,980 3,839,852 3,844,927 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data. Release Date: 08/31/2016 Next Release Date:

  14. Blast furnace gas fired boiler for Eregli Iron and Steel Works (Erdemir), Turkey

    SciTech Connect (OSTI)

    Green, J.; Strickland, A.; Kimsesiz, E.; Temucin, I.

    1996-11-01

    Eregli Demir ve Celik Fabriklari T.A.S. (Eregli Iron and Steel Works Inc.), known as Erdemir, is a modern integrated iron and steel works on the Black Sea coast of Turkey, producing flat steel plate. Facilities include two blast furnaces, coke ovens, and hot and cold rolling mills, with a full supporting infrastructure. Four oil- and gas-fired steam boilers provide steam for electric power generation, and to drive steam turbine driven fans for Blast Furnace process air. Two of these boilers (Babcock and Wilcox Type FH) were first put into operation in 1965, and still reliably produce 100 tons/hour of steam at a pressure of 44 bar and a temperature of 410 C. In 1989 Erdemir initiated a Capacity Increase and Modernization Project to increase the steel production capability from two million to three million tons annually. This project also incorporates technology to improve the product quality. Its goals include a reduction in energy expenses to improve Erdemir`s competitiveness. The project`s scheduled completion is in late 1995. The by-product gases of the blast furnaces, coke ovens, and basic oxygen furnaces represent a considerable share of the consumed energy in an integrated iron and steel works. Efficient use of these fuels is an important factor in improving the overall efficiency of the operation.

  15. Huge natural gas reserves central to capacity work, construction plans in Iran

    SciTech Connect (OSTI)

    Not Available

    1994-07-11

    Questions about oil production capacity in Iran tend to mask the country's huge potential as a producer of natural gas. Iran is second only to Russia in gas reserves, which National Iranian Gas Co. estimates at 20.7 trillion cu m. Among hurdles to Iran's making greater use of its rich endowment of natural gas are where and how to sell gas not used inside the country. The marketing logistics problem is common to other Middle East holders of gas reserves and a reason behind the recent proliferation of proposals for pipeline and liquefied natural gas schemes targeting Europe and India. But Iran's challenges are greater than most in the region. Political uncertainties and Islamic rules complicate long-term financing of transportation projects and raise questions about security of supply. As a result, Iran has remained mostly in the background of discussions about international trade of Middle Eastern gas. The country's huge gas reserves, strategic location, and existing transport infrastructure nevertheless give it the potential to be a major gas trader if the other issues can be resolved. The paper discusses oil capacity plans, gas development, gas injection for enhanced oil recovery, proposals for exports of gas, and gas pipeline plans.

  16. Black liquor combustion validated recovery boiler modeling: Final year report. Volume 4 (Appendix IV)

    SciTech Connect (OSTI)

    Grace, T.M.; Frederick, W.J.; Salcudean, M.; Wessel, R.A.

    1998-08-01

    This project was initiated in October 1990, with the objective of developing and validating a new computer model of a recovery boiler furnace using a computational fluid dynamics (CFD) code specifically tailored to the requirements for solving recovery boiler flows, and using improved submodels for black liquor combustion based on continued laboratory fundamental studies. The key tasks to be accomplished were as follows: (1) Complete the development of enhanced furnace models that have the capability to accurately predict carryover, emissions behavior, dust concentrations, gas temperatures, and wall heat fluxes. (2) Validate the enhanced furnace models, so that users can have confidence in the predicted results. (3) Obtain fundamental information on aerosol formation, deposition, and hardening so as to develop the knowledge base needed to relate furnace model outputs to plugging and fouling in the convective sections of the boiler. (4) Facilitate the transfer of codes, black liquid submodels, and fundamental knowledge to the US kraft pulp industry. Volume 4 contains the following appendix sections: Radiative heat transfer properties for black liquor combustion -- Facilities and techniques and Spectral absorbance and emittance data; and Radiate heat transfer determination of the optical constants of ash samples from kraft recovery boilers -- Calculation procedure; Computation program; Density determination; Particle diameter determination; Optical constant data; and Uncertainty analysis.

  17. A comprehensive program to develop correlations for physical properties of kraft black liquor. Final report

    SciTech Connect (OSTI)

    Fricke, A.L.; Zaman, A.A.

    1998-05-01

    The overall objective of the program was to develop correlations to predict physical properties within requirements of engineering precision from a knowledge of pulping conditions and of kraft black liquor composition, if possible. These correlations were to include those relating thermodynamic properties to pulping conditions and liquor composition. The basic premise upon which the research was based is the premise that black liquor behaves as a polymer solution. This premise has proven to be true, and has been used successfully in developing data reduction methods and in interpreting results. A three phase effort involving pulping, analysis of liquor composition, and measurement of liquor properties was conducted.

  18. Integration of the Mini-Sulfide Sulfite Anthraquinone (MSS-AQ) Pulping Process and Black Liquor Gasification in a Pulp Mill

    SciTech Connect (OSTI)

    Hasan Jameel, North Carolina State University; Adrianna Kirkman, North Carolina State University; Ravi Chandran,Thermochem Recovery International Brian Turk Research Triangle Institute; Brian Green, Research Triangle Institute

    2010-01-27

    produced a comparable tensile and burst index pulps. Product gas composition determined using computer simulations The results demonstrate that RVS-1 can effectively remove > 99.8% of the H2S present in simulated synthesis gas generated from the gasification of black liquor. This level of sulfur removal was consistent over simulated synthesis gas mixtures that contained from 6 to 9.5 vol % H2S.A significant amount of the sulfur in the simulated syngas was recovered as SO2 during regeneration. The average recovery of sulfur as SO2 was about 75%. Because these are first cycle results, this sulfur recovery is expected to improve. Developed WINGems model of the process.The total decrease in variable operating costs for the BLG process compared to the HERB was in excess of $6,200,000 per year for a mill producing 350,000 tons of pulp per year. This represents a decrease in operating cost of about $17.7/ton of oven dry pulp produced. There will be additional savings in labor and maintenance cost that has not been taken into account. The capital cost for the MSSAQ based gasifier system was estimated at $164,000,000, which is comparable to a High Efficiency Recovery Boiler. The return on investment was estimated at 4%. A gasifier replacement cannot be justified on its own, however if the recovery boiler needs to be replaced the MSSAQ gasifier system shows significantly higher savings. Before black liquor based gasifer technology can be commercialized more work is necessary. The recovery of the absorbed sulfur in the absorbent as sulfur dioxide is only 75%. This needs to be greater than 90% for economical operation. It has been suggested that as the number of cycles is increased the sulfur dioxide recovery might improve. Further research is necessary. Even though a significant amount of work has been done on a pilot scale gasifiers using liquors containing sulfur, both at low and high temperatures the lack of a commercial unit is an impediment to the implementation of the MSSAQ

  19. Estimate of Maximum Underground Working Gas Storage Capacity in the United States: 2007 Update

    Reports and Publications (EIA)

    2007-01-01

    This report provides an update to an estimate for U.S. aggregate natural gas storage capacity that was released in 2006.

  20. CLEAR LIQUOR SCRUBBING WITH ANHYDRITE PRODUCTION

    SciTech Connect (OSTI)

    R.C. SKARUPA; T.R. CAREY

    1998-08-01

    This project is funded by the US Department of Energy's Federal Energy Technology Center (DOE/FETC) under a cost-sharing PRDA with Radian International. The Electric Power Research Institute (EPRI) is providing co-funding and technical oversight. The project is part of FETC's Advanced Power Systems Program, whose mission is to accelerate the commercialization of affordable, high-efficiency, low emission, coal-fueled electric generating technologies. This project was submitted in response to Area 4 of DOE's Mega-PRDA: Advanced High-Performance SO{sub 2} Control Concepts. The goals of this research area are to develop advanced flue gas desulfurization (FGD) processes that achieve greater than 99% SO{sub 2} removal efficiency, are 25% cheaper than commercial FGD systems, and provide a valuable byproduct that will be recycled rather than disposed. Area 4 also included the development of a byproduct process that could be added to FGD systems to produce high value byproducts for reuse rather than disposal.

  1. Philadelphia gas works medium-Btu coal gasification project: capital and operating cost estimate, financial/legal analysis, project implementation

    SciTech Connect (OSTI)

    Not Available

    1981-12-01

    This volume of the final report is a compilation of the estimated capital and operating costs for the project. Using the definitive design as a basis, capital and operating costs were developed by obtaining quotations for equipment delivered to the site. Tables 1.1 and 1.2 provide a summary of the capital and operating costs estimated for the PGW Coal Gasification Project. In the course of its Phase I Feasibility Study of a medium-Btu coal-gas facility, Philadelphia Gas Works (PGW) identified the financing mechanism as having great impact on gas cost. Consequently, PGW formed a Financial/Legal Task Force composed of legal, financial, and project analysis specialists to study various ownership/management options. In seeking an acceptable ownership, management, and financing arrangement, certain ownership forms were initially identified and classified. Several public ownership, private ownership, and third party ownership options for the coal-gas plant are presented. The ownership and financing forms classified as base alternatives involved tax-exempt and taxable financing arrangements and are discussed in Section 3. Project implementation would be initiated by effectively planning the methodology by which commercial operation will be realized. Areas covered in this report are sale of gas to customers, arrangements for feedstock supply and by-product disposal, a schedule of major events leading to commercialization, and a plan for managing the implementation.

  2. Estimate of Maximum Underground Working Gas Storage Capacity in the United States

    Reports and Publications (EIA)

    2006-01-01

    This report examines the aggregate maximum capacity for U.S. natural gas storage. Although the concept of maximum capacity seems quite straightforward, there are numerous issues that preclude the determination of a definitive maximum volume. The report presents three alternative estimates for maximum capacity, indicating appropriate caveats for each.

  3. Control of SOx emission in tail gas of the Claus Plant at Kwangyang Steel Works

    SciTech Connect (OSTI)

    Kang, H.S.; Park, J.W.; Hyun, H.D.; Lee, D.S.; Paik, S.C.; Chung, J.S.

    1995-12-01

    Pilot and/or laboratory studies were conducted in order to find methods for reducing the SOx emission in the Claus tail gas of the cokes unit. The TGT process which is based on the complete hydrogenation of the sulfur-containing compounds (SO{sub 2}, S) into H{sub 2}S and returning to the COG main line can reduce the SOx emission to zero. In case the return to the COG main is impossible, the SPOR process (Sulfur removal based on Partial Oxidation and Reduction) can be successfully applied to reduce the SOx emission.

  4. U.S. Working Natural Gas Total Underground Storage Capacity (Million Cubic

    Gasoline and Diesel Fuel Update (EIA)

    586,953 575,601 549,151 489,505 505,318 514,809 1978-2014 From Gas Wells 259,848 234,236 208,970 204,667 186,887 159,337 1978-2014 From Oil Wells 327,105 341,365 340,182 284,838 318,431 355,472 1978

    Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1970's NA NA NA NA NA NA NA 1980's 155 176 145 132 110 126 113 101 101 107 1990's 123 113 118 119 111 110 109 103 102 98 2000's 90 86 68 68 60 64 66 63 61 65 2010's 65 60 61 55 60 59 - = No Data Reported; -- = Not

  5. Black liquor combustion validated recovery boiler modeling: Final year report. Volume 2 (Appendices I, section 5 and II, section 1)

    SciTech Connect (OSTI)

    Grace, T.M.; Frederick, W.J.; Salcudean, M.; Wessel, R.A.

    1998-08-01

    This project was initiated in October 1990, with the objective of developing and validating a new computer model of a recovery boiler furnace using a computational fluid dynamics (CFD) code specifically tailored to the requirements for solving recovery boiler flows, and using improved submodels for black liquor combustion based on continued laboratory fundamental studies. The key tasks to be accomplished were as follows: (1) Complete the development of enhanced furnace models that have the capability to accurately predict carryover, emissions behavior, dust concentrations, gas temperatures, and wall heat fluxes. (2) Validate the enhanced furnace models, so that users can have confidence in the predicted results. (3) Obtain fundamental information on aerosol formation, deposition, and hardening so as to develop the knowledge base needed to relate furnace model outputs to plugging and fouling in the convective sections of the boiler. (4) Facilitate the transfer of codes, black liquid submodels, and fundamental knowledge to the US kraft pulp industry. Volume 2 contains the last section of Appendix I, Radiative heat transfer in kraft recovery boilers, and the first section of Appendix II, The effect of temperature and residence time on the distribution of carbon, sulfur, and nitrogen between gaseous and condensed phase products from low temperature pyrolysis of kraft black liquor.

  6. Black liquor combustion validated recovery boiler modeling: Final year report. Volume 1 (Main text and Appendix I, sections 1--4)

    SciTech Connect (OSTI)

    Grace, T.M.; Frederick, W.J.; Salcudean, M.; Wessel, R.A.

    1998-08-01

    This project was initiated in October 1990, with the objective of developing and validating a new computer model of a recovery boiler furnace using a computational fluid dynamics (CFD) code specifically tailored to the requirements for solving recovery boiler flows, and using improved submodels for black liquor combustion based on continued laboratory fundamental studies. The key tasks to be accomplished were as follows: (1) Complete the development of enhanced furnace models that have the capability to accurately predict carryover, emissions behavior, dust concentrations, gas temperatures, and wall heat fluxes. (2) Validate the enhanced furnace models, so that users can have confidence in the predicted results. (3) Obtain fundamental information on aerosol formation, deposition, and hardening so as to develop the knowledge base needed to relate furnace model outputs to plugging and fouling in the convective sections of the boiler. (4) Facilitate the transfer of codes, black liquid submodels, and fundamental knowledge to the US kraft pulp industry. Volume 1 contains the main body of the report and the first 4 sections of Appendix 1: Modeling of black liquor recovery boilers -- summary report; Flow and heat transfer modeling in the upper furnace of a kraft recovery boiler; Numerical simulation of black liquor combustion; and Investigation of turbulence models and prediction of swirling flows for kraft recovery furnaces.

  7. Investigation of Fuel Chemistry and Bed Performance in a Fluidized Bed Black Liquor Steam Reformer

    SciTech Connect (OSTI)

    Kevin Whitty

    2007-06-30

    University of Utah's project entitled 'Investigation of Fuel Chemistry and Bed Performance in a Fluidized Bed Black Liquor Steam Reformer' (DOE Cooperative Agreement DE-FC26-02NT41490) was developed in response to a solicitation released by the U.S. Department of Energy in December 2001, requesting proposals for projects targeted towards black liquor/biomass gasification technology support research and development. Specifically, the solicitation was seeking projects that would provide technical support for Department of Energy supported black liquor and biomass gasification demonstration projects under development at the time.

  8. Simultaneous and rapid determination of multiple component concentrations in a Kraft liquor process stream

    DOE Patents [OSTI]

    Li, Jian; Chai, Xin Sheng; Zhu, Junyoung

    2008-06-24

    The present invention is a rapid method of determining the concentration of the major components in a chemical stream. The present invention is also a simple, low cost, device of determining the in-situ concentration of the major components in a chemical stream. In particular, the present invention provides a useful method for simultaneously determining the concentrations of sodium hydroxide, sodium sulfide and sodium carbonate in aqueous kraft pulping liquors through use of an attenuated total reflectance (ATR) tunnel flow cell or optical probe capable of producing a ultraviolet absorbency spectrum over a wavelength of 190 to 300 nm. In addition, the present invention eliminates the need for manual sampling and dilution previously required to generate analyzable samples. The inventive method can be used in Kraft pulping operations to control white liquor causticizing efficiency, sulfate reduction efficiency in green liquor, oxidation efficiency for oxidized white liquor and the active and effective alkali charge to kraft pulping operations.

  9. Controlling emissions from a black liquor fluidized bed evaporator (Copeland reactor) using a regenerative thermal oxidizer and a prefilter

    SciTech Connect (OSTI)

    Grzanka, R.

    1997-12-31

    This paper reports on an intriguing pilot project developed to control air emissions from a pulp mill. Testing is complete, and the results show favorable emissions reductions. Stone Container Corporation, REECO, NCASI, the Ohio DEP, and the US EPA, have all worked together and approved the installation of control equipment, for VOC and HAP emissions under Presumptive MACT, setting the standard for the Copeland Reactor process in a semi chem pulp mill. The equipment, once operational, will reduce VOC and CO emissions by greater than 90%. This installation will be done at one seventh the cost of the significant process modifications required to accomplish the same emission reduction. In addition, increased process operating efficiency will be achieved with the use of an energy recovery system. The process is a black liquor fluidized bed boiler, which is used to generate sodium carbonate from the black liquor. The vapor emissions were high in VOCs, CO and particulate. After much study and testing, a wet electrostatic precipitator was chosen as the filter system for particulate control, followed by a regenerative thermal oxidizer for VOC and HAP control, finally an air-to-air heat exchanger is being used to preheat the combustion air entering the process.

  10. Total Working Gas Capacity

    Gasoline and Diesel Fuel Update (EIA)

    Monthly Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Data Series Area 2009 2010 2011 2012 2013 2014 View History U.S. 4,327,844 4,410,224 4,483,650 4,576,356 4,748,636 4,785,669 2008-2014 Alaska 67,915 67,915 2013-2014 Alabama 20,900 25,150 27,350 27,350 27,350 33,150 2008-2014 Arkansas 13,898 13,898 12,036 12,178 12,178 12,178 2008-2014 California 296,096 311,096 335,396 349,296 374,296 374,296 2008-2014

  11. Mill Integration-Pulping, Stream Reforming and Direct Causticization for Black Liquor Recovery

    SciTech Connect (OSTI)

    Adriaan van Heiningen

    2007-06-30

    MTCI/StoneChem developed a steam reforming, fluidized bed gasification technology for biomass. DOE supported the demonstration of this technology for gasification of spent wood pulping liquor (or 'black liquor') at Georgia-Pacific's Big Island, Virginia mill. The present pre-commercial R&D project addressed the opportunities as well as identified negative aspects when the MTCI/StoneChem gasification technology is integrated in a pulp mill production facility. The opportunities arise because black liquor gasification produces sulfur (as H{sub 2}S) and sodium (as Na{sub 2}CO{sub 3}) in separate streams which may be used beneficially for improved pulp yield and properties. The negative aspect of kraft black liquor gasification is that the amount of Na{sub 2}CO{sub 3} which must be converted to NaOH (the so called causticizing requirement) is increased. This arises because sulfur is released as Na{sub 2}S during conventional kraft black liquor recovery, while during gasification the sodium associated Na{sub 2}S is partly or fully converted to Na{sub 2}CO{sub 3}. The causticizing requirement can be eliminated by including a TiO{sub 2} based cyclic process called direct causticization. In this process black liquor is gasified in the presence of (low sodium content) titanates which convert Na{sub 2}CO{sub 3} to (high sodium content) titanates. NaOH is formed when contacting the latter titanates with water, thereby eliminating the causticizing requirement entirely. The leached and low sodium titanates are returned to the gasification process. The project team comprised the University of Maine (UM), North Carolina State University (NCSU) and MTCI/ThermoChem. NCSU and MTCI are subcontractors to UM. The principal organization for the contract is UM. NCSU investigated the techno-economics of using advanced pulping techniques which fully utilize the unique cooking liquors produced by steam reforming of black liquor (Task 1). UM studied the kinetics and agglomeration problems of

  12. Production of ammonium sulfate fertilizer from FGD waste liquors. Quarterly technical report, October 1, 1994--December 31, 1994

    SciTech Connect (OSTI)

    Randolph, A.D.; Mukhopadhyay, S.; Unrau, E.

    1994-12-31

    During this quarterly period, an experimental investigation was performed to study the precipitation kinetics and hydrolysis characteristics of calcium imido disulfonate crystals (CaADS). The CaADS crystals were precipitated by a metathetical reaction of lime, supplied by Dravo Lime Co., with flue gas desulfurization (FGD) scrubber waste liquor. Before approaching for the continuous Double Draw-Off (DDO) crystallization studies, the influence of a Dravo lime slurry on the precipitation characteristics of N-S compounds will be established. A series of N-S compound batch crystallization studies were completed in a wide range of pH (7.0--9.0), and the influence of pH on the amount of lime required, as well as the amount of precipitate obtained, was investigated. Although the amount of precipitate increased with increase in solution pH, the safe or optimum pH for the precipitation of CaADS lies in the vicinity of 8.2 to 8.3. For studying the crystallization characteristics of CaADS crystals, a bench scale 7.0 liter DDO crystallizer was built. DDO crystallizer is found to be superior compared to Mixed Suspension Mixed Product Removal (MSMPR) crystallizer. The precipitated crystals were analyzed for elemental composition by chemical analysis. The crystals were also examined under optical microscope for their morphological features. The present studies confirmed our prediction that N-S compounds in the waste liquor can be precipitated by a reaction with lime slurry. The precipitated crystals were mostly calcium imido disulfonate.

  13. Role of vanadium(V) in the aging of the organic phase in the extraction of uranium(VI) by Alamine 336 from acidic sulfate leach liquors

    SciTech Connect (OSTI)

    Chagnes, A.; Cote, G.; Courtaud, B.; Thiry, J.

    2008-07-01

    The present work is focussed on the chemical degradation of Alamine 336-tridecanol-n-dodecane solvent which used in the recovery of uranium by solvent extraction. Degradation occurs due to the presence of vanadium(V), an oxidant, in the feed solution. After a brief overview of the chemistry of vanadium, the kinetics of degradation of the solvent when contacted with acidic sulfate leach liquor was investigated and interpreted by the Michelis-Menten mechanism. GCMS analyses evidenced the presence of tridecanoic acid and dioctylamine as degradation products. A mechanism of degradation is discussed. (authors)

  14. Burden distribution control for maintaining the central gas flow at No. 1 blast furnace in Pohang Works

    SciTech Connect (OSTI)

    Jung, S.K.; Lee, Y.J.; Suh, Y.K.; Ahn, T.J.; Kim, S.M.

    1995-12-01

    The causes for temperature lowering at the upper shaft center in Pohang No. 1 blast furnace were investigated. The test operation with charging notch change in the actual blast furnace and with a 1/12 scale model to Pohang No. 1 blast furnace were carried out in order to improve central gas flow in the shaft. Finally, rebuilding of the lower bunker interior was performed using the results of model experiments. It was confirmed that the main reason for the gas temperature lowering at the upper shaft center was the smaller particle size at center than the wall according to the discharging characteristics of center feed bunker with stone box. The central gas flow could be secured through modifying the stone box in the bunker.

  15. Black liquor combustion validated recovery boiler modeling: Final year report. Volume 3 (Appendices II, sections 2--3 and III)

    SciTech Connect (OSTI)

    Grace, T.M.; Frederick, W.J.; Salcudean, M.; Wessel, R.A.

    1998-08-01

    This project was initiated in October 1990, with the objective of developing and validating a new computer model of a recovery boiler furnace using a computational fluid dynamics (CFD) code specifically tailored to the requirements for solving recovery boiler flows, and using improved submodels for black liquor combustion based on continued laboratory fundamental studies. The key tasks to be accomplished were as follows: (1) Complete the development of enhanced furnace models that have the capability to accurately predict carryover, emissions behavior, dust concentrations, gas temperatures, and wall heat fluxes. (2) Validate the enhanced furnace models, so that users can have confidence in the predicted results. (3) Obtain fundamental information on aerosol formation, deposition, and hardening so as to develop the knowledge base needed to relate furnace model outputs to plugging and fouling in the convective sections of the boiler. (4) Facilitate the transfer of codes, black liquid submodels, and fundamental knowledge to the US kraft pulp industry. Volume 3 contains the following appendix sections: Formation and destruction of nitrogen oxides in recovery boilers; Sintering and densification of recovery boiler deposits laboratory data and a rate model; and Experimental data on rates of particulate formation during char bed burning.

  16. Other States Natural Gas Coalbed Methane, Reserves Based Production

    Gasoline and Diesel Fuel Update (EIA)

    August 2009 Revised: October 2009 Next MECS will be conducted in 2010 Table 3.5 Selected Byproducts in Fuel Consumption, 2006; Level: National and Regional Data; Row: NAICS Codes; Column: Energy Sources; Unit: Trillion Btu. Waste Blast Pulping Liquor Oils/Tars NAICS Furnace/Coke Petroleum or Wood Chips, and Waste Code(a) Subsector and Industry Total Oven Gases Waste Gas Coke Black Liquor Bark Materials Total United States 311 Food 10 0 3 0 0 7 Q 3112 Grain and Oilseed Milling 7 0 1 0 0 6 *

  17. Underwater robotic work systems for Russian arctic offshore oil/gas industry: Final report. Export trade information

    SciTech Connect (OSTI)

    1997-12-15

    The study was performed in association with Rosshelf, a shelf developing company located in Moscow. This volume involves developing an underwater robotic work system for oil exploration in Russia`s Arctic waters, Sea of Okhotsk and the Caspian Sea. The contents include: (1) Executive Summary; (2) Study Background; (3) Study Outline and Results; (4) Conclusions; (5) Separately Published Elements; (6) List of Subcontractors.

  18. Industrial Gas Turbines

    Broader source: Energy.gov [DOE]

    A gas turbine is a heat engine that uses high-temperature, high-pressure gas as the working fluid. Part of the heat supplied by the gas is converted directly into mechanical work. High-temperature,...

  19. Working Gas Capacity of Aquifers

    Gasoline and Diesel Fuel Update (EIA)

    3,274,385 3,074,251 2,818,148 3,701,510 3,585,867 3,100,594 1944-2015 Alaska 7,259 6,523 9,943 2013-2015 Lower 48 States 3,074,251 2,818,148 3,694,251 3,579,344 3,090,651 2011-2015 Alabama 16,740 15,408 23,651 22,968 28,683 29,187 1968-2015 Arkansas 4,368 4,409 2,960 3,964 3,866 2,272 1967-2015 California 203,653 242,477 170,586 268,548 235,181 204,077 1967-2015 Colorado 45,010 48,341 56,525 63,531 70,692 64,053 1967-2015 Connecticut 1973-1996 Delaware 1967-1975 Georgia 1974-1975 Illinois

  20. Stability and Regeneration of Catalysts for the Destruction of Tars from Bio-mass Black Liquor Gasification

    SciTech Connect (OSTI)

    Pradeep Agrawal

    2004-09-07

    The goal of this project was to develop catalytic materials and processes that would be effective in the destruction of tars formed during the gasification of black liquor and biomass. We report here the significant results obtained at the conclusion of this two year project.

  1. A high sensitivity fiber optic macro-bend based gas flow rate transducer for low flow rates: Theory, working principle, and static calibration

    SciTech Connect (OSTI)

    Schena, Emiliano; Saccomandi, Paola; Silvestri, Sergio

    2013-02-15

    A novel fiber optic macro-bend based gas flowmeter for low flow rates is presented. Theoretical analysis of the sensor working principle, design, and static calibration were performed. The measuring system consists of: an optical fiber, a light emitting diode (LED), a Quadrant position sensitive Detector (QD), and an analog electronic circuit for signal processing. The fiber tip undergoes a deflection in the flow, acting like a cantilever. The consequent displacement of light spot center is monitored by the QD generating four unbalanced photocurrents which are function of fiber tip position. The analog electronic circuit processes the photocurrents providing voltage signal proportional to light spot position. A circular target was placed on the fiber in order to increase the sensing surface. Sensor, tested in the measurement range up to 10 l min{sup -1}, shows a discrimination threshold of 2 l min{sup -1}, extremely low fluid dynamic resistance (0.17 Pa min l{sup -1}), and high sensitivity, also at low flow rates (i.e., 33 mV min l{sup -1} up to 4 l min{sup -1} and 98 mV min l{sup -1} from 4 l min{sup -1} up to 10 l min{sup -1}). Experimental results agree with the theoretical predictions. The high sensitivity, along with the reduced dimension and negligible pressure drop, makes the proposed transducer suitable for medical applications in neonatal ventilation.

  2. Natural Gas Weekly Update

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

    Btu per cubic foot as published in Table A4 of the Annual Energy Review 2002. Source: Energy Information Administration, Office of Oil and Gas. Storage: Working gas in storage...

  3. Natural Gas Weekly Update

    Gasoline and Diesel Fuel Update (EIA)

    Btu per cubic foot as published in Table A4 of the Annual Energy Review 2002. Source: Energy Information Administration, Office of Oil and Gas. Storage: Working gas in...

  4. Natural Gas Weekly Update

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

    Btu per cubic foot as published in Table A2 of the Annual Energy Review 2001. Source: Energy Information Administration, Office of Oil and Gas. Storage: Working gas in storage...

  5. Natural Gas Weekly Update

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

    gas in storage, as well as decreases in the price of crude oil. Wellhead Prices Annual Energy Review More Price Data Storage Working gas in storage increased to 2,905 Bcf as of...

  6. Natural Gas Weekly Update

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

    Btu per cubic foot as published in Table A2 of the Annual Energy Review 2001. Source: Energy Information Administration, Office of Oil and Gas. Storage: Working gas in...

  7. Natural Gas Weekly Update

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

    of natural gas into storage, despite robust inventories. Wellhead Prices Annual Energy Review More Price Data Storage Working gas in storage increased to 3,258 Bcf as of...

  8. Natural Gas Weekly Update

    Gasoline and Diesel Fuel Update (EIA)

    to withdraw natural gas from storage to meet current demand. Wellhead Prices Annual Energy Review More Price Data Storage Working gas in storage decreased to 2,406 Bcf as of...

  9. Natural Gas Weekly Update

    Gasoline and Diesel Fuel Update (EIA)

    Btu per cubic foot as published in Table A2 of the Annual Energy Review 2001. Source: Energy Information Administration, Office of Oil and Gas. Storage: Working gas inventories...

  10. Natural Gas Weekly Update

    Gasoline and Diesel Fuel Update (EIA)

    Working gas in storage was 3,121 Bcf as of Friday, Oct 24, 2003, according to the Energy Information Administration (EIA) Weekly Natural Gas Storage Report. This is 2.7...