Table 28. Refinery Input of Crude Oil and Petroleum Products by PAD and Refining Districts, Jun 2004 (Thousand Barrels, Except Where Noted) -------------------------------------------------------------------------------- PAD District I -------------------------------------------- Commodity East Appalachian Total Coast No. 1 -------------------------------------------------------------------------------- Crude Oil 47,263 2,823 50,086 Natural Gas Liquids 81 0 81 Pentanes Plus 0 0 0 LPGs 81 0 81 Ethane 0 0 0 Propane 0 0 0 Normal Butane 1 0 1 Isobutane 80 0 80 Other Liquids 12,687 131 12,818 Oth Hydrocarbons/Oxy 2,728 111 2,839 Oth Hydrocarbs/Hydrogen 0 0 0 Oxygenates W W 2,839 Fuel Ethanol W W W Methanol W W W MTBE W W 1,727 Other Oxygenates(a) W W W Unfinished Oils (net) 2,537 17 2,554 Mogas Blend. Comp.(net) 7,607 3 7,610 Avgas Blend. Comp.(net) -185 0 -185 Total Input to Refineries 60,031 2,954 62,985 Atmos Crude Distillation Gross Input (d) 1,545 94 1,639 Operable Capacity (d) 1,642 94 1,736 Oper Util Rate(%)(b) 94.1 99.7 94.4 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 672 22 694 Catalytic Hydrocracking 36 0 36 Delayed & Fluid Coking 80 0 80 Crude Oil Qualities Sulfur Content,(%)(e) 0.95 1.39 0.98 API Gravity,(degrees)(e) 31.19 31.74 31.22 Operable Capacity (d) 1,642 94 1,736 Operating 1,642 94 1,736 Idle 0 0 0 Alaskan Crude Oil Receipts 0 0 0 -------------------------------------------------------------------------------- PAD District II ------------------------------------------------- Commodity Ind., Minn.,Wis., Okla., Ill.,Ky. N.Dak.,S.Dak Kans.,Mo. Total -------------------------------------------------------------------------------- Crude Oil 68,297 12,961 23,206 104,464 Natural Gas Liquids 1,039 227 951 2,217 Pentanes Plus 437 169 734 1,340 LPGs 602 58 217 877 Ethane 0 0 0 0 Propane 0 0 0 0 Normal Butane 64 2 0 66 Isobutane 538 56 217 811 Other Liquids 1,188 -1,165 889 912 Oth Hydrocarbons/Oxy 1,917 653 427 2,997 Oth Hydrocarbs/Hydrogen 87 48 102 237 Oxygenates 1,830 605 325 2,760 Fuel Ethanol W W W 2,760 Methanol W W W W MTBE W W W W Other Oxygenates(a) W W W W Unfinished Oils (net) 2,896 377 -622 2,651 Mogas Blend. Comp.(net) -3,630 -2,195 1,084 -4,741 Avgas Blend. Comp.(net) 5 0 0 5 Total Input to Refineries 70,524 12,023 25,046 107,593 Atmos Crude Distillation Gross Input (d) 1,907 433 777 3,116 Operable Capacity (d) 2,327 426 773 3,526 Oper Util Rate(%)(b) 81.9 101.6 100.5 88.4 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 839 145 218 1,202 Catalytic Hydrocracking 133 0 6 140 Delayed & Fluid Coking 181 62 94 337 Crude Oil Qualities Sulfur Content,(%)(e) 1.29 2.30 0.85 1.32 API Gravity,(degrees)(e) 32.14 26.70 35.42 32.20 Operable Capacity (d) 2,327 426 773 3,526 Operating 2,327 426 773 3,526 Idle 0 0 0 0 Alaskan Crude Oil Receipts 0 0 0 0 -------------------------------------------------------------------------------- PAD District III ------------------------------------------------------ Texas La. Commodity Texas Gulf Gulf N.La., New Inland Coast Coast Ark. Mexico Total -------------------------------------------------------------------------------- Crude Oil 18,864 114,218 93,863 4,737 2,963 234,645 Natural Gas Liquids 984 3,137 1,932 95 231 6,379 Pentanes Plus 536 1,423 1,155 47 111 3,272 LPGs 448 1,714 777 48 120 3,107 Ethane 0 0 0 0 0 0 Propane 0 0 0 0 0 0 Normal Butane 284 200 133 0 0 617 Isobutane 164 1,514 644 48 120 2,490 Other Liquids -273 5,827 -339 -45 -494 4,676 Oth Hydrocarbons/Oxy 212 2,740 975 0 16 3,943 Oth Hydrocarbs/Hydrogen 189 550 520 0 0 1,259 Oxygenates 23 2,190 455 W W 2,684 Fuel Ethanol W W W W W W Methanol W W W W W W MTBE W 2,116 W W W 2,580 Other Oxygenates(a) W W W W W W Unfinished Oils (net) -417 6,944 5 -45 91 6,578 Mogas Blend. Comp.(net) -71 -3,857 -1,318 0 -601 -5,847 Avgas Blend. Comp.(net) 3 0 -1 0 0 2 Total Input to Refinerie 19,575 123,182 95,456 4,787 2,700 245,700 Atmos Crude Distillation Gross Input (d) 634 3,778 3,192 146 99 7,849 Operable Capacity (d) 615 3,854 3,121 211 96 7,895 Oper Util Rate(%)(b) 103.1 98.0 102.3 69.2 103.3 99.4 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 209 1,507 1,028 19 30 2,793 Catalytic Hydrocrackin 69 269 249 0 0 587 Delayed & Fluid Coking 5 638 483 12 0 1,138 Crude Oil Qualities Sulfur Content,(%)(e) 0.90 1.83 1.55 1.79 0.59 1.62 API Gravity,(degrees)(e) 36.52 28.15 29.59 29.17 40.01 29.58 Operable Capacity (d) 615 3,854 3,121 211 96 7,895 Operating 615 3,854 3,121 211 96 7,895 Idle 0 0 0 0 0 0 Alaskan Crude Oil Receipts 0 0 0 0 0 0 -------------------------------------------------------------------------------- PAD Dist. IV PAD Dist. V Commodity -------------- --------------- U.S. Rocky Mt. West Coast Total -------------------------------------------------------------------------------- Crude Oil 17,081 81,041 487,317 Natural Gas Liquids 442 1,539 10,658 Pentanes Plus 182 644 5,438 LPGs 260 895 5,220 Ethane 0 0 0 Propane 0 0 0 Normal Butane 101 553 1,338 Isobutane 159 342 3,882 Other Liquids 815 2,398 21,619 Oth Hydrocarbons/Oxy 115 2,739 12,633 Oth Hydrocarbs/Hydrogen 26 888 2,410 Oxygenates 89 1,851 10,223 Fuel Ethanol 89 1,851 5,838 Methanol W W 0 MTBE W 0 4,307 Other Oxygenates(a) W W 78 Unfinished Oils (net) 396 -130 12,049 Mogas Blend. Comp.(net) 304 -211 -2,885 Avgas Blend. Comp.(net) 0 0 -178 Total Input to Refineries 18,338 84,978 519,594 Atmos Crude Distillation Gross Input (d) 574 2,879 16,057 Operable Capacity (d) 582 3,163 16,902 Oper Util Rate(%)(b) 98.6 91.0 95.0 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 162 784 5,635 Catalytic Hydrocracking 14 509 1,286 Delayed & Fluid Coking 43 509 2,106 Crude Oil Qualities Sulfur Content,(%)(e) 1.36 1.24 1.42 API Gravity,(degrees)(e) 31.89 27.61 30.05 Operable Capacity (d) 582 3,163 16,902 Operating 581 3,107 16,845 Idle 1 57 57 Alaskan Crude Oil Receipts 0 29,976 29,976 -------------------------------------------------------------------------------- (a) Includes ethyl tertiary butyl ether(ETBE), tertiary amyl methyl ether (TAME), tertiary butyl alcohol(TBA), and other aliphatic alcohols and ethers intended for motor gasoline blending(e.g., isopropyl ether(IPE) or n-propanol). (b) Represents gross input divided by operable capacity. (d) Daily Average. (e) Weighted Average. W = Withheld to avoid disclosure of individual company data. LPG = Liquefied Petroleum Gases. Oxy = Oxygenates. Atmos = Atmospheric. Note: Totals may not equal sum of components due to independent rounding. Sources: Energy Information Administration (EIA) Form EIA-810, "Monthly Refinery Report." ------------ For additional information, please contact the Energy Information Administration's National Energy Information Center at (202)586-8800.