Table 28. Refinery Input of Crude Oil and Petroleum Products by PAD and Refining Districts, August 1998 (Thousand Barrels, Except Where Noted) -------------------------------------------------------------------------------- PAD District I -------------------------------------------- Commodity East Appalachian Total Coast No. 1 -------------------------------------------------------------------------------- Crude Oil 47,714 3,012 50,726 Natural Gas Liquids 31 0 31 Pentanes Plus 0 0 0 LPGs 31 0 31 Ethane 0 0 0 Propane 0 0 0 Normal Butane 10 0 10 Isobutane 21 0 21 Other Liquids 11,123 -11 11,112 Oth Hydrocarbons/Oxy 2,136 0 2,136 Oth Hydrocarbs/Hydrogen 0 0 0 Oxygenates W W 2,136 Fuel Ethanol W W W Methanol W W W MTBE W W 2,060 Other Oxygenates(a) W W W Unfinished Oils (net) 3,085 -7 3,078 Mogas Blend. Comp.(net) 5,980 -4 5,976 Avgas Blend. Comp.(net) -78 0 -78 Total Input to Refineries 58,868 3,001 61,869 Atmos Crude Distillation Gross Input (d) 1,497 97 1,594 Operable Capacity (d) 1,547 98 1,645 Oper Util Rate(%)(b) 96.7 99.5 96.9 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 630 22 653 Catalytic Hydrocracking 55 0 55 Delayed & Fluid Coking 86 0 86 Crude Oil Qualities Sulfur Content,(%)(e) 1.01 1.11 1.01 API Gravity,(degrees)(e) 32.85 34.17 32.93 Operable Capacity (d) 1,547 98 1,645 Operating 1,453 98 1,551 Idle 94 0 94 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 72,067 13,869 20,561 106,497 Natural Gas Liquids 992 191 1,056 2,239 Pentanes Plus 133 122 558 813 LPGs 859 69 498 1,426 Ethane 0 0 0 0 Propane 0 0 0 0 Normal Butane 191 0 162 353 Isobutane 668 69 336 1,073 Other Liquids 1,477 819 -429 1,867 Oth Hydrocarbons/Oxy 892 234 88 1,214 Oth Hydrocarbs/Hydrogen 25 0 16 41 Oxygenates 867 234 72 1,173 Fuel Ethanol W W W 1,016 Methanol W W W W MTBE W W W W Other Oxygenates(a) W W W W Unfinished Oils (net) 2,820 29 -524 2,325 Mogas Blend. Comp.(net) -2,216 556 7 -1,653 Avgas Blend. Comp.(net) -19 0 0 -19 Total Input to Refineries 74,536 14,879 21,188 110,603 Atmos Crude Distillation Gross Input (d) 2,427 447 665 3,540 Operable Capacity (d) 2,410 414 701 3,525 Oper Util Rate(%)(b) 100.7 108.1 94.9 100.4 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 830 137 187 1,154 Catalytic Hydrocracking 141 0 4 145 Delayed & Fluid Coking 189 50 83 322 Crude Oil Qualities Sulfur Content,(%)(e) 1.14 2.07 0.75 1.18 API Gravity,(degrees)(e) 33.19 28.98 34.93 32.98 Operable Capacity (d) 2,410 414 701 3,525 Operating 2,410 414 701 3,525 Idle 0 0 0 0 Alaskan Crude Oil Receipts 92 0 0 92 -------------------------------------------------------------------------------- PAD District III ------------------------------------------------------ Texas La. Commodity Texas Gulf Gulf N.La., New Inland Coast Coast Ark. Mexico Total -------------------------------------------------------------------------------- Crude Oil 19,080 112,319 91,015 5,817 2,883 231,114 Natural Gas Liquids 1,078 2,560 1,371 206 254 5,469 Pentanes Plus 566 976 299 176 133 2,150 LPGs 512 1,584 1,072 30 121 3,319 Ethane 0 0 0 0 0 0 Propane 0 0 0 0 0 0 Normal Butane 427 294 331 0 0 1,052 Isobutane 85 1,290 741 30 121 2,267 Other Liquids 5 6,038 1,524 -255 -205 7,107 Oth Hydrocarbons/Oxy 142 2,266 959 1 23 3,391 Oth Hydrocarbs/Hydrogen 142 336 497 0 0 975 Oxygenates 0 1,930 462 W W 2,416 Fuel Ethanol W W W W W W Methanol W W W W W W MTBE W 1,837 W W W 2,270 Other Oxygenates(a) W W W W W W Unfinished Oils (net) 139 5,406 1,311 -216 138 6,778 Mogas Blend. Comp.(net) -277 -1,634 -741 -40 -366 -3,058 Avgas Blend. Comp.(net) 1 0 -5 0 0 -4 Total Input to Refinerie 20,163 120,917 93,910 5,768 2,932 243,690 Atmos Crude Distillation Gross Input (d) 617 3,564 2,931 176 93 7,380 Operable Capacity (d) 591 3,490 2,854 201 95 7,230 Oper Util Rate(%)(b) 104.3 102.1 102.7 87.7 98.3 102.1 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 200 1,398 973 27 31 2,629 Catalytic Hydrocrackin 58 239 252 0 0 550 Delayed & Fluid Coking 5 433 437 12 0 887 Crude Oil Qualities Sulfur Content,(%)(e) 0.80 1.54 1.43 1.76 0.52 1.43 API Gravity,(degrees)(e) 37.85 31.57 31.34 30.66 38.62 32.06 Operable Capacity (d) 591 3,490 2,854 201 95 7,230 Operating 591 3,463 2,854 201 95 7,203 Idle 0 27 0 0 0 27 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 15,695 81,436 485,468 Natural Gas Liquids 479 2,060 10,278 Pentanes Plus 226 932 4,121 LPGs 253 1,128 6,157 Ethane 0 0 0 Propane 0 0 0 Normal Butane 111 674 2,200 Isobutane 142 454 3,957 Other Liquids 128 5,149 25,363 Oth Hydrocarbons/Oxy 51 4,178 10,970 Oth Hydrocarbs/Hydrogen 3 986 2,005 Oxygenates 48 3,192 8,965 Fuel Ethanol W W 1,047 Methanol W W 65 MTBE W 3,136 7,617 Other Oxygenates(a) W W 236 Unfinished Oils (net) -18 982 13,145 Mogas Blend. Comp.(net) 95 -11 1,349 Avgas Blend. Comp.(net) 0 0 -101 Total Input to Refineries 16,302 88,645 521,109 Atmos Crude Distillation Gross Input (d) 518 2,775 15,806 Operable Capacity (d) 524 2,907 15,832 Oper Util Rate(%)(b) 98.8 95.4 99.8 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 154 757 5,347 Catalytic Hydrocracking 4 470 1,223 Delayed & Fluid Coking 38 492 1,824 Crude Oil Qualities Sulfur Content,(%)(e) 1.41 1.22 1.30 API Gravity,(degrees)(e) 32.13 25.24 31.17 Operable Capacity (d) 524 2,907 15,832 Operating 524 2,886 15,689 Idle 0 22 143 Alaskan Crude Oil Receipts 0 37,354 37,446 -------------------------------------------------------------------------------- (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.