Table 28. Refinery Input of Crude Oil and Petroleum Products by PAD and Refining Districts, September 1998 (Thousand Barrels, Except Where Noted) -------------------------------------------------------------------------------- PAD District I -------------------------------------------- Commodity East Appalachian Total Coast No. 1 -------------------------------------------------------------------------------- Crude Oil 43,886 2,936 46,822 Natural Gas Liquids 143 0 143 Pentanes Plus 0 0 0 LPGs 143 0 143 Ethane 0 0 0 Propane 0 0 0 Normal Butane 48 0 48 Isobutane 95 0 95 Other Liquids 8,785 45 8,830 Oth Hydrocarbons/Oxy 2,052 0 2,052 Oth Hydrocarbs/Hydrogen 0 0 0 Oxygenates W W 2,052 Fuel Ethanol W W W Methanol W W W MTBE W W 2,005 Other Oxygenates(a) W W W Unfinished Oils (net) 4,288 53 4,341 Mogas Blend. Comp.(net) 2,445 -8 2,437 Avgas Blend. Comp.(net) 0 0 0 Total Input to Refineries 52,814 2,981 55,795 Atmos Crude Distillation Gross Input (d) 1,436 98 1,534 Operable Capacity (d) 1,547 98 1,645 Oper Util Rate(%)(b) 92.8 100.3 93.2 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 659 20 679 Catalytic Hydrocracking 54 0 54 Delayed & Fluid Coking 82 0 82 Crude Oil Qualities Sulfur Content,(%)(e) 1.04 1.18 1.05 API Gravity,(degrees)(e) 33.27 34.02 33.32 Operable Capacity (d) 1,547 98 1,645 Operating 1,467 98 1,565 Idle 80 0 80 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 66,064 11,225 20,732 98,021 Natural Gas Liquids 661 185 1,081 1,927 Pentanes Plus 74 125 634 833 LPGs 587 60 447 1,094 Ethane 0 0 0 0 Propane 0 0 0 0 Normal Butane 211 39 227 477 Isobutane 376 21 220 617 Other Liquids 3,360 508 -1,014 2,854 Oth Hydrocarbons/Oxy 829 261 76 1,166 Oth Hydrocarbs/Hydrogen 32 0 31 63 Oxygenates 797 261 45 1,103 Fuel Ethanol W W W 991 Methanol W W W W MTBE W W W W Other Oxygenates(a) W W W W Unfinished Oils (net) 3,330 -50 -900 2,380 Mogas Blend. Comp.(net) -787 297 -190 -680 Avgas Blend. Comp.(net) -12 0 0 -12 Total Input to Refineries 70,085 11,918 20,799 102,802 Atmos Crude Distillation Gross Input (d) 2,251 376 695 3,322 Operable Capacity (d) 2,410 414 701 3,525 Oper Util Rate(%)(b) 93.4 90.8 99.1 94.2 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 758 121 204 1,083 Catalytic Hydrocracking 145 0 4 149 Delayed & Fluid Coking 171 43 80 294 Crude Oil Qualities Sulfur Content,(%)(e) 1.18 2.20 0.70 1.19 API Gravity,(degrees)(e) 33.12 28.97 34.53 32.94 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 0 0 0 0 -------------------------------------------------------------------------------- PAD District III ------------------------------------------------------ Texas La. Commodity Texas Gulf Gulf N.La., New Inland Coast Coast Ark. Mexico Total -------------------------------------------------------------------------------- Crude Oil 17,935 99,533 79,927 5,496 2,844 205,735 Natural Gas Liquids 1,006 2,879 1,785 193 242 6,105 Pentanes Plus 488 1,191 273 157 126 2,235 LPGs 518 1,688 1,512 36 116 3,870 Ethane 0 0 0 0 0 0 Propane 0 0 0 0 0 0 Normal Butane 421 634 725 9 0 1,789 Isobutane 97 1,054 787 27 116 2,081 Other Liquids -85 6,819 3,589 -18 9 10,314 Oth Hydrocarbons/Oxy 139 2,214 720 1 22 3,096 Oth Hydrocarbs/Hydrogen 125 355 425 0 0 905 Oxygenates 14 1,859 295 W W 2,191 Fuel Ethanol W W W W W W Methanol W W W W W W MTBE W 1,764 W W W 2,034 Other Oxygenates(a) W W W W W W Unfinished Oils (net) 356 6,685 2,054 -12 39 9,122 Mogas Blend. Comp.(net) -575 -2,080 807 -7 -52 -1,907 Avgas Blend. Comp.(net) -5 0 8 0 0 3 Total Input to Refinerie 18,856 109,231 85,301 5,671 3,095 222,154 Atmos Crude Distillation Gross Input (d) 599 3,296 2,687 175 95 6,852 Operable Capacity (d) 591 3,490 2,854 201 95 7,230 Oper Util Rate(%)(b) 101.3 94.4 94.2 87.1 100.2 94.8 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 202 1,357 902 28 31 2,520 Catalytic Hydrocrackin 59 267 196 0 0 522 Delayed & Fluid Coking 5 391 396 9 0 800 Crude Oil Qualities Sulfur Content,(%)(e) 0.79 1.56 1.47 1.70 0.51 1.45 API Gravity,(degrees)(e) 38.17 31.20 31.40 30.84 38.68 31.98 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 15,151 79,877 445,606 Natural Gas Liquids 475 2,210 10,860 Pentanes Plus 259 897 4,224 LPGs 216 1,313 6,636 Ethane 0 0 0 Propane 0 0 0 Normal Butane 135 799 3,248 Isobutane 81 514 3,388 Other Liquids -33 4,948 26,913 Oth Hydrocarbons/Oxy 61 4,165 10,540 Oth Hydrocarbs/Hydrogen 1 855 1,824 Oxygenates 60 3,310 8,716 Fuel Ethanol W W 1,032 Methanol W W 52 MTBE W 3,239 7,395 Other Oxygenates(a) W W 237 Unfinished Oils (net) 75 252 16,170 Mogas Blend. Comp.(net) -169 541 222 Avgas Blend. Comp.(net) 0 -10 -19 Total Input to Refineries 15,593 87,035 483,379 Atmos Crude Distillation Gross Input (d) 512 2,821 15,041 Operable Capacity (d) 524 2,907 15,832 Oper Util Rate(%)(b) 97.8 97.0 95.0 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 160 748 5,189 Catalytic Hydrocracking 4 423 1,152 Delayed & Fluid Coking 35 521 1,731 Crude Oil Qualities Sulfur Content,(%)(e) 1.36 1.19 1.30 API Gravity,(degrees)(e) 33.44 25.19 31.14 Operable Capacity (d) 524 2,907 15,832 Operating 524 2,886 15,703 Idle 0 22 129 Alaskan Crude Oil Receipts 0 36,084 36,084 -------------------------------------------------------------------------------- (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.