Table 28. Refinery Input of Crude Oil and Petroleum Products by PAD and Refining Districts, June 1998 (Thousand Barrels, Except Where Noted) -------------------------------------------------------------------------------- PAD District I -------------------------------------------- Commodity East Appalachian Total Coast No. 1 -------------------------------------------------------------------------------- Crude Oil 45,935 2,971 48,906 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 10,451 97 10,548 Oth Hydrocarbons/Oxy 2,231 0 2,231 Oth Hydrocarbs/Hydrogen 0 0 0 Oxygenates W W 2,231 Fuel Ethanol W W W Methanol W W W MTBE W W 2,155 Other Oxygenates(a) W W W Unfinished Oils (net) 2,046 96 2,142 Mogas Blend. Comp.(net) 6,248 1 6,249 Avgas Blend. Comp.(net) -74 0 -74 Total Input to Refineries 56,467 3,068 59,535 Atmos Crude Distillation Gross Input (d) 1,515 99 1,614 Operable Capacity (d) 1,547 98 1,645 Oper Util Rate(%)(b) 97.9 101.3 98.1 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 613 21 634 Catalytic Hydrocracking 62 0 62 Delayed & Fluid Coking 79 0 79 Crude Oil Qualities Sulfur Content,(%)(e) 0.93 1.00 0.93 API Gravity,(degrees)(e) 33.42 34.33 33.47 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 68,319 12,942 22,115 103,376 Natural Gas Liquids 967 145 1,204 2,316 Pentanes Plus 160 85 813 1,058 LPGs 807 60 391 1,258 Ethane 0 0 0 0 Propane 0 0 0 0 Normal Butane 176 0 75 251 Isobutane 631 60 316 1,007 Other Liquids 599 781 -431 949 Oth Hydrocarbons/Oxy 870 277 109 1,256 Oth Hydrocarbs/Hydrogen 24 0 34 58 Oxygenates 846 277 75 1,198 Fuel Ethanol W W W 1,029 Methanol W W W W MTBE W W W W Other Oxygenates(a) W W W W Unfinished Oils (net) 1,290 -112 -848 330 Mogas Blend. Comp.(net) -1,554 616 308 -630 Avgas Blend. Comp.(net) -7 0 0 -7 Total Input to Refineries 69,885 13,868 22,888 106,641 Atmos Crude Distillation Gross Input (d) 2,365 432 743 3,540 Operable Capacity (d) 2,404 414 701 3,519 Oper Util Rate(%)(b) 98.4 104.3 105.9 100.6 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 773 141 207 1,121 Catalytic Hydrocracking 134 0 4 138 Delayed & Fluid Coking 194 63 83 340 Crude Oil Qualities Sulfur Content,(%)(e) 1.21 2.22 0.80 1.25 API Gravity,(degrees)(e) 33.03 28.58 34.91 32.89 Operable Capacity (d) 2,404 414 701 3,519 Operating 2,404 414 701 3,519 Idle 0 0 0 0 Alaskan Crude Oil Receipts 160 0 0 160 -------------------------------------------------------------------------------- PAD District III ------------------------------------------------------ Texas La. Commodity Texas Gulf Gulf N.La., New Inland Coast Coast Ark. Mexico Total -------------------------------------------------------------------------------- Crude Oil 18,153 108,043 82,223 5,506 2,861 216,786 Natural Gas Liquids 1,069 2,684 1,529 216 253 5,751 Pentanes Plus 577 1,353 312 186 129 2,557 LPGs 492 1,331 1,217 30 124 3,194 Ethane 0 0 0 0 0 0 Propane 0 0 0 0 0 0 Normal Butane 410 298 360 0 0 1,068 Isobutane 82 1,033 857 30 124 2,126 Other Liquids -70 6,830 3,995 -87 -227 10,441 Oth Hydrocarbons/Oxy 146 2,253 988 0 29 3,416 Oth Hydrocarbs/Hydrogen 138 449 438 0 0 1,025 Oxygenates 8 1,804 550 W W 2,391 Fuel Ethanol W W W W W W Methanol W W W W W W MTBE W 1,701 W W W 2,175 Other Oxygenates(a) W W W W W W Unfinished Oils (net) 247 5,645 3,519 -47 89 9,453 Mogas Blend. Comp.(net) -467 -1,068 -515 -40 -345 -2,435 Avgas Blend. Comp.(net) 4 0 3 0 0 7 Total Input to Refinerie 19,152 117,557 87,747 5,635 2,887 232,978 Atmos Crude Distillation Gross Input (d) 608 3,587 2,787 176 95 7,252 Operable Capacity (d) 589 3,494 2,851 201 95 7,229 Oper Util Rate(%)(b) 103.2 102.6 97.7 87.7 100.8 100.3 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 198 1,400 961 30 32 2,620 Catalytic Hydrocrackin 52 277 282 0 0 611 Delayed & Fluid Coking 5 428 380 8 0 821 Crude Oil Qualities Sulfur Content,(%)(e) 0.84 1.63 1.51 1.75 0.53 1.51 API Gravity,(degrees)(e) 37.99 30.34 29.26 30.62 38.76 30.68 Operable Capacity (d) 589 3,494 2,851 201 95 7,229 Operating 589 3,461 2,851 201 95 7,196 Idle 0 33 0 0 0 33 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 15,234 76,740 461,042 Natural Gas Liquids 354 2,363 10,865 Pentanes Plus 96 1,083 4,794 LPGs 258 1,280 6,071 Ethane 0 0 0 Propane 0 0 0 Normal Butane 136 729 2,185 Isobutane 122 551 3,886 Other Liquids 527 6,268 28,733 Oth Hydrocarbons/Oxy 49 4,063 11,015 Oth Hydrocarbs/Hydrogen 6 791 1,880 Oxygenates 43 3,272 9,135 Fuel Ethanol W W 1,069 Methanol W W 44 MTBE W 3,146 7,643 Other Oxygenates(a) W W 379 Unfinished Oils (net) 91 1,496 13,512 Mogas Blend. Comp.(net) 387 707 4,278 Avgas Blend. Comp.(net) 0 2 -72 Total Input to Refineries 16,115 85,371 500,640 Atmos Crude Distillation Gross Input (d) 516 2,729 15,651 Operable Capacity (d) 521 2,907 15,822 Oper Util Rate(%)(b) 99.0 93.9 98.9 Downstream Processing Fresh Feed Input (d) Catalytic Cracking 161 728 5,265 Catalytic Hydrocracking 4 470 1,285 Delayed & Fluid Coking 44 513 1,797 Crude Oil Qualities Sulfur Content,(%)(e) 1.40 1.18 1.33 API Gravity,(degrees)(e) 33.06 23.99 30.40 Operable Capacity (d) 521 2,907 15,822 Operating 521 2,886 15,687 Idle 0 22 135 Alaskan Crude Oil Receipts 0 34,593 34,753 -------------------------------------------------------------------------------- (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.