P.1 

OAR Box 1116 

Prepped by Ryan Dugan 

Document Number: 

102)11-1-30 

Docket Number: 

A-84-44 

Printed 4/14/2008 8:35:59 AM Sheet 102 of 123 
P.2 

4-84-W 

NATIONAL PETROLEUM REFINERS ASSOCIATION 

Founded 1902 

SUITE 1000, 1899 L STREET, N.W.. WASHINGTON. D.C. 20036 

TELEPHONE (202 ) 457-0480 

July 1, 1985 

U.S. Refining Capacity 

The attached summary of petroleum refineries in the United States and 

U.S. territories is taken from the Department of Energy's Petroleum Supply 

Annual. 

On January 1, 1985, there were 219* operable refineries in the United 

States with total crude oil distillation capacity of 15.7 million barrels per 

calendar day and 16.5 million barrels per stream day. There were 195* 

refineries operating on January 1, with operating capacity listed at 14.4 

million barrels per calendar day and 15.1 million barrels per stream day. The 

OOE Energy Information Administration reports 26 refineries, with a total crude 

distillation capacity of 0.6 million barrels per calendar day, were shut down 

during 1984 and 2 refineries were started up. Since January 1, 1981, a net 

total of U O refineries have been shut down with a total capacity of 2.5 

million barrels per calendar day. 

This chart represents operable U.S. refining capacity for the past 

five years: 

January Operable Capacity in Thousands of Barrels Per Calendar Day 

1981 1982 1983 1984 1985 

U.S. Capacity 

Puerto Rico 

Virgin Islands and Guam 

Hawaiian Foreign Trade Zone 

8,051 

228 

714 

68 

17,890 

255 

744 

68 

16,859 

244 

559 

60 

16,137 

121 

558 

60 

15,659 

121 

588 

62 

* This number does not include installations that do not have crude 

distillation capacity. The Energy Information Administration, however, defines 

"petroleum refinery" as "an installation that manufactures finished petroleum 

products from crude oil, unfinished oils, natural gas plant liquids, other 

hydrocarbons, and alcohol." EIA's definition does include installations having 

no crude distillation capacity. The EIA therefore counts 223 operable and 199 

operating refineries in the United States. EIA also includes data from 29 

gasoline blending plants in the tables on Input/Production of Petroleum 

Products, Working Storage Capacity, and Shell Storage Capacity (Tables 5, 6, 

and 7). These blenders are listed on page 51. 
CONTENTS 

Pages 

U. S. Refining Capacity: 1985 (EIA Summary) iii 

Operating U. S. Refineries (1970 - 1985) vi 

Table 1. Number and Capacity of Operable Petroleum Refineries by PAD District 

and State 1 

Table 2. Production Capacity of Operable Petroleum Refineries by PAD District 

and State 3 

Table 3. Capacity of Operable Petroleum Refineries by State 5 

Companies in Guam, Puerto Rico, Hawaiian Foreign Trade Zone 

and Virgin Islands 18 

Table 4. Refiners' Operable Crude Oil Distillation Capacity 19 

Companies with a Capacity More than 100,000 B/CD 

(30 companies; 118 refineries) 19-2 1 

Companies with a Capacity 30,001 to 100,000 B/CD 

(24 companies; 31 refineries) 21-2 2 

Companies with a Capacity 10,001 to 30,000 B/CD 

(25 companies; 33 refineries) 22-2 3 

Companies with a Capacity 10,000 B/CD or Less 

(35 companies; 37 refineries) 23-2 4 

Table 5. Input/Production of Petroleum Products at Refineries and Blending Plants 

by PAD District 25 

Table 6. Working Storage Capacity at Refineries and Gasoline Blending Plants by 

PAD District and State 26 

Table 7. Shell Storage Capacity at Refineries and Gasoline Blending Plants by 

PAD District and State 27 

Table 8. Operable Capacity of Petroleum Refineries 28 
Table 9. Refinery Crude Oil Distillation Capacity and Utilization by PAD District, 

by month 29 

Table 10. Refineries Shutdown During 1984 30 

Table 11. New and Reactivated Refineries during 1984 31 

Table 12. Refineries Shutdown Since January 1, 1981 32 

Table 13. Refinery Sales Since 1981 35 

Table 14. Refinery Receipts of Crude Oil by Method of Transportation 

by PAD District 38 

Table 15. Fuels Consumed at Refineries by PAD District 38 

Explanatory Notes 40 

Definitions of Petroleum Products and Other Terms 52 
P.5 

U.S. Refining Capacity: 1985 

Introduction 

This chapter presents the results of the Energy Information Administration's 1985 annual refinery survey 

(Form EIA-820, "Annual Refinery Report"). Statistics 

reflect capacities as of January 1,1985, and operations 

during 1984. Projections are based on the expectations 

of survey respondents and may not be consistent with 

the forecasts of the Energy Information Administration. 

Number of Operable Refineries 

On January 1,1985, there were 223 operable petroleum 

refineries in the United States1 reporting a combined 

operable crude distillation capacity of 15.7 million barrels per calendar day, (16.5 million barrels per stream 

day2). Compared to January 1, 1984, crude distillation 

capacity fell 0.5 million barrels per calendar day and (0.6 

million barrels per stream day). 

Refiners continued to respond to slowdowns in 

product demand, shifts in product mix and changes in 

crude oil quality by reducing capacity through plant 

closings and down-sizing capacity. During 1984, 26 

closings and 2 start-ups resulted in a net decrease of 24 

plants with an associated loss in crude distillation 

capacity of 0.5 million barrels per calendar day. The 

majority of these closings occurred at refineries with 

crude distillation capacity of 30,000 barrels per calendar day or less. These closings accounted for a net reduction of 19 facilities. Refineries with crude distillation capacity greater than 30,000 barrels per calendar 

day showed a net reduction of 5 during 1984 (see Table 

B1). 

dar day was idle on January 1,1985. Slightly more than 

half of this capacity, 0.7 million barrels per calendar 

day, was at facilities partially in operation, while the 

remaining 0.6 million barrels per calendar day was at 24 

completely idle refineries. Idle refineries are capable of 

being restarted within 30 days, or under active repairs 

that could be completed within 90 days. Although fewer 

plants were completely idle as of January 1,1985, compared to the same date last year, their combined crude 

distillation capacity exceeded the previous year's level 

by 0.1 million barrels per calendar day. -

Since January 1, 1981, crude distillation capacity has 

declined nearly 3.0 million barrels per calendar day (3.3 

million barrels per stream day). Respondents to the 

Energy Information Administration's annual refinery 

survey project that crude distillation capacity will decrease by about 100,000 barrels per day between January 1, 1985 and January 1, 1986. Refinery utilization 

peaked at 78.2 percent in August 1984; the average rate 

for the year rose to 76.2 percent, from the previous 

year's average of 71.7 percent. 

Downstream Capacity 

Total downstream charge capacity on January 1, 1985 

stood at 28.3 million barrels per stream day, a net decrease of 0.4 million barrels per stream day. New construction at existing refineries and the start-up of previously closed refineries was more than offset by the 

nearly 0.7 million barrels per stream day capacity 

closed during 1984. The most significant declines were 

in vacuum distillation and catalytic reforming, dropping 

2 percent and 4 percent, respectively. However, during 

Crude Distillation Capacity 

Of the 15.7 million barrels per calendar day of operable 

crude distillation capacity, 1.3 million barrels percalen-

'The 50 United States and District of Columbia excluding U.S. 

territories and possessions. 

2See definitions for explanation of "calendar day" and "stream 

day". 

Table B1. Number of Operable Refineries, by size, from January 1,1981 to 1985 

Crude Distillation Capacity 

(Barrels per Calendar Day) 

Years 

1985 

56 

43 

38 

39 

25 

22 

223 

1984 

63 

55 

41 

41 

26 

21 

247 

1983 

67 

59 

40 

44 

26 

22 

258 

1982 

82 

80 

44 

43 

30 

22 

301 

1981 

91 

93 

42 

44 

27 

27 

324 

Less than 10,000 

10,001-30,000 

30,001-50,000 

50,001-100,000 

100,001-175,000 

Over 175,000 

Total 

Source: Form EIA-820. 

I l l 

Potroloum 9upplr Annuml 1994, Volumo I I Knorgy Mormotion Admlnl&trmtlon 
i 

I 

! 

e 

« 

I 

I 

5" 

s 

Figure 1. Simplied Flow Diagram of A Typical U.S. Refjnery 

UNSTABILIZEOCAS 

CRUOE 

UNIT 

ATMOSPHERIC 

DISTILLATION 

KEROSENE ANO DIESEL RANGE 

MIDDLE DISTILLATES 

ATMOSPHERIC 

CRUOE 

OIL 

VACUUM 

DISTILLATION 

UNIT 

CUTTER 

STOCK 

COKER 

NAPHTHA 

I . . FUEL 

~W GAS 

SATURATE 

GAS 

RECOVERV 

- ^ LPG'S 

NBUTAN E ISOMERIZATION 

LIGHT STRAIGHT 

R U N GASOLINE 

REFORMER GAS 

NAPHTHA 

DESULFURIZER 

CATALYTIC 

REFORMER REFORMATE 

UNSAT 

URATEO 

GAS 

COKER 

CYCLE 

Oil 

THERMAL 

OPERATIONS 

LIGHT 

CYCLE 

OIL 

CATALYTIC 

CRACKING 

AND 

UNSATURATE 

GAS 

RECOVERY 

GAS OIL 

DISTILLATE 

HYOROTREATING 

ANO 

BLENDING 

UNSAT 

GAS 

• ALKYLATION 

UNIT 

3 

CRACKEO GASOLINE 

GASOLINE 

TREATING 

ANO 

BLENDING 

UNLEAOEO 

' GASOLINE 

, LEADED 

GASOLINE 

- ^ KEROSENE 

- ^ JET FUEL 

^P DISTILLATE 

FUEL OIL 

-fc> LPG'S 

GAS OIL 

CATALYTIC 

HYDROCRACKING 

-§> LPG S 

. j w MIDDLE 

OISTILLATES 

->>> FINISHED 

GASOLINE 

Sourct: Adapted Irom American Petroleum Institute, Standard Definitions lor Petroleum Statistics, Technical Report No. 1, Third Edition. 

ASPHALT 

ROAO-OIL 

- PETROLEUM 

^ COKE 

- . RESIDUAL 

~ FUEL OILS 

WAXES 

LUBE OILS 

I 
P.7 

the year downstream charge capacity increased 3 percent for catalytic cracking (recycled), and nearly 11 percent for catalytic hydrocracking. The relationship 

between downstream units and product output is 

shown in Figure 1. 

Refiners project that total downstream charge capacity 

mty drop to 28.2 million barrels per stream day by 1986. 

However, the downstream processing mix is not projected to change appreciably from January 1, 1985 

levels. All major downstream refinery processes, except catalytic hydrotreating, are expected to fall below 

current year levels. 

Refinery Receipts of Crude Oil 

Refinery receipts of crude oil averaged 12.2 million barrels per day during 1984, up 0.5 million barrels per day 

from 1983. This increase represented a reversal of the 

downward trend that started in 1979. Receipts of 

domestic crude oil averaged 8.8 million barrels per day 

and foreign averaged 3.3 million barrels per day. Most 

of the increase in refinery receipts of crude oil was from 

domestic sources, rising from 8.6 million barrels per 

day during 1983 to 8.8 million barrels per day during 

1984. Foreign crude receipts also rose during 1984, 

reaching 3.3 million barrels per day from 3.2 million barrels per day during 1983. 

Storage Capacity 

Shell and working storage capacity at refineries and 

blending plants on January 1, 1985 totaled 911 million 

barrels and 803 million barrels, respectively. Shell 

storage capacity was relatively unchanged from the 

previous year, but working storage capacity recorded a 

2 percent gain from the January 1,1984 level. Refineries 

previously closed, but retaining their storage capabilities, accounted for 50.3 million barrels of total working 

storage capacity and 54.6 million barrels of total shell 

storage capacity. 

Fuels Consumed 

Various energy forms such as crude oil, distillate and 

residual fuel oil, liquefied petroleum gases, natural gas, 

still gas, petroleum coke, coal, electricity, and purchased steam are consumed at refineries. In 1984, refineries used 20.3 million barrels of distillate and residual 

fuel oil, down from 21.5 million barrels in 1983. Petroleum coke, including both marketable and catalyst 

coke, consumed during 1984 was 67.6 million barrels, 

slightly above the 1983 level of 66.9 million barrels. 

Still gas consumption increased to 192 million barrels 

from 188 million barrels reported in 1983; natural gas 

use increased 0.4 million cubic feet from the year-earlier level. 

Potroloum 9upply Annum! 1994, Volumo I I Knorgy Informmtlon Admlnlmtrmtlon 
CO 

4) 

L_ 

<D 

C 

• — 

<D 

£ 

z 

320 

OPERATING U.S. REFINERIES 

1970 - 1985 

' 313 ^314 : 

190 

1970 

1 

1975 

( 

1980 1985 

Based on data from DOE/EIA 
Table 1. 

Number and Capacity of Operable Petroleum Refineries by PAD District, Refining District, 

and State as of January 1,1985 

District 

and 

State Total 

IB 

1 

2 

1 

6 

1 

1 

4 

2 

8 

6 

2 

a 

1 

27 

8 

6 

4 

4 

4 

1 

5 

2 

2 

1 

13 

7 

6 

4 * 

17 

22 

19 

2 

16 

1 

16 

2 

4 

5 

S 

4 

78 

3 

6 

7 

6 

22 

Number of 

Operable Refineries 

Operating 

14 

1 

2 

0 

S 

0 

0 

4 

2 

7 

5 

2 

21 

1 

25 

7 

6 

3 

4 

4 

1 

4 

2 

1 

1 

12 

7 

5 

42 ' 

16 

19 

15 

1 

13 

1 

15 

1 

4 

5 

5 

4 

M 

3 

5 

6 

6 

20 

Idle' 

4 

0 

0 

1 

1 

1 

1 

0 

0 

1 

1 

0 

6 

0 

2 

1 

0 

1 

0 

0 

0 

1 

0 

1 

0 

1 

0 

1 

4 

1 

3 

4 

1 

3 

0 

1 

1 

0 

0 

0 

0 

9 

0 

1 

1 

0 

2 

Total 

1.472.050 

140.000 

28.500 

14.200 

570.400 

41.850 

3.000 

622.100 

52,000 

112.891 

96.221 

16.670 

1.SM.M 1 

66.000 

2.251.500 

960.500 

442.300 

222,500 

116.500 

449,700 

60.000 

306.143 

204.143 

63.000 

39.000 

719.060 

337.450 

381.600 

1.342.H ! 

566.100 

3.705.774 

2.574,656 

106.600 

2,173,056 

296.000 

257,780 

43,000 

65.480 

75.900 

73.400 

68.200 

7.171,610 

82.700 

148.550 

161.500 

172.005 

6(4,766 

Barrels per 

Calendar Day 

Operating 

1,257.000 

140.000 

28.500 

0 

414.400 

0 

0 

622.100 

52.000 

112,711 

96,041 

16,670 

1,3M,711 

66,000 

1.996,900 

706,500 

442,300 

221,900 

116.500 

449.700 

60.000 

301,143 

204,143 

58,000 

39.000 

711.460 

337.450 

374.000 

3,071,4(3 

553.250 

3.382.874 

2.446,500 

80.000 

2.071,500 

295.000 

235.800 

33.600 

53.000 

75.900 

73,400 

68,200 

*.*M,C24 

82,700 

135.150 

155.500 

172.005 

646,356 

Crude Capacity 

Idle 

215.050 

0 

0 

14.200 

156.000 

41,850 

3.000 

0 

0 

180 

180 

0 

215.230 

0 

254,600 

254.000 

0 

600 

0 

0 

0 

5.000 

0 

5.000 

0 

7,600 

0 

7,600 

2*7,200 

11.850 

322.900 

128.156 

26.600 

101,556 

0 

21.980 

9,500 

12,480 

0 

0 

0 

4s4,SM 

0 

13,400 

6.000 

0 

11.400 

Total 

1.558.000 

150.000 

31.800 

15.000 

606.700 

46.000 

3.500 

652.000 

54.000 

118.700 

101.200 

17.500 

1,(7»,700 

68,000 

2,370,500 

1,019,600 

458.500 

230,800 

124.600 

472,000 

66,000 

316,220 

211,220 

65,000 

40.000 

754,383 

355,383 

399,000 

J^0S,103 

593.750 

3.909.594 

2.692,850 

109.300 

2,273.560 

310.000 

273.215 

45.000 

67,250 

81.965 

79.000 

71.700 

7.541.100 

103.400 

153,850 

168,500 

1/7.750 

•03.600 

Barrels per 

Stream Day 

Operating 

1.329.500 

150.000 

31.800 

0 

441.700 

0 

0 

652.000 

54.000 

118,500 

101,000 

17.500 

1,448,000 

68.000 

2.102,500 

752.600 

458.500 

229.800 

124.600 

472.000 

66.000 

311.220 

211.220 

60,000 

40,000 

745,883 

355.383 

390,500 

3,227,(03 

581.250 

3.572.494 

2,553,350 

81,300 

2.162,050 

310,000 

250,315 

35.000 

54.350 

81.965 

79.000 

71,700 

7,02»,100 

103.400 

139.850 

161.500 

177.750 

682,500 

Idle 

228.500 

0 

0 

15.000 

165.000 

46.000 

3.600 

0 

0 

200 

200 

0 

220,700 

0 

268.000 

267.000 

0 

1.000 

0 

0 

0 

5.000 

0 

5.000 

0 

8.500 

0 

8.500 

2*1,000 

12.500 

337,100 

139,500 

28,000 

111,500 

0 

22.900 

10.000 

12.900 

0 

0 

0 

612,000 

0 

14,000 

7.000 

0 

21,000 

Vacuum 

Distillation 

778.400 

95.000 

0 

14.300 

320.100 

27.000 

0 

294.000 

28,000 

48.575 

38,900 

9.675 

•2M7 I 

33,000 

895,980 

381.700 

231.280 

90.000 

26.000 

155,000 

12,000 

147,000 

132.000 

0 

15.000 

234,500 

100,500 

134,000 

1^10,4*0 

184,975 

1,646,200 

1.142,000 

30.000 

869,000 

243.000 

122,945 

19,000 

32,020 

28,050 

43,875 

11.900 

3.100,020 

37.000 

41.250 

45.500 

75.400 

109.160 

Thermal 

Operation 

102.000 

54.000 

0 

0 

34.500 

0 

0 

0 

13.500 

0 

0 

0 

102,000 

0 

212,700 

105,700 

22.000 

57.600 

0 

27,400 

0 

49.500 

48.000 

1.500 

0 

82,300 

52.000 

30,300 

344* 0 

24.800 

331.300 

458,900 

0 

397.900 

62,000 

18,500 

10.000 

0 

0 

8.500 

0 

(34.600 

4,500 

9.700 

8.500 

9.000 

31.700 

Charge Capa 

Catalytic 

Cracking 

(Fresh) 

603.800 

60.000 

0 

0 

274,000 

0 

0 

242.300 

27.500 

18.000 

18.000 

0 

• 2 1 ,(0 0 

25.000 

837.000 

374,000 

168.000 

60.000 

45.000 

160.000 

30.000 

113,500 

78.000 

26.000 

9.500 

259.000 

125.500 

133.500 

1,2*4,800 

216.100 

1.396.000 

820.900 

0 

764.900 

56.000 

34.000 

0 

18.000 

0 

16.000 

27.100 

2.4*4,100 

23.000 

52.100 

54.800 

61.000 

1*0.(00 

city.* Barrels per 

Catalytic 

Cracking 

1 Recycled) 

71.800 

15.000 

0 

0 

46,000 

0 

0 

9.100 

2.500 

200 

200 

0 

71 J M 

0 

112.700 

17.400 

8.200 

40.000 

1.300 

33.800 

12.000 

7.200 

1.000 

5.200 

1.000 

17,400 

11,000 

6,400 

137,300 

23.700 

130,650 

-45,300 

0 

43,300 

2,000 

7,775 

0 

775 

0 

7,000 

6,100 

211,126 

1,000 

6.600 

10.603 

15.700 

33,(00 

Stream Day) 

Catalytic 

Reforming 

373,860 

56,000 

. 0 

0 

125.500 

0 

0 

183.600 

8,750 

27.620 

23.870 

3.750 

401,47* 

20.000 

620.900 

310,400 

84.500 

46.000 

31.000 

139.700 

9.300 

71.000 

51.000 

12.000 

8.000 

187,300 

90.300 

97.000 

M M M 

146.700 

922.100 

568.300 

21.000 

•448.300 

90.000 

41.700 

6.000 

9.000 

20.900 

5.800 

17.600 

1.MM M 

20.400 

39.800 

25.500 

31.250 

11M M 

Catalytic 

Hydrocracking 

74,000 

19.000 

0 

0 

0 

0 

0 

56.000 

0 

4.440 

0 

4.440 

71.44* 

0 

148,500 

66,500 

0 

0 

0 

82.000 

0 

0 

0 

0 

0 

8.190 

3.190 

5.000 

M M M 

0 

194.000 

203,700 

0 

13$700 

68,000 

0 

0 

0 

0 

0 

0 

1*7,700 

6.000 

4.900 

0 

0 

10,000 

Catalytic 

Hydrotreating 

984.316 

110.000 

2.016 

0 

434.500 

0 

0 

413,300 

24,500 

38,820 

38.820 

0 

140 . ' M 

50,000 

1,147,500 

575.800 

211,700 

153,300 

36.700 

140,500 

29,500 

209.950 

178.200 

16.960 

14.800 

291.400 

144.400 

147.000 

1.MM M 

278.200 

2.794.100 

1.278.000 

48.000 

1,041,000 

189,000 

83.000 

21.500 

18.000 

32.200 

11.300 

28.600 

4.4*1 .(10 

28.700 

120.400 

35.600 

48.800 

233,600 

E M I CO-MI 

Delaware 

Georgia 

Maryland 

J 

• roloum 4 

e 

§ 

«« fc a 

a 

c 

a 

«t 

• tt 

4k olum « 

• 

*» 

*«. 

? 

• 

(Q 

K 

***** 

a 

•5ormm 1 

a 

*, 

a 

3 

3 lira •* 

0 

3 

1—» 

New Jersey 

New York: East 

North Carolina 

Pennsylvania: East 

Virginia 

Appalachian f l 

Pennsylvania: West 

West Virginia 

P A D District 1 Total 

Appalachian 12 

Ind., !«. , Ky. 

Illinois 

Indiana 

Kentucky 

Michigan 

Ohio: West 

Tennessee 

Minn. , Wbc , Daks. 

Minnesota 

North Dakota 

Wisconsin 

Ok la., Kana., Mo . 

Kansas 

Oklahoma 

P A D District II Total 

Tai M Inland 

Tax M GuM CoM t 

Louisiana Gulf CoM t 

Alabama: Gulf 

Louisiana: Gulf 

Mississippi: Gulf 

North La., Arii. 

Alabama: Inland 

Arkansas 

Louisiana: Inland 

Mississippi: Inland 

N a w Msxtco 

P A D Distric t 111 Tota l 

Colorado 

Monluna 

Utah 

Wyoming 

PAD District IV Total 

See footnotes at end of table. 
ro 

Table 1. 

Number and Capacity of Operable Petroleum Refineries by PAD District. Refining District, and State as of January 1, 1985 (continued) 

Potro lou 

3 

m upplyAnt tuml 1994, Volui 

Distrkl 

and 

State 

Alaska 

California 

Hawaii 

Nevada 

Oregon 

Washington 

PAD District V Total 

UNITED STATES TOTAL 

Puerto Rico 

Virgin Islands 

Guam 

Hawaiian Foreign Trade Zone 

Total 

4 

37 

1 

1 

1 

7 

11 

213 

3 

1 

1 

1 

Number of 

Operatjto Refineries 

Operating 

4 

34 

1 

1 

0 

7 

47 

I M 

3 

1 

0 

1 

Idle1 

0 

3 

0 

0 

1 

0 

4 

24 

0 

0 

1 

0 

I 

Total 

139.000 

2.060.600 

48.000 

4,500 

15.000 

411,300 

umm 

1UH. M 

121.000 

545.000 

43,300 

62.000 

Barrels per 

Calendar Day 

Operating 

139.000 

2.089.600 

48.000 

4.500 

0 

411.300 

2*).4M 

M.MMH 

121.000 

395,000 

0 

62,000 

'Refineries where distillation units are completely idle but not permanently shutdown 

Source: Form EIA-820. 

Crude Capacity 

Idle 

0 

296.470 

0 

0 

15.000 

0 

311,47* 

1.2M.1M 

0 

160.000 

43.900 

0 

Barrels per 

Stream Day 

Total Operating 

1-42.563 142,553 

2,531,546 2,206,146 

50.000 50.000 

4,700 4,700 

16.000 0 

429.254 429.254 

i.i7Mn yuajma 

K.6M/4M W,1tt.M6 

130,000 130.000 

596.000 430.000 

47,160 0 

70,000 70,000 

on January 1,1985 

Idle 

0 

325.400 

0 

0 

16.000 

0 

341,4* 

iJKjm 

0 

166.000 

47.160 

0 

Vacuum 

Distillation 

6.000 

1.305.800 

28.000 

2.500 

16.000 

195.000 

1JBU M 

MKT.SS 

68.000 

215.000 

1.400 

30,000 

Thermal 

Operation 

0 

486.500 

0 

0 

0 

59.000 

546.CM 

1.KU M 

0 

86.000 

0 

0 

Charge Capacity 1 Barrels per 

•Catalytic 

Cracking 

1 Fresh) 

0 

576.950 

22,000 

0 

0 

91,500 

>MMB0 

cai,7s* 

14.000 

0 

0 

0 

Catalytic 

Cracking 

(Recycled) 

0 

27.060 

0 

0 

0 

23.000 

50,*M 

MM7 S 

0 

0 

0 

0 

Stream Day) 

Catalytic 

Reforming 

12.000 

530.030 

0 

0 

0 

103.800 

*46 « 

3.74MM 

58.570 

115.000 

0 

13.000. 

Catalytic 

Hydrocracking 

7,500 

353.200 

0 

0 

0 

49.000 

>*M.7M 

1.M.-4M 

15.000 

0 

0 

12.000 

Catatytic 

Hydrotreating 

0 

1.28S.440 

3.500 

0 

0 

190.300 

1.471.240 

tjmjm 

'81.600 

420.000 

0 

13.000 

? 

[ 

! 

r 
Table 2. 

Production Capacity of Operable Petroleum Refineries by PAD District, Refining District, and State as of January 1,1985 

(Barrels per Stream Day, Except Where Noted) 

sr 

o 

r 

** i 

•y 

kp 

a 

a 

c 

f 

•0 

*•; 

f 

lb I 

3* 

8-

District 

and 

State 

East Coast 

Delaware 

Georgia 

Maryland 

New Jersey 

NewYorIc East 

Pennsylvania: East 

Virginia 

.Appalachian f l 

Pennsylvania: West 

West Virginia 

PAD District 1 Total 

Appalachian #2 

Ind., IH., Ky. 

Illinois 

Indiana 

Kentucky 

Michigan 

Ohio: West 

Tennessee 

Minn., Wise., Daks. 

Minnesota 

North Dakota 

Wisconsin 

Okla., Kan*., Mo. 

Kansas 

Oklahoma 

PAD District II Total 

Texas Inland 

Texas Gulf Coast 

Louisiana Gulf Coast 

Alabama: Gulf 

Louisiana: Gulf 

Mississippi: Gulf 

Alkyiation 

69,000 

8,000 

0 

0 

20,000 

0 

41,000 

0 

2,500 

2,500 

0 

71,500 

7,000 

149,-400 

74,200 

28,900 

11,000 

7,500 

24,300 

3,500 

18,800 

14,400 

2,800 

1,600 

66,600 

33,800 

32,800 

241,800 

51,500 

202,475 

175,900 

0 

159,700 

16,200 

Production Capacity 

Asphalt 

163,884 

0 

22,784 

11,300 

91,800 

13,000 

25,000 

0 

4,000 

4,000 

0 

187,884 

12,000 

139,430 

37,550 

50,230 

30,000 

8,650 

9,500 

3,500 

62,500 

49,000 

0 

13,500 

29,600 

8,800 

20,800 

243,530 

22,125 

30,300 

91.900 

6,000 

65,900 

20,000 

Aromatics 

12,672 

3,372 

0 

0 

0 

0 

9,300 

0 

0 

0 

0 

12,872 

0 

39,000 

3,500 

13,000 

6,500 

0 

16,000 

0 

0 

0 

0 

0 

3,245 

1,445 

1,800 

42,246 

1,550 

130,870 

18,714 

0 

13,214 

5,500 

Isomerization 

25,000 

0 

0 

0 

25,000 

0 

0 

0 

0 

0 

0 

25,000 

0 

35,000 

0 

18,000 

17,000 

0 

0 

0 

12,500 

8,000 

4,500 

0 

16,800 

9,000 

7,800 

84,300 

39,700 

56,100 

7,000 

0 

7,000 

0 

Lubricating Oils 

23,200 

0 

0 

0 

11,700 

0 

11,500 

0 

16,849 

11,600 

5,249 

40,049 

0 

23,400 

5,800 

6,800 

7,900 

0 

2,900 

0 

0 

0 

0 

0 

13,000 

2,500 

10,500 

38,400 

1.000 

93.600 

26,-400 

0 

26,400 

0 

Hydrogen 

(MMCFD) 

96 

40 

0 

0 

11 

0 

45 

0 

5 

4 

1 

101 

0 

117 

25 

0 

20 

0 

72 

0 

22 

22 

0 

0 

9 

0 

9 

148 

70 

546 

360 

0 

165 

195 

Petroleum 

Coke 

33,475 

9,900 

0 

0 

10,675 

0 

7,300 

5;600 

0 

0 

0 

33,475 

1,000 

60,875 

33,075 

8,700 

8,300 

0 

10,800 

0 

3,600 

3,600 

0 

0 

16.100 

9,900 

6,200 

81,575 

6.580 

80,145 

96,595 

0 

80,595 

16,000 
Table 2. 

Production Capacity of Operable Petroleum Refineries by PAD District, Refining Distripct, and State as of January 1,1985 (continued) 

(Barrels par Stream Day, Except Whara Noted) 

i 

t 

*» 

a 

O, 

I 

I 

k i 

8* 

5 

! 

District 

and 

State 

North la.. Ark. 

Alabama: Inland 

Arkansas 

Louisiana: Inland 

Mississippi: Inland 

New Mexico 

PAD District III Total 

Colorado 

Montana 

Utah 

Wyoming 

PAD District IV Total 

Alaska 

California 

Hawaii 

Oregon 

Washington 

PAD District V Total 

UNITED STATES TOTAL 

Puerto Rico 

Virgin Islands 

Guam 

Hawaiian Foreign Trade 

Zone 

Alkyiation 

8.400 

0 

4,400 

0 

4,000 

2,900 

441,175 

0 

10,880 

11,p400 

8,850 

31,130 

0 

102,700 

4,500 

0 

24.600 

131,800 

917,406 

0 

0 

0 

0 

Production Capacity 

Asphalt 

46,741 

12,000 

12,160 

1,511 

21,070 

3,100 

194,188 

3,300 

15,600 

1,700 

15,400 

38,000 

8,300 

87,533 

1,300 

11,500 

16,700 

125,333 

768,913 

1,000 

0 

350 

0 

Aromatics 

5,000 

0 

0 

5,000 

0 

0 

156,134 

0 

0 

0 

0 

0 

0 

3,500 

0 

0 

0 

3,500 

214,561 

14,580 

35,000 

0 

0 

Isomerization -

2,000 

0 

0 

2,000 

0 

0 

104,800 

0 

4,450 

2,150 

1,500 

8,100 

0 

12,200 

1,500 

0 

2,900 

18,600 

218,800 

0 

15,000 

0 

0 

Lubricating Oils 

17,150 

0 

5,4-60 

11,690 

0 

0 

138,150 

0 

0 

0 

1,540 

1,640 

0 

26,400 

0 

0 

0 

26.400 

242.539 

6,900 

0 

0 

0 

Hydrogen 

(MMCFD) 

302 

8 

288 

6 

0 

0 

1,278 

8 

19 

0 

0 

27 

13 

923 

3 

0 

79 

1,018 

2.572 

18 

0 

0 

17 

Petroleum 

Coke 

3,750 

2,000 

0 

0 

1,750 

400 

187,470 

900 

3.700 

2,690 

3,700 

10,990 

0 

95,143 

0 

0 

14,900 

110,043 

423,563 

0 

. 0 

0 

0 

Source: Form EIA-820. 
Table 3. 

•« 

o 

e 

e 

3 

« I 

•*? 

k 

a 

a 

c 

4k 

? 

3 

a I 

k 

a 

3 

3" 

Capacity of Operable Petroleum Refineries by State as of January 1.1986 (Borate Per Stream Day, Except Where Noted) 

Refiner 

Allied Materials Corp. 

taber Refining Inc. 

Amerada Hess Corp. 

American Petroflna Co. Of Texas 

American Refining Group Inc. 

Amoco Oil Co. 

Asamera 011 (US) Inc. 

Ashland 011 Inc. 

Atlantic Richfield Co. 

B-T Energy Corp. 

Beacon 011 Co. 

Bloomfleld Refining Co. 

BP 011 Corp. 

Calcasieu Refining Co. 

Cal met Refining Co. 

Canal Refining Co. 

Cenex 

ChampUn Petroleum Co. 

Charter International 011 Co. 

Chevron U.S.A. Inc. 

C1bro Petroleum Products Inc. 

C1tgo Petroleum Corp. 

Claiborne Gasoline Co. 

Clark Oil 4 Refining Corp. 

Coastal Petroleum Refiners Inc. 

Coastal States Petroleum Co. 

Conoco Inc. 

Cross 011 4 Refining Co. 

Crown Central Petroleum Corp. 

Cry-sen Corp. 

Crystal 011 Co. 

Crystal Refining Co. 

Damson Gas Processing Corp. 

Derby Refining Co. 

Diamond Shamrock Refg. 4 Mktg. Co. 

Edglngton 011 Co. Inc. 

Ergon Inc. 

Exxon Co. U.S.A. 

Farmland Industries Inc. 

Fletcher 011 4 Refining Co. 

Flint Chemical Co. 

Flying J Petroleum Inc. 

Refineries 

on 

Pagels) 

13 

16 

11,12,18 

14,16 

14 

8,9,13.14 

16,17,18 

8 

10,11,13,14 

6,14,17 

10 

6 

12 

14 

10 

11 

10 

12 

6,14 

15 

6,8,11,12 

14,16,17 

13 

10 

11 

8,10 

7 

15 

7,8,10,12 

13,15 

6 

15 

16,17 

6 

11 

16 

9 

16 

7 

11 

7,10,12,15 

9 

7 

16 

12,13 

Refiner 

Gary Refining Corp. 

Giant Refining Co. 

Gibson 011 4 Refining Co. Inc. 

Gladleux Refinery Inc. 

GNC Energy Corp. 

Golden Eagle Refining Co. Inc. 

Golden Uest Refining Co. 

Guam Oil 4 Refining Co. Inc. 

Gulf Refining 4 Marketing 10, 

Hawaiian Independent Refinery Inc. 

Howell Hydrocarbons Corp. 

Hunt Oil Co. 

Huntway Refining Co. 

Indiana Farm Bureau Coop. Assn. 

International Processors 

Kenco Refining Inc. 

Kentucky 011 4 Refining Co. 

Kern 011 4 Refining Co. 

Kerr-McGee Refining Corp. 

Koch Refining Co. 

La Gloria Oil 4 Gas Co. 

Lakeside Refining Co. 

Laketon Refining Corp. 

Liquid Energy Corp. 

Littl e America Refining 

Louisiana Land 4 Exploration Co. 

Lunday Thagard Oil Co. 

MacMlllan Petroleum Co. 

Mapco Petroleum Inc. 

Marathon Petroleum Co. 

Mobil 011 Corp. 7 

Mobile Bay Refining Co. 

Montana Refining Co. 

Morrison Petroleum Co. 

Motor Oils Refining Co. 

Mountaineer Refining Co. Inc. 

Murphy 011 U.S.A. Inc. 

National Coop. Refy. Assn. 

Navajo Refining Co. 

Nevada Refining Co. 

Newhall Refining Co. Inc. 

Oxnard Refinery 

Refineries 

on 

Page(s) 

8 

12 

7 

9 

13 

7 

7 

18 

13,14,15,18 

18 

16 

6 

7 

9 

10 

12 

9,10 

7 

11,13 

11,15 

16 

11 

9 

16 

18 

6 

7 

6,7 

6,14 

8,10,11,15 

.8.12.15.17 

" ' ',1 

12 

16 

9 

18 

10,17 

9 

13 

12 

7 

7 

Refiner 

Pacific Refining Co. Inc. 

Paramount Petroleum Corp. 

Pennzoll Co. Inc. 

Pester Refining Co. 

Petrolite Corp. 

Petroaax Refining Co. Inc. 

Phillips Petroleum Co. 

Phillips Puerto R1co Core Inc. 

Placid Refining Co. 

Pride Refining Inc. 

Quaker State 011 Refining Corp. 

RMT Properties Inc. 

Rock Island Refining Corp. 

Saber Refining Co. 

San Joaquin Refining Co. Inc. 

Seagull Refining Co. 

Seaview Petroleum Inc. 

Shell 011 Co. 7 

Sinclair 011 Corp. 

Somerset Refinery Inc. 

Southland 011 Co. 

Southwestern Refining Co. Inc. 

Standard 011 Co. of Ohio 

Sun Co. Inc. 

Sunland Refining Corp. 

Tenneco 011 Co. 

Tesoro Petroleum Corp. 

Texaco Refining 4 Marketing Inc. 

Texas City Refining Inc. 

Texas NAPC0 Inc. 

ThHftway Co. 

Tosco Corp. 

Total Petroleum Inc. 

Troplcana Energy Co. 

United Refining Co. 

Unocal Corp. 

U.S. Oil 4 Refining Co. 

Vicksburg Refining Inc. 

Virginia 011 4 Refining Co. Inc. 

Vulcan Refining Co. 

West Coast 011 Co. 

Wltco Chemical Corp. 

Wyoming Refining Co. 

Young Refining Corp. 

Refineries 

on 

Pagels) 

7 

7 

11,14 

9 

lb 

15 

15,16,17 

18 

10 

16 

14,17 

17,18 

9 

15 

7 

17 

12 

,9,10,15,16,17 

13,18 

10 

11 

15 

13 

13.14.18 

7 

10 

6 

7.8.9.10 

12,15,16,1-7 

15 

i r\ 

13 

6,8 

9,11,13 

16 

! 

14 I 

8,9,16 | 

wl 12 

17 

6 

8 

8,14 

18 

a 
P.M 

1 i 

M 

1 

! 

I 

s 

to 

t 

H 

ifi 

I 

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II* 

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Potroloum 9uooiv Annuel 1994. Volumo I I Enorgy Informmtlon Admlnlotrotlon 
3 

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*«-

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Table 3. 

Capacity of Operable Petroleum Refineries by State as of January 1,1885 (Barrels per Stream Day. Except Where Noted) (continued) 

Crude-Capacity Charge Capacity 

Refinet/State/Location 

Barrets per 

Calendar Day 

Barrels per 

Stream Day 

Operating Idle Operating 

Vacuum Catalytic Catalytic Catalytic 

DetiBa- Thermal Cracking Cracking Catalytic Hydration Operation (Fresh) I Recycled! Reforming cracking 

•Catalytic 

H^Jlo-

•uaaronw icuriunuaui 

Coastal PeuulauiTi Refinen Inc. 

(Formerly -Coastal Petroleum 

Inc.r-BakanfMd (Palomel 

•Conoco Inc.-Santa Maria 

EJp>p)jtuii O i Co. Inc.-Long Beech 

Exxon Co. U.S.A.-Benicia 

Fletcher OU & Refining Co-Carson 

Gibson Oil & Refining Co. Inc. 

-Bakersfield 

Golden Eagle Refining Co. Inc. 

-Carson 

Golden West Refining Co. 

-Santa Fe Springs 

Huntway Refining Co. 

(Formally Huntway Refining 

Co. of Northern California I 

-Benicia IVan Nuys) 

-Wilmington 

Kern Oil & Refining Co.-Bakersfield 

Lunday Thagard Oil Co-South Gate 

MacMillan Petroleum Co.-Signal Hill 

(Long Beach) 

M oW Oil Corp.-Torrance 

10.000 

9.600 

41.600 

108.000 

0 

0 

0 

0 

10.200 

10.000 

44.800 

114.000 

0 

0 

0 

0 

0 

7,800 

21.000 

61.000 

0 

0 

0 

"27.50 0 

29,500 

S.SOO 

40.600 

7.300 

5.500 

21.400 

8.100 

11.000 

123.500 

Newhall Refining Co. Inc.-Newhall 21,400 

Oxnard Refinery-Oxnard 4,000 

Pacific Refining Co. Inc.-Hercules 56,000 

Paramount Petroleum Corp. 

(Formerly Independent Valley 

Energy Cd.)-Bakersfield 0 

Paramount Petroleum Corp. 

(Formerly Pacific Oasis Corp.) 

•Paramount 

San Joaquin Refining Co. Inc. 

-Bakersfield 

Shell OH Co.-Martinei 

16.170 

21.500 

32.000 14.500 

-Wilmington 

Sunland Refining Corp.-Bakersfield 

Texaco Refining & 

Marketing Inc. 

(Formerly Getty Refining 

& Marketing Co.) 

-Bakersfield 38,000 0 

Texaco Refining & 

Merketing Inc. 

(Formerly Texaco Inc.) 

-Wilmington 0 75,000 

31.700 

8.600 

0 

42.300 

9,000 

5.800 

23.000 

8.500 

12.200 

130.000 

23,000 

5.000 

57,000 

33,000 

10,000 

91,400 

93,000 

12,000 

14.300 

0 

0 

0 

11.000 

94.000 

96.000 

17.000 

42.000 

0 0 0 

0 0 0 

16,500 0 0 

0 25,000

 10 13,800 

0 0 

5.200 0 

0 *7,000 

7.000 0 

0 0 

95.000 '48.000 

8,000 

0 0 

15,000 '"12,000 

21.500 23,000 '11.800 

15.000 28.000 0 

16,000 10.000 *°5.000 

0 67.300 "22.00 0 

60.000 '52.000 

0 22.000 

0 

0 

0 

57.000 

9.450 

0 

0 

13.500 

0 

0 

0 

0 

0 

61.000 

0 

60.000 

35,000 

0 

0 

0 

0 

11,000 

1,050 

0 

0 

0 

0 

0 

"28.00 0 

'4.200 

0 

0 

'19.000 

0 

0 

'3.000 

0 

0 

'36,000 

'2,500 

0 

'15.000 

'11,500 

0 

"23.00 0 

'24.000 

0 '9.500 

0 

0 

0 

28.000 

0 

0 

0 

11.000 

0 

0 

0 

0 

0 

21.700 

0 

5.000 

0 

-yciooo 

0 78.400 42.000 '48.000 28.000 8.000 '35.000 20.000 

0 

0 

0 

•2O.00O 

"25.000 

"22.500 

•33,000 

*11,500 

•10.000 

0 

0 

'12,000 

•860 

0 

'3.000 

0 

0 

•16,000 

'28.000 

'21.000 

'5.000 

'2.500 

0 

'15,000 

'7,000 

'11.500 

'10,000 

0 

*17.000 

'16,000 

'83,300 

•27,000 

'33.000 

•71.000 

0 

"S.soo 

4

15.000 

'25.000 

Production -Capacity 

IsomeriAHtylation Asphalt Aromatics zation 

Lubricating 

0*s 

Hydrogen Petroteun 

IMMCFOI Coke 

0 

0 

0 

11.600 

0 

6.800 

15.000 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

104 

0 

0 

0 

S.SOO 

0 0 

0 0 

0 0 

3.000 4.000 

0 0 

0 3.200 

0 0 

0 5.833 

0 

12.300 

0 

fl rvm 

8.600 

6.000 

2.500 

0 

0 

15.000 

5.000 

V ceo 

0 

0 

0 0 

0 0 

0 0 

0 0 

0 0 

0 0 

c 0 

0 "2.70 0 

0 0 

0 

4.600 

0 

0 

0 

11 oooo 0 

62 

0 

0 

0 

0 oooo 

0 

14,500 

0 3.000 

0 0 

106 100 

36 12.500 

4.400 8.250 

See footnotes at end of table. 
C.apacHy of Operable Petroleum Refineries by State as of January 1,1985 (Barrels per Stream Day, Except Where Noted) (continued) 

i 

a I 

«•* 

a f 

oo 

Refiner/ State/ Location 

California (continued) 

Toaco Corp.-Maninej (Avon) 

Unocal Corp. 

(Formerly Union 01 Co. 

of California] 

Arroyo Grande (Santa Maria) 

-Rodeo (San Francisco) 

-Wilmington 

Wast Coast -OH Co.-Oddale 

Witco -Chemical Corp.-Bakersfield 

(Oitdale) 

Total 

Crude Capacity 

Barrets per 

Calendar Day 

Operating 

126.000 

41.000 

70.000 

108.000 

10.000 

0 

2.0*0,800 

Idle 

0 

0 

0 

0 

9.000 

0 

2*8,470 

Ban eb per 

Stream Oay 

Operating 

132.600 

43.300 

74.000 

111,000 

11,000 

0 

2J08.148 

Idle 

0 

0 

0 

0 

10.000 

0 

"05.400 

Vacuum 

Distilation 

106.000 

32.000 

38.500 

83.000 

0 

9,000 

ijgs^se 

Thermal 

Operation 

"37.000 

•27.000 

"18.500 

'°20.000 

0 

0 

488.680 

Catalytic 

Cracking 

(Fresh) 

46.000 

0 

0 

47.000 

0 

0 

S78.860 

Charge Capacity 

Catalytic 

Cracking 

(Recycled) 

0 

0 

0 

7.000 

0 

0 

27,050 

Catalytic 

Reforming 

"8.700 

'20.000 

0 

'28.000 

'52.000 

0 

0 

UO.OO 

Catalytic 

Hydrocracking 

20.000 

0 

34.000 

22.000 

0 

0 

361.200 

Catalytic 

Hydrotreating 

•24.500 

'10.000 

'4S.000 

0 

"S.SOO 

*23.000 

'14.500 

'36.000 

•54,000 

0 

'580 

1,286.440 

Alkyfation 

10.500 

0 

0 

10.000 

0 

0 

102.700 

Asphalt 

0 

0 

0 

0 

0 

3.200 

t7.sn 

Production Capacity 

Aromatics 

0 

0 

0 

0 

0 

0 

1.600 

Isomerization 

0 

0 

0 

0 

0 

0 

12,200 

Lubricating 

Oils 

0 

0 

4.800 

0 

0 

5.300 

28,400 

Hydrogen 

(MMCFOI 

75 

0 

70 

49 

0 

0 

*2J 

Coke 

6.000 

6.500 

4.250 

0 

0 

0 

86.141 

Colorado 

Asamera Oil IUS) Inc. 

-Commerce City (Denver) 26.000 

Conoco Inc.-Commerce City 

(Denver) 41.500 

Gary Refining Corp. 

(Formerly Gary Western 

Co.l-Fruita 15,200 

Total 82,700 

Delaware 

Texaco Refining & Marketing 

Inc. (Formerly Getty 

Refining & Marketing 

0 

0 

0 

0 

44.900 

42.500 

16.000 

103,400 

0 

0 

0 

0 

20.000 

7,000 

10.000 

37,000 

0 

0 

•4,600 

4,600 

8,000 

15,000 

0 

23,000 

0 

1.000 

0 

1,000 

'10.000 

'7,000 

'3,400 

20,400 

0 

0 

6.000 

8,000 

'10.000 

'7,000 

•8.500 

'3.200 

28,700 

0 

0 

0 

0 

0 

3.300 

0 

1,100 

900 

1 

s fc 1 

1 J 

Col-Delaware -City 

Georgia 

Amoco Oil Co.-Savannah 

Young Refining Corp.-Douglesville 

Total 

Hawaii 

Chevron U.S.A. Inc.-Honolulu 

Illinois 

Clark -Oil & Refining Corp. 

Island 

-Hanford (Wood River) 

Marathon Petroleum Co. 

(Formerly Marathon Oil 

Co.)-Robinson 

Mobil Oil Corp. Joliet 

Blue 

140.000 

24.000 

4.500 

28,800 

48.000 

57,000 

47,500 

120.000 

180.000 

0 

0 

0 

e 

0 

0 

0 

75.000 

0 

150.000 

27.000 

4.800 

31.800 

50.000 

60.000 

60.000 

126.000 

200.000 

0 

0 

0 

0 

0 

0 

0 

80.000 

0 

95.000 

0 

0 

8 

28.000 

27.000 

18.000 

62.000 

88.000 

"54.000 

0 

0 

0 

0 

0 

'14.500 

1o4.000 

'24.000 

'35.000 

60.000 

0 

0 

0 

22.000 

25.000 

27.000 

38.000 

98.000 

15.000 

0 

0 

0 

0 

1.000 

1.000 

400 

0 

'66.000 

0 

0 

0 

0 

'30.500 

'12.000 

"12,400 

'65.000 

'46.000 

19.000 

0 

0 

0 

0 

11.000 

0 

22.000 

0 

'66.000 

'56.000 

0 

*192 

'1.296 

'528 

2 At * 

'S.SOO 

'20.500 

•10.000 

'12.000 

'6.000 

'52.000 

"9.000 

'75.000 

'72.000 

8.000 

0 

0 

0 

4.500 

6.000 

8.000 

7.600 

24.000 

0 

20.000 

2.784 

22.784 

1.300 

3.000 

0 

0 

0 

3,372 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

"1.500 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

40 

0 

0 

0 

3 

0 

0 

25 

0 

9.900 

0 

0 

0 

0 

0 

4.350 

6.000 

11,125 

Sue footnotes ot end of table 
Table 3. 

Capacity of Operable Petroleum Refineries by State as of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

Refiner/State/Location 

Crude Capacity Charge Capacity 

Barrels per 

Calendar Day 

Barrets per 

Stream Oay Vacuum Catalytic Catalytic Catalytic Catalytic 

OistiHa- Thermal Cracking Cracking Catalytic Hydro- HydroOperating Idle Operating Idle tion Operation (Fresh) (Recycled) Reforming cracking treating 

Production Capacity 

Isomeri- eating Hydrogen Petroleum 

Alkyiation Asphatt Aromatics zation Oils (MMCFD) Coke 

m 

% 

"O 

fc 

a I 

I 

e 

f I 

fc I 

3" 5* 

s 

! 

t£) 

IMnois (continued) 

Motor Oils Refining Co. 

(Formerly Moreoo Energy 

Inc.l-McCook 

Shell Oil Co.-Wood River 

Texaco Refining & 

Marketing Inc. 

(Formerly Texaco Inc.) 

•Lawrenceviile 

Unocal Corp. 

(Formerly Union Oil Co. 

of California) 

-Lemont (Chicago) 

Total 

Indiana 

Amoco Oil Co.-Whiting 

Gladieux Refinery Inc.-Fori Wayne 

Indiana Farm Bureau Cooperative 

Association-Mount Vernon 

Kentucky Oil & Refining Co-Troy 

Laketon Refining Corp.-Laketon 

Rock Island Refining Corp. 

-Indianapolis 

Total 

Kansas 

Derby Refining Co.-Wichita 

Farmland Industries Inc.-CoffeyrHls 

-Phillipsburg 

National Cooperative Refinery 

Association-McPherson 

PMtet Refining Co.-El OorarJo 

Texaco Refining & 

Merketing Inc. 

(Formerty Geny Refining 

& Marketing Co. I 

El Dorado 

Total Petroleum Inc.-Arkansas City 

Total 

See lootnotes al end oi table. 

1.000 0 

250,000 0 

51.000 28,000 

0 151,000 

706.680 264,0 

19.000 

21.200 

1.000 

E7.900 

43.200 

442,300 

28.800 

56.SC0 

26.400 

70.000 

33.250 

80.000 

42.500 

"07.460 

1.600 

261.000 

66,000 

762,800 

360.000 

19.900 

22.600 

2.000 

9,500 

44.600 

468.600 

30.000 

60,723 

27.460 

73.000 

36.000 

82.000 

0 '.200 

0 105.500 

30.000 25.000 

0 

94.000 

287,000 181.700 106.708 

203.000 '22.000 

374,000 

27.000 '12.000 32.000 

47,200 0 6,000 0 18,000 

W.U 3 0 1(0.600 62,000 125,800 

0 0 

0 "68.000 

'22.000 

0 167.000 K-***" '28.200 58.000 5.000 '30.500 

310,4 

7.000 "73,000 

ooo 

0 

0 

0 

0 

0 

0 

0 

7,200 

0 

6.080 

15.000 

231,280 

10.000 

19,600 

10.000 

18.000 

10.000 

ooo 

0 

22X00 

'5.000 

'13,000 

0 

'22,000 

0 

8,000 

0 

0 

20,000 

mooo 

17.000 

23.000 

0 

20,000 

16.500 

200 

6 

0 

1.000 

8,200 

2.500 

1.500 

0 

1.000 

2.000 

'3.600 

0 

0 

'8,000 

84.600 

',7000 

•16,000 

'5.300 

'15,000 

'5.700 

4.000 '25.000 

0 '16.300 

11,000 80,100 

0 

33.500 

3.190 

1,180 

0 

'64.000 

'52.500 

'68.000 

'5.000 

'12.000 

•24,000 

"21,500 

'39,000 

'30.500 

*1,800 

88,500 676.800 

'4.300 

'28.000 

4

40,000 

'16,300 

144/400 

0 150 0 

22.000 28,500 0 

6,600 2.700 

10.000 

3.200 3.500 

74,200 37,560 

0 

0 ooo 

0 

0 

0 

0 

0 

0 

0 

'42.000 

•"ss.ooo 

4

60.000 

•5.200 

0 

'4.500 

0 

0 

• 10.000 

•5.000 

211,700 

"*7.obo 

'5.000 

'18.800 

"^.SOO 

'11.000 

H.sao 

23.000 

0 

1.700 

0 

0 

4,200 

28,888 

3.000 

6.000 

0 

6.000 

3.300 

40.000 

0 

2.200 

0 

3.230 

4.800 

80,210 

n 

6 

2.000 

0 

4.800 

1.446 

0 1J00 

0 4.600 

"2.000 

'V.OOO 

0 0 

6.808 

0 0 0 

0 0 2.500 

0 0 0 

0 "2.000 0 

0 

5.500 2.000 0 0 0 

M.800 8,800 1.448 8.000 2.600 

0 0 

0 3,600 

3M>C 

8.700 

SJW 

0 

0 

0 

0 

0 

1.060 

3.000 

0 

2.800 

200 

0 3.060 

0 0 

6 8.860 
Table 3. 

&>pacity of Operable Petroleum Refineries by State as of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

| 

i I 

IB 

m 

? 

* 

I 

fc I 

! 

J 

5 S, 

| 

? 

o 

Refiner/State/Location 

Kentucky 

AaNand 08 Inc.-Catlettsburg 

^^. 

B-T Energy Corp-Louisv»e 

Kentucky 08 & Refining Co. 

-Betsy Lane' 

Somerset Refinery Inc.-Somerset 

Barrels per 

Crude Capacity 

Calendar Day 

Operating 

213.400 

E3.000 

0 

5.500 

Idle 

0 

0 

600 

0 

Barrels per 

Stream Day 

Operating 

220.000 

E3.S00 

0 

6,300 

Idle 

0 

0 

1.000 

0 

Vapcuum 

Distinction 

90.000 

0 

0 

0 

Thermal 

Operation 

,o2.600 

•56.000 

0 

0 

0 

•Catalytic 

Cracking 

1 Fresh) 

60,000 

0 

0 

0 

Charge Capacity 

Catalytic 

Cracking 

IRecyded) 

40.000 

0 

0 

0 

Catalytic 

Reforming 

'45.000 

0 

0 

'1,000 

Catalytic 

Hydrocracking 

0 

0 

0 

0 

-Catalytic 

Hydrotreating 

•10.000 

'40.000 

'46.000 

4

40.000 

•17.000 

0 

0 

'1.300 

Afcytation 

11.000 

0 

0 

0 

Asphalt 

30.000 

0 

0 

0 

Produ-rtion Capecrry 

fsomeriAromatics obon 

6.500 "5.000 

,412.000 

0 0 

0 • 0 

0 0 

Lubricating 

Ols 

7.900 

0 

0 

0 

Hydrogen 

(MMCFD) 

20 

0 

0 

0 

Coke 

8.300 

0 

0 

0 

Total 

Uxaisana: GuH 

2214 

Calcasieu Refining Co. 

(Formerly CPI Oil & 

Refining Inc. I 

-Lake Charles 14.000 

Canal Refining Co.-Church Point 8.000 

Chgo Petroleum Corp.-Lake Charles 297.000 23,000 

Clark Oil & Refining Co-Mount Airy 

Conoco Inc.-Egan (Acadia) 

-Westlake (Lake Charles) 

Exxon Co. USA-Baton Rouge 

Gulf Refining & Marketing Co. 

(Formerly Gulf Oil Corp.) 

-Beee Cheese (Alliance) 

International Procassors-St. Rosa* 

Marathon Petroleum Co. 

(Formerly Marathon Oil Co.) 

-Garyvile 

Murphy Ol U.S.A. Inc.-Meraux 

Placid Refining Co.-Pon Allen 

Shea Oil Co.-Norco 

Tenneco OH Co.-Cheimene 

Texaco Refining & 

Marketing Inc. 

(Formerly Texaco Inc.) 

•Convent 

Texas NAPCO Inc.-St. James* 

Total 

0 

6,500 

166,600 

437.000 18.000 

198.500 

256,0-00 

46.000 

218.000 

133.000 

28.366 

78.000 12,200 

0 

0 

» 

0 

0 

0 

n 

14.500 

8,800 

306.000 

0 

13,750 

164.000 

466.000 

0 

0 

25.000 ooo 

19.000 

0 

0 

83.000 

11.000 

0 

63.000 

206.000 

0 

0 

•63.000 

'°16.000 

0 

'10.600 

'48.800 

*76,O0O 

0 

0 

160.000 

0 

0 

30.600 

166.000 

206.000 

0 

263.000 

80.000 

48,000 

225.000 

140.000 

0 

36,000 

12.500 

225.000 

0 

.871.800 

0 

20.000 

101 .SM 

240.000 

0 

2.181,060 

0 

20.000 

111JJ00 

73.000 *21,000 89.000 

14.000 0 0 

125.000 

40.000 

16.000 0 

78.000 '19.500 

'103.600 

64.000 '27.500 

75.000 

35.300 

18.000 

100.000 

42.000 

75.000 '"12.00O 70,000 

20.000 0 0 

888,000 JT7.800 784,800 

2,000 

2.000 

0 

0 

0 

0 

0 

0 

0 

0 

"1.900 

"45.000 

'46.000 

0 

0 

'27,400 

'96.000 

0 

0 

30,000 

0 

0 

0 

24.000 

0 

0 

'14.000 

»91,000 

'40.000 

0 

0 

'61,000 

*33,000 

*27,000 

•2.500 

'66,000 

'se.ooo 

•19.000 

0 

0 

20,200 

0 

0 

6.000 

29.800 

2.300 '40,000 

0 0 

14,000 '50.000 

3.000 '21,000 

'7.000 

"28.000 

'47,000 

20.000 '40.000 

0 0 

4Moo 4s*rion 

0 '46.000 28.400 

'42,000 

0 0 0 

0 

27,700 

19,000 

'36.500 

Ho.ooo 

•SB.OOO 

'15.000 

'26,000 

'7,000 

•29.000 

•98.000 

'20,000 

*36.000 

35.000 '102.000 

'40.000 

0 0 

m.Too 1.041.000 

9,100 

4.200 

13.500 

16.000 

12.500 

0 

168.700 

28.900 

20.000 25.000 

12.000 

0 

0 

2.300 

3.914 

0 

0 

0 

7.000 

0 

0 

11,214 

WJ. 

o 

0 

'7.000 

0 

0 

9.000 

17.400 

0 0 

0 0 

7,000 28,488 

0 

0 

28 

0 

51 

8.160 

0 

0 

15.000 

0 

0 

15.800 

25.415 

8,600 

0 

0 

8.600 

7.280 

62 0 

0 0 

188 80,886 

See footnotes at end of table. 
r 

[ 

r i 

• 

s 

1 i 

•**••» 

aaX 

• 

8 Volume 

*» 

? 

\ 

Table 3. 

-Opacity of Operable Petroleum Refineries by State 

Refiner / State / Location 

Louisiana: Inland 

Catumst Refmg Co-Princeton 

CWbome Gaanina Co.-Liabon 

Kerr-MeGee Refining Corp. 

(Formerly Kerr-McGae Corp.) 

-Cotton Va-lay 

Karr-McGaa Refining Corp. 

(Formerly Kail MLuee Corp.) 

-Dubech 

Penruod Co. Inc. 

1 Formerly Atlas Proteasing 

Co.l-Shrevapon 

Total 

Maryland 

Chevron U.S.A. Inc.-Bafrimore* 

MIchigMi 

Crystal Refining Co-Carson City 

Lakeside Refining Co.-Kalamazoo 

Marathon Petroleum Co. 

(Formerly Marathon Oil Co.) 

-Detroit 

Total Petroleum Inc.-Alma 

Crude Capacity 

Barrels per 

Calendar Day 

Operating 

4.400 

E7.500 

7.800 

10.000 

46^00 

0 

3,000 

5,000 

68.500 

40,000 

Idle 

0 

0 

0 

0 

0 

14.200 

0 

0 

0 

0 

Barrels per 

Stream Day 

Operating 

4.766 

7.700 

8,600 

11.000 

60.000 

Idle 

0 

0 

0 

0 

0 

0 15,000 

6.000 

5,600 

71,000 

•42.000 

0 

0 

0 

0 

BS of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

Vacuum 

Distillation 

3.750 

0 

0 

0 

24,300 

14.300 

0 

0 

26.000 

0 

Tftermal 

Operation 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

Catalytic 

Cracking 

(Fresh) 

0 

0 

0 

0 

0 

0 

0 

0 

27.000 

18.000 

Charge Cepecpty 

Catalytic 

Cracking 

(R-scyded) 

0 

0 

0 

0 

0 

0 

0 

0 

1,300 

0 

Catalytic 

Reforming 

0 

'2.000 

0 

"3.900 

'15.000 

0 

0 

0 

'17.000 

'14,000 

Catalytic 

Hydrocracking 

0 

0 

0 

. 0 

o 

0 

0 

0 

0 

0 

Catalytic 

Hydrotreating 

0 

0 

0 

0 

•7,100 

'15.000 

*8,900 

"1.200 

-OJS6 

0 

0 

0 

'17.600 

'1,400 

'14.000 

'3.800 

Afcytation 

0 

0 

0 

0 

0 

6 

0 

0 

0 

4.000 

3,500 

Asphalt 

911 

0 

0 

0 

600 

1,811 

11,300 

0 

0 

8.660 

0 

Aromatics 

0 

0 

0 

0 

5.000 

MSS 

0 

0 

0 

0 

0 

Production 

zation 

0 

,42.000 

0 

0 

0 

xm 

0 

0 

0 

0 

0 

Capacity 

Lubricating 

Ols 

3.190 

0 

0 

0 

8.600 

11,880 

0 

0 

0 

0 

0 

Hydrogen 

(MMCFDI 

0 

0 

0 

0 

6 

6 

0 

0 

0 

0 

0 

Petro&etjrn 

Coke 

0 

0 

0 

0 

0 

6 

0 

0 

0 

0 

0 

fc 

r 

I 

Total 116,866 

Minnesota 

Ashland Oil Inc St. Paul 67,143 

Koch Refining Co.-St. Paul 

(Rosemount! 137,000 

Total 284,141 

Mississippi: Gulf 

-Chevron U.S.A. Inc.-Paacagoula 295,000 

Mississippi: Inland 

124,888 

69.220 

142,000 

211,220 

310.000 

8 28,888 8 -SU 

0 32.000 0 23.000 

1.SB8 81,668 

0 '13.000 

0 100.000 '48.000 56.000 1.000 '38.000 

6 132J60 48,886 78.666 1.688 11.860 

0 243.000 *62.000 56.000 2.000 '90.000 

16.788 

'7,200 

'13.000 

*23,000 

•8.000 

'51.000 

»26.000 

4

50.000 

7,860 8,660 

5.900 14.000 

8.500 36.000 

178,286 14,488 48.686 

0

 ,48.000 

S 6,866 

),000 '30.000 16.200 20.000 5.600 0 

'96.000 

*63,000 

1.000 

Pt 

196 16.000 

Amerada Hess Corp.-Purvis 

Ergon Inc.-Vicksburg 

Southland Oil Co.-Lumberton 

• Sandersville 

30.000 

20.600 

5.800 

11.000 

0 

0 

0 

0 

32.000 

22.000 

6.600 

12.500 

0 

0 

0 

0 

20.000 

17.000 

0 

6.875 

"8,500 

0 

0 

0 

16,000 

0 

0 

0 

7.000 

0 

0 

0 

'5.800 

0 

0 

0 

0 

0 

0 

0 

'5.500 

'5.800 

0 

0 

0 

4.000 

0 

0 

0 

0 

12.000 

3.445 

6.625 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

1.750 

0 

0 

0 
ro 

table J. 

Capecfty of Operable Petroleum Refineries by S m 

Cfude Capacity Charge Capacity Production Capacity 

Refiner/State/Location 

Barrets per 

Calendar Day 

Barrels per 

Stream Day 

Operating Idle Operating 

Vacuum Catalytic Catalytic Catalytic Catalytic LubriD*vHa Thermal Cracking Crackng Catalytic Hydro- Hydro- bomeri- eating Hydrogen Petroleum 

tion Operation I Fresh) (Recycled) Reforming cracking treating Afcytation Asphalt Aromatics zation Ois (MMCFD) Coke 

! 

fc 

Mississippi: Inland (continued) 

? 

1 

1 n Eupply Annumli • 

to 

a.Volume . 

Vicksburg Refining Ine.-Vickaburg 

Total 

Montana 

Canes 

(Formerly Farmers Union 

Central Exchange Inc.) 

•Laurel 

Conoco Inc.-Billings 

Exxon Co. U.S.A.-BHIings 

Flying J Petroleum tnc.-Cutbenk* 

Kenco Refining Inc.-Wolf Point 

Montana Refining Co. 

(Formerty Simmons Refining 

Corp. (-Great Falls 

Total 

6.000 

78/488 

33.660 

48,500 

42.000 

0 

4,700 

6.300 

136,180 

0 

8 

7.800 

0 

0 

5.600 

0 

0 

13,400 

6.000 

26.886 

34.500 

50.000 

-44.000 

0 

4.850 

6,500 

138,860 

0 

6 

8.000 

0 

0 

6.000 

0 

0 

14.606 

0 

43.875 

0 

20.000 

18.000 

0 

0 

3.250 

41,260 

0 

-uss 

0 

0 

"7.50 0 

•2,200 

0 

0 

8,700 

0 

16,888 

13.600 

15.500 

21.000 

0 

0 

2.100 

62,180 

0 

7.666 

1.500 

1.000 

3.500 

0 

0 

600 

6,800 

0 

SwSBS 

'12.000 

'14.600 

"10,00 0 

'2.300 

0 

'1.000 

38,880 

Nevada 

Nevada Refining Co.-Tonopah 4,500 

New Jersey 

Amerada Hesa Corp.-Port Reading* 0 

Chevron U.S.A. Inc.-Perth Ambo y 80,000 

68,000 

88,000 

4,700 

0 70.000 

86.000 95.000 

Exxon Co. U.S.A.-Linden 

M o M 09 Corp.-Paulsboro 

100,000 

100,000 

Seaview Petroleum Inc.-Paulsboro 44.400 0 

Texaco Refining & 

Marketing Inc. 

(Formerty Texaco Inc.) 

-Westville 

110.000 

47.700 

2.600 

30.000 0 

96.000 0 

68.000 

45.000 

33.000 

0 0 

8.000 '39.000 

120.000 25.000 '25.000 

Total 

New Mexico 

Bloomfield Refining Co. 

(Formerly Plateau Inc.) 

-Bloomfield 

Giant Refining Co. 

(Formerly Giant Industries 

Inc.l-Gallup ICiniia) 

90.000 0 

414/100 166,000 

13.700 0 

18.000 0 

95.000 0 

441,700 166,000 

14.000 

62.400 '21.600 36,000 0 '23.500 

34.700 0 0 0 0 

31.000 '"13.000 40.000 12.000 '38.000 

220,100 24.600 274,000 46,000 126,608 

0 0 5.400 500 '2.800 

7.900 0 7.200 3.600 '6.800 

0 0 

4.088 21,878 

4.900 

•4,000 

'15.000 

'14.000 

'3.500 

•37.000 

•15.500 

'20.000 

•6.000 

'90 0 

*2,300 

0 

'1,200 

'1.000 

3.780 

4.400 

2.700 

0 

0 

0 

5.000 

6.500 

3.000 

0 

0 

1.100 

4,600 128,480 M.8S0 16,880 

0 

0 

0 

0 

0 

0 

0 

'20,000 

•39,000 

•so.ooo 

*19,000 

'66.000 

'28.000 

•so.ooo 

'42.000 

'15.000 

0 

'30,000 

'43.000 

4.000 

3.000 

8.500 

1,500 

0 

3,000 

0 

50.000 

38.000 

0 

3.800 

0 

•O4.60S 28,000 81.800 

•2.800 0 0 

'6.800 1.400 700 

'1.250 

'3.200 

0 

0 

0 

0

 ,*2S,000 0 

0 0 8.500 

0 0 3.200 

0 0 0 

6 2MS8 11.700 

0 

19 

0 

0 

0 

18 

0 

3.700 

0 

0 

0 

1,780 

5.800 

11 4,875 

0 0 

0 0 

11 16,676 

See footnotes at end of table. 
Table 3. 

Capacity of Operable Petroleum Refineries by State aa of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

Crude Capacity 

Refiner/ State/ Location 

Barrels per 

Calendar Day 

Operating 

Barrels per 

Stream Day 

Operating 

Charge Capacity 

Vacuum Catalytic 

Oistilla- Thermal Cracking 

tion Operation (Fresh) 

Catalytic 

Cracking Catalytic 

(Recycled) Reforming 

Catalytic Catalytic 

Hydro- Hydrocracking treating 

Production Capacity 

LubriIsomeri- eating Hydrogen Petroleum 

Afcytation Asphalt Aromatics ration OSs (MMCFD) Coke 

f 

SI I 

fc 

I 

5* S 

New Mexico (continued) 

Navajo Refining Co.-Artesia 

Tnrifrway Co.-Farmington 

(Bloomfield) 

Total 

New Yortc: East 

Cibro Petroleum Products 

Inc.-Albany 

30.400 

6.100 

41.860 

Gulf Relining & Marketing Co. 

(Formerly GuH Oil Corp.) 

-Cincinneti ICIeves) •13.700 

Total 

Son loomotos al end ol table. 

374.000 

32.000 

6.700 

71.788 

46.000 

Standard Oil Co. of Ohio-Lima 

-Toledo 

Sun Co. Inc.-Toledo 

Total 

Oklahoma 

Allied Materials Corp.-Stroud 

Conoco Inc.-Ponca City 

Kerr-McGee Refining Corp. 

(Formerly Kerr-McGee Corp.) 

-Wynnepwood 

Sinclapr Oil Corp. Tulsa 

Sun Co Inc. Tulsa 

Total Pmioleum Inc. Ardmore 

168.000 

120.000 

118.000 

'448.700 

0 

134.000 

43.000 

50.000 

85.000 

62.000 

0 

0 

0 

0 

7.600 

0 

0 

0 

0 

0 

177,000 

126.000 

124.000 

472,000 

0 

138.000 

46.000 

53.000 

90.000 

64.500 

380.600 

0 4,000 

0 0 

6 11,888 

0 46.000 27.000 

Annu 004, Vol 

e 

3 

• 

•••» Energy 

North Carolina 

GNC Energy Corp.-Greensboro 

North Dakota 

Amoco Oil Co.-Mandan 

Frying J Petroleum Inc.-WHItston 

Total 

Ohio: East 

Ashland Oil Inc.-Canton 

Ohio: West 

0 

58.000 

0 

68.888 

66.000 

E3.000 

0 

5,000 

6,000 

0 

0 

60.000 

0 

68.806 

68.000 

E3.500 

0 

5,000 

6,886 

0 33.000 

0 1.1 

0 51.000 '16.200 

0 68.000

 511.200 

22.000 0 

166.806 27,400 

8.500 2.600 0 

0 40.000 "23.000 

8,600 134.000 30.300 

14.500 2.000 "2.000 

'6.000 

0 0 0 

27.188 8,168 17.868 

0 0 26.000 6.200 '10.000 

0 *1.500 0 0 '2,000 

28^80 6,208 12406 

25.000 

0 

46.000 

0 13.000 0 20.000 

0 15.000 0 18.000 

0 31.500 '7.300 28.000 

0 32,000 0 22.500 

133.600 

0 '20.000 

0 "-9.000 

0 '10.000 

0 0 

8 

0 '7.000 

'20.000 

'23,000 

1.500 2.400 

0 0 

2J88 l.« 

0 13.000 

•4.000 

11.000 

*950 

'1.000 

2.800 

0 

0 

0 

0 

0 

"4.000 

"SOO 

2.888 

7.000 12.000 

6 4,600 

18.000 

37.000 

55.000 

50.000 

60.600 

2.000 

7.800 

16.500 

7.500 

33400 

'11.000 

'47,000 

"23,000 

'41.000 

1*8.700 

0 

21.000 

35.000 

26.000 

82.880 

"fl.000 

'11,000 

•59.000 

•37.000 

' "^.-soo 

146.660 

6,000 

0 

11.300 

7.000 

24 JOS 

0 

0 

7.000 

2.600 

8.680 

0 

7.500 

0 

8.500 

18.806 

0 

'33.500 

0 '8.600 

5.000 '20.000 

1.400 '23.000 

0 '12,000 

6,400 87,000 6,000 

0 

"9,000 

'33.500 

*4.000 

"9,000 

'5.000 

'20.000 

*24.O0O 

•10.500 

'12.000 

"20.000 

147.000 

0 

9.700 

2.500 

0 

5.000 5.000 0 

3.000 2.500 0 

8.600 4.800 1.800 

6.500 6.000 

12,800 2OJ00 

2.900 

0 

0 

2408 

0 0 1.000 

0 "5.000 2.000 

0 0 

"600 0 

'2.300 7.600 

0 0 

7400 10480 

0 0 

0 0 

0 0 

0 0 

0 . 1.000 

750 

0 

24 

48 

72 

0 

0 

9 

0 

0 

0 

3.200 

3.660 

3.200 

18406 

0 

E3.700 

0 

0 

2. SOO 

0 

0,200 
f 

IS I 

"•? fc 

a 

a 

s 

f 

? 

« 

fc I 

3* 

5" 

i 

a 

Table 3. 

Capacity of Operable Petroleum Refineries by State i i of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

Crude Capacity Charge Capacity 

Refiner/State/Location 

Barrels per 

Calendar Day 

Barrels per 

Stream Day 

Operating Operating 

Vacuum Catalytic Catalytic -Catalytic Catalytic 

Distilla- Thermal Cracking Cracking Catalytic Hydro- Hydration Operation (Freshl I Recycled) Reforming cracking treating 

Oregon 

Chevron U.S.A. Inc-WUlbridge 0 15.000 

Pennsylvania: East 

Atlantic Richfield Co.-Philadelphia 125.000 0 

BP Oil Corp. Marcus Hook 168.000 0 

Gulf Refining & Marketing Co. 

I Formerty Gulf Oil Corp.) 

-Philadelphia 174,100 

Sun Co. Inc.-Marcus Hook 156.000 

Total 822.180 

Pennsylvania: West 

American Refining Group Inc. 

-Indianola 

Ashland Oil Inc.-Freedom 

Pennzoil Co. Inc.-Rouseville 

•Quaker State Oil Refining Corp. 

-Bradford (Smethport) 6,700 

United Refining Co. 

(Formerty Coral Petroleum 

Taxes: Gulf 

American Petrofina Co. of Texas 

-Port Arthur 

Amoco Oil Co.-Texas City 

90.000 

415.000 

Atlantic Richfield Co-Houston 260,000 

Champlin Petroleum Co. 

-Corpus Christi 157.000 

130.000 

177,000 

0 

6,800 

15.700 

ISO 

0 

0 

0 

7.000 

16.500 

7.000 

Inc.l-Warren 

Witco Chemical Corp.-Bradford 

Total 

Tpsnnessee 

Mapco Petroleum Inc-Memphis 

80.000 

6.841 

88441 

60.000 

0 

0 

188 

0 

62.000 

8.500 

101,808 

65.000 

100,000 

432.000 

266.000 

160.000 

16.000 16.000 

83.000 0 29.000 

86.000 0 48.000 

200 

0 

0 

284460 

0 

3.600 

6.500 

2.800 

26.000 

0 

12.000 

0 242408 

18,000 

0 

18400 

30.000 

40.000 '°13.000 36.000 

195.000 '37,000 194.000 

130.000 •M.OOO 78,000 

78.000 '29.000 61.600 

0 '60.000 

1.600 '50.000 

180.000 

166,000 

0 

0 

80.000 

46.000 

0 

0 

86.300 

80.000 

3.500 

4.000 

'34.000 

"10.800 

'28.800 

6.168 

12.000 

0 

0 

'3,600 

0 '2,270 

200 '16.000 

0 '2.000 

280 23478 

'9.300 

'25.000 

'43.000 

30.000 

25.000 

66480 413J00 

0 

0 

'4,600 

•7,800 

*2.520 

43.000 '152.000 113.000 

'68.000 

Production Capacity 

LutKTbomerv eating Hydrogen Petroleun 

Afcytation Asphalt Aromatics ration OJs (MMCFO) Coke 

0 11.500 

•so.ooo 

••54.000 

•"24.000 

•64.000 

'41.000 

•43.000 

'30.000 

'34,000 

•54,300 

'13.000 

•e.ooo 

0 

9.000 

20.000 

12.000 

25.000 

0 

0 

0 

0 

0 

4.000 

5.300 

0 

0 

0 

0 

0 

1.500 

0 

10.000 

46 

0 

0 

0 

0 

0 

3,000 

4.300 

41488 26488 6400 8 II J 

0 

0 

8 

0 

'1.600 

'20,000 

•2.500 

"•420 

•4.200 

'16.000 

*9.300 

2,500 

0 

2468 

3.600 

4.000 

0 

4488 

3.500 

0 

1.400 

4.750 

0 2.450 

0 0 

0 3.000 

6 11488 

7468 

0 

30 

0 

0 

'34.000 

'25.000 

'53.000 

'152.000 

•se.ooo 

•9.000 

'89.000 

'68.000 

4

 46,000 

*43.600 

'32,600 

'46.000 

'eo.ooo 

3.500 

23.000 

9.000 

22.000 

0 

0 

0 

0 

2.300 

45.000 

11.600 

3.600 

0 

0 

0 

0 

0 

0 

6.400 

0 

0 

180 

0 

0 

0 

17..4O0 

12.000 

7.600 

See footnotes ai end of table. 
Table 3. 

Capacity of Operable Petroleum Refete ^ 

Crude Capacity Charge Capacity 

Refiner/State/ Location 

Barrels per 

Calendar Day 

Barrets per 

Stream Day 

Operating Operating 

Vacuum Catalytic Catalytic Catalytic • Catalytic 

Distilla- Thermal Cracking Cracking Catalytic Hydro- Hydration Operation (Fresh! {Recycled) Reforming cracking treating 

Production Capacity 

LubriIsomen eating Hydrogen Petroleum 

Alkyiation Asphalt Aromatics zation OHs (MMCFD) Coke 

Texae: GuH (continued) 

Charier International Oil Co. 

? 

5 0 

r 

O) 

% 

•8 "? fc 

a 

i 119 

• * V 

C 

I • " M 

«"•* 

? 

• 2 "•s 

3 

S 

I J» 

f fc 

a 'mlnlotrett 0 

3 

-Houston 

-Coastal States Petroleum Co. 

-Corpus Christi 

Conoco Inc.-Atvin/Texas City 

Crown Central Petroleum Corp. 

-Pasadena 

Exxon Co. U.S.A.-Baytown 

Gull Refining & Marketing Co. 

(Formerly GuH Oil Corp.) 

•Port Arthur 

Koch Refining Co.-Corpus Christi 

Marathon Petroleum Co. 

(Formerly Marathon Oil Co l 

-Texas City 

Mobil Oil Corp.-Beaumont 

Petromax Refining Co. Inc. 

-Channel-view (Houston)' 

Phillips Petroleum Co.-Sweeny 

Saber Refining Co.-Corpus Christi 

Shell Oil Co-Deep Park 

Southwestern Reiining Co. inc. 

-Corpus Christi 

Texaco Refining & 

Merketing Inc. 

IFormerty Texaco Inc.) 

-Port Arthur 

Texaco Refining & 

Marketing Inc. 

(Formerly Texaco Inc.) 

, -Port Neches 

rj-| Texas City Relining Inc. Texas City 

0 

ES7.500 

33.274 

100.000 

494.000 

328.500 

125.000 

49.000 

275,000 

0 

175.000 

0 

250.000 

104.000 

200.000 

0 

119.600 

65.-300 

0 

0 

0 

0 

78.400 

0 

20.500 

0 

2,000 

0 

0 

0 

0 

126.000 

31.000 

0 

0 

E95.000 

37.194 

103.000 

525.000 

338.000 

130.000 

50.000 

290.000 

0 

195.000 

0 

Z72.000 

106.000 

215.000 

0 

IX.000 

68.000 

0 

0 

0 

0 

80,000 

0 

22.000 

0 

2.500 

0 

0 

0 

0 

131,000 

32.600 

0 

26.000 

E48.000 

0 

38.000 

208.000 

203,200 

38.000 

28.000 

86.000 

0 

83.000 

24,000 

128.000 

36.000 

139.000 

26.000 

49.000 

"^.soo 

'"EH.OOO 

•E12.500 

0 

'E12.500 

0 

6

34.000 

•12.300 

- 0 

'29.500 

0 

0 

0 

••55.000 

•20,000 

0 

0 

0 

, 0 19.000 

SO.OOO 

E20.000 

0 

56.000 

155,000 

110.000 

29.500 

38.000 

102,000 

0 

87.000 

53,000 

60,000 

52,000 

135.000 

0 

40,000 

0 

0 

0 

0 

15.000 

6.000 

aoo 

1.000 

0 

0 

7.700 

2.650 

10.000 

0 

40. SOO 

0 

0 

' 13,500 

'E20.000 

0 

'36.000 

"60,00 0 

'63.000 

'67,'l00 

"27.00 0 

"8.00 0 

'103.000 

0 

'36.000 

0 

"40,00 0 

'15.000 

'30.000 

'60.000 

0 

"11.00 0 

'12.000 

0 

0 

0 

0 

19,000 

0 

0 

0 

32,000 

0 

0 

0 

15,000 

0 

15.000 

0 

0 

•1,500 

'28.000 

'14.500 

'E12.000 

'E25.000 

4E25,000 

'E12.000 

0 

'7,000 

'28,000 

*23.500 

'1-33.000 

'139.000 

'71,000 

•85.000 

'44,100 

'31.560 

'138,000 

'67.100 

"6.000 

'29,000 

0 

'116.000 

"92.000 

•5,660 

0 

'50,000 

'53.000 

'75,000 

'54,000 

'71.000 

'135,000 

8

102.000 

'27.000 

'40.000 

4

18.000 

'80.000 

'60,000 

'24,500 

0 

"29.000 

'23,000 

5.500 

E2.500 

0 

10.000 

29,000 

16,900 

6,000 

11.000 

13.000 

0 

10.500 

8.500 

8.176 

4.500 

9.000 

0 

6.200 

6.000 

E2.000 

0 

0 

7.000 

0 

0 

0 

0 

0 

0 

0 

4,900 

0 

0 

9.000 

0 

2.800 

El 1,000 

0 

2.000 

0 

4.595 

7.600 

2.500 

0 

0 

5,575 

0 

20.800 

6.500 

0 

0 

0 

0 

0 

0 

0 

0 

, 4 7.20 0 

0 

0 

"20.00 0 

0 

"16.90 0 

"12.00 0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

36.300 

13.200 

0 

0 

8.300 

0 

0 

0 

10.000 

0 

16,300 

0 

0 

0 

EIS 

0 

0 

85 

0 

0 

0 

60 

0 

80 

55 

71 

0 

0 

0 

0 

0 

E5.250 

0 

1.250 

5.800 

13.700 

2,(XX) 

0 

6.760 

0 

5.985 

0 

2.400 

0 

0 

0 

0 

See footnotes at end of table. 
Table 3. 

Capacity of Operable Petroleum Refineries by State as of January 1,1986 (Barrels per Stream Day, Except Where Noted) (continued) 

CTt 

Refiner/State/Location 

Crude Capacity 

Barrels per 

Calendar Day 

Operating 

Barrets per 

Stream Day 

Operating 

Charge Capacity 

Vacuum 

Distilla- Thermal 

tion -Operation 

Catalytic 

Cracking 

(Fresh) 

Catalytic 

Cracking Catalytic 

(Recycled) Reforming 

Catalytic Catalytic 

Hydro- Hydrocracking treating 

Production Capacity 

Afcytation Asphalt Aromatics 

Lubrifsomeri- eating 

zation Otis 

Hydrogen Petto-leu 

(MMCFD) Coke 

Texas: GuH (continued) 

J 

r 

t 

*-» 

a 

a 

•a 

tt 

! 

i 

I 

J 

a 

r 

Unocal Corp. 

(Formerly Union OH Co. of 

Califomial-Nedertand 

(Beaumont! 

Total 

Texas: Inland 

Amber Refining Inc.-Fort Worth 

American Petrofina Co. of Texas 

-Big Spring 

120.000 

3.3(2.674 

12.500 

60.000 

0 

222.600 

7.200 

0 

126.300 

3,672,4*4 

13,000 

66.000 

Chevron U.S.A. Inc.-EI Peso 

Damson Gas Processing Corp. 

(Formerly Dorchester 

Refining Co.) 

-White Deer (Cargray) 

Diamond Shamrock Refining & 

Marketing Co.-Sunray 

Diamond Shamrock Refining & 

Marketing Co. 

(Formerty Sigmor Corp.) 

-Three Rivers 

Flint Chemical Co-San Antonio 

Howell Hydrocarbons Corp. 

I Formerty Howell Corp. I 

-San Antonio 

La Gloria Oil & Gas Co.-Tyler 

Liquid Energy Corp.-Bridgeport 

Petrolite Corp.-Kilgore 

Phillips Petroleum Co. Borger 

Pride Refining Inc.-Abilene 

Shell Oil Co. Odessa 

Texaco Refining & 

Marketing Inc. 

(Formerly Texaco Inc.) 

-Amarillo 

El Paso 

Tropicana Energy Co.-Fort Worth 

lEulessI" 

Total 

Utah 

76.000 

79.000 

47,000 

1,500 

9.900 

46.000 

10.000 

1.000 

100.000 

42.750 

30.600 

20.000 

17.000 

Amoco Oil Co. Salt Lake City 40,000 

Chevron U.S.A. Inc. Salt Lake City 45.000 

Crysen Corp.-Woods 

Cross 

Morrison Petroleum Co.-Woods 

Cross" 

See tootnotes at end oi table. 

12.500 

0 

4.650 

661,260 11.660 

0 

6.000 

78,000 

0 

80.000 

49.500 

1,550 

10.000 

49.500 

10.800 

1.400 

105,000 

45.000 

33.500 

21,000 

18.000 

H I .260 

41,500 

46.000 

13.500 

0 

5.000 

12.600 

0 

7.000 

43.000 

0 54.000 0 

0 0 0 

0 45.000 *4.000 

20.000 

0 

0 

14.000 

0 

475 

0 

12.500 

10,500 

0 

164.676 

0 

35,500 

3,000 

0 

0 

'9.300 

0 

0 

0 

*4.000 

'4.000 

0 

s

8.pS00 

39.000 

-07.160 1,646.200 211,300 1,300.000 

7,500 3,500 0 3.600 

0 25.000 '°3,500 23.000 

22.000 

0 

45.000 

22.000 

0 

0 

15.000 

0 

0 

60.000 

0 

I0.-5O0 

8.000 

7.000 

0 0 

24,600 216,100 

18.000 

18.000 

"12.500 

'20.000 

130,660 622,166 

2,600 

0 

"1.700 

'20,000 

'25.000 

0 "1,000 

0 '18.000 

0 

0 

10.400 

0 

5.500 

2.400 

2.000 

'8.500 

0 

0 "1.200 

800 '20.000 

0 

0 

"7,000 

'19.000 

0 

'11.000 

'5,000 

'4,800 

0 0 

23,700 146,700 

4,000 '6.000 

1.000 '5.500 

'3.000 

0 

0 '10.600 4.200 

'32,500 

•tO.500 

164,000 2,764.110 2S2.47S 

9.000 

0 

0 

*5.000 

'15.000 

0 

0 

'40.000 

'26.500 

•50.000 

0 

•ll.OOO 

0 '5.000 

0 '4.800 

6.000 

0 

0 

4,700 

0 

0 

14.000 

0 

3.000 

1.500 

1.500 

0 0 

271,200 61,600 

*6.000 4.000 

'5.500 4,300 

'5.500 

2.400 

0 

0 

0 

*6.400 

•25,000 

'11,000 

*6.000 

'18.000 

'25,000 

300 

6,000 

5.500 

0 

5,500 

5,500 

0 0 0 0 

0 '20.500 9.000 4.000 

7.000 

0 

0 

0 

0 

125 

0 

0 

22.126 

13M76 

1.200 

0 

0 

350 

0 

0 

'3.000 

0 

'1.500 

0 0 

0 0 

0 "8 . tOO 

,424.600 

'2.000 

0 

0 

'500 

0 

36.700 

"1.400 

"750 

3.100 

1.000 

0 

0 

1,000 

646 66,146 

0 

0 

0 

0 

0 

20 

0 

0 

50 

0 

0 

0 

0 

0 

70 

0 

0 

0 

0 

0 

0 

0 

0 

0 

1.-S80 

0 

0 

3.900 

0 

0 

500 

500 

0 

6,660 

0 

1.750 

0 

0 
Table 3. 

Capacity of Operable Petroleum Refineries by State as of January 1,1985 (Barrels per Stream Day, Except Where Noted) (continued) 

Crude Capacity Charge Capacity Production Capacity 

Refiner/ State/ Location 

Barrels per 

Calendar Day 

Operating Idle 

Utah (continued) 

Phillips Petroleum Co -Woods Cross 25,000 

RMT Properties Inc. 

(Formerly Husky Oil Co.l 

-Salt Lake 

Seagull Refining Co. 

(Formerly Plateau Inc.l 

-Roosevelt 

Total 

Virginia 

Amoco Oil Co.-Yotktown 

Virginia Oil S. Refining Co. Inc. 

-Jonesville 

Total 

Washington 

25.000 

8.000 

166,600 

51.000 

1.000 

62,600 

0 

6,000 

Atlantic Richfield Co.-Ferndale 

(Cherry Pointl 

Chevron U.S.A. Inc. 

-Richmond Beach 

Crysen Corp. 

(Formerly Sound Refining 

Inc.l-Tacoma 

Mobil Oil Corp.-Femdale 

Shell Oil Co. Anacortes 

Texaco Refining & 

Marketing Inc. 

IFormerly Texaco Inc.) 

-Anacortes 

146.000 

5,500 

11,900 

71.500 

72,000 

78.000 

U.S. Oil & Refining Co.-Tacoma 26.400 

Total 411,300 

West Virginia 

Quaker State Oil Refining Corp. 

-Newell (Congol 

St Mary's (Ohio Vallayl 

Total 16.670 

Wisconsin 

Murphy Oil U.S.A. Inc.-Superior 39.000 

Banels per 

Stream Day LubriOperating 

Vacuum Catalytic Catalytic Catalytic Catalytic 

Distilla- Thermal Cracking Cracking Catalytic Hydro- Hydro- Isomeri- eating Hydrogen Petroleum 

tion Operation (Fresh) (Recycled) Reforming cracking treating Alkyiation Asphalt Aromatics zation Oils (MMCFD) Coke 

26.000 

26.000 

8.500 

161,600 

53.000 

1,000 

64,000 

150.000 

6.000 

12,754 

75,000 

75.000 

0 82.000 

0 28.500 

0 426,264 

3,200 

3.800 

17,600 

40.000 

0 

7,000 

0 87.000

 546,OO0 

6,000 

6.000 

20.000 

33.000 

8,400 2.600 '6.000 

4.400 2.500 '5.000 

'1.600 

'11.000 

•6,000 

0 0 6.000 SOO 0 

46,600 6,500 64,600 10,600 25,600 

28,000

 513.500 27,500 2,500 '8,750 

0 0 0 0 0 

26.000 13,600 27,600 2,600 6,760 

'46.000 49.000 

0 

25.500 

0 

2.000 

36.000 12,000 

0 

'11.800 

"20.000 

'31.000 

'17.000 

0 

'21.000 

'13.500 

'27,000 

'21,000 

•8.000 

2.100 1,700 

1.000 

0 

0 

0 

0 

0 

0 

35,000 

•9.000 

'15.500 

0 

24,500 

0 

11.400 

0 

0 

0 

0 

1,700 

0 

0 

0 

0 

5.900 

12.100 

5.000 

3.000 

0 

26,000 '13.000 30.0-30 9.000 '20,000 

17,000 0 0 0 '6.000 

116,000 S9.000 01.600 23,000 103,600 46.000 1M.300 24.600 16.700 

'17.000 6.600 0 

'20,000 

'5.000 

"6,000 0 8.700 

'3.800 

0 

2,160 

'2.900 

2.900 

1,676 

15,000 9.500 

3.760 

1.000 "8,000 

4,440 6.246 

'5,800 

'9.000 

1.600 13,600 

940 

0 

0 

2,660 

5.600 

0 

6^00 

79 11,000 

0 0 

0 3.900 

0 0 

76 14,600 

12.150 

4.520 

0 

0 

12.500 

6.000 

0 

0 

7.500 

E2.I75 

0 

0 

0 

0 

0 

0 

'2.150 

'1.600 

4.440 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

3.892 

1.357 

1 

0 

0 

0 

See f ootnoies at end at table. 
00 

Table 3. 

Capacity of Operable Petroleum Refineries by State as of January 1,1985 (Barrels per Stream Day, Except Where Noted) (continued) 

Crude Capacity Charge Capacity Production-Capacity 

Refiner/State/Location 

Barrels per 

Calendar Day 

Barrels per 

Stream Day 

Operating Operating 

Vacuum Catalytic 

Distilla- Thermal Cracking 

tion Operation (Fresh) 

Catalytic Catalytic Catalytic 

Cracking Catalytic Hydro- Hydro-

(Recycled) Reforming cracking treating Alkyiation Asphalt Aromatic tafia s 

0 

0 

0 

0 

0 

0 

0 

bomerii zation 

0 

0 

0 

"1,500 

0 

0 

1J60 

Lubricating 

Oils 

1.540 

0 

0 

0 

0 

0 

1,640 

Hydrogen 

(MMCFD) 

0 

0 

0 

0 

0 

0 

0 

Petroleum 

Coke 

0 

0 

0 

2.700 

1.000 

0 

3.760 

•o 

I 

3 

st 

| 

* 

a 

a 

s 

tt 

a 

Wyoming 

Amoco Ol Co.-Casper 

Little America Refining Co. 

-EvsnsviBe (Casper) 

Mountaineer Refining Co. Inc. 

-La Barge 

RMT Properties Inc. 

(Formerty Husky Oil Co.) 

-Cheyenne 

Sindair Oil Corp.-Sinclair 

Wyoming Refining Co.-Newcastle 

Total 

Guam 

Guam Oil & Refining Co. Inc. 

•Agana 

Puerto Rico 

48.000 

24,500 

360 

E33.600 

53.000 

12,555 

172.066 

0 

0 

0 

0 

0 

0 

0 

0 

49.000 

25.500 

750 

36.000 

54.000 

13.500 

177,760 

0 

0 

0 

0 

0 

0 

6 

16,400 

12.000 

0 

17.000 

30.000 

0 

76,400 

0 

0 

0 

*9,000 

0 

0 

6,000 

13.500 

10.500 

0 

12.000 

21,000 

4.000 

61,000 

2.700 

5.000 

0 

4,000 

1,000 

3.000 

16,700 

'6.000 

'6.000 

0 

'6.500 

"10,000 

"2.750 

31.260 

»7.100 

'3.700 

0 

'4,500 

•7.500 

•14.000 

'12,000 

0 

43,600 

1,700 

0 

0 

2.750 

3,500 

900 

43.900 47,160 

0 

4.400 

0 

6,000 

5.000 

0 

16,400 

350 

Gulf Refining & Marketing Co. 

(Formerly Gulf Oil Corp.) 

t 

•ak 

tt 

"•; 

? metl 

% Admlnl ttretlon 

San Juan (Bayamon) 

Phillips Puerto Rico Core Inc. 

-Guayama 

Sun Co. Inc.-Yabucoa 

Total 

Hawaiian Foreign Trade 

Zone 

Hawaiian Independent Refinery 

Inc.-Ewa Beach 

Virgin Islands 

Amerada Hess Corp. St Croix 

(E) - Estimated 

'Bi-Metallic 

'Other 

36.000 

0 

85.000 

121,000 

62.000 

395.000 

'Distillate 

'Gas Oil 

nna 1964. 

0 

0 

0 

0 

0 

150.000 

40.000 

0 

90.000 

130,000 

70,000 

430.000 

0 

0 

0 

0 

0 

165.000 

• 

20.000 

0 

48.000 

66.000 

30.000 

215.000 

'Relormer Feeds 

°Visbreaking 

0 

0 

0 

0 

0 

,o85,000 

14.000 

0 

0 

14.000 

0 

0 

'Heavy Gas Oil 

"C 

0 

0 

0 

0 

0 

0 

'6.500 

'52.070 

0 

60,570 

'13.000 

'115,000 

0 

0 

15.000 

16,000 

12,000 

0 

'11.000 

H.eoo 

•54.000 

'10,000 

61,600 

'13,000 

'166,000 

'125,000 

"•130.000 

"Delayed Coking 

"Fluid Coking 

0 

0 

0 

0 

0 

0 

1.000 

0 

0 

1,000 

0 

0 

11 

0 

14.560 

0 

14,660 

0 

0 

0 

0 

0 

0 

35.000 '"M5.000 

Naphthas 

Conventional 

0 

0 

6.900 

0.600 

0 

0 

0 

0 

18 

16 

17 

0 

'Residual 

"C'andC * 

0 

0 

0 

0 

0 

0 

Source: Form EIA-820. 
1 

1 

"6 

i 

a 

f 

3 

J 

• 

4 

a 

• s •c 

* 

•"Xa 

? 1 

a 

« 

3 

9 

2 r 

ik 

1 tn 

55* * 

m *% 

§ 

Table 4. 

Refiner's Operable Crude 0» Distillation Capacity as of January 1,1968 

Bane's Per 

Refiner Calendar Day 

Companies with Capacity 

Over 1OT.M0 B/CD 

Chevron Corp.' 

Chevron U.S.A. inc. 

El -Segundo, CaSfomia -406,000 

Richmond, Cailfomia 365.000 

PiMcngogiB, Mississippi 296,000 

Perth Ai-aboy, New JpS-rsey T88.000 

El Paso, Tewas ""6,000 

Honolulu, Hawaii 46.000 

Salt Lake City, Utah 45.000 

Bakersfield, California 26,000 

Kenai, Alaska 22,000 

Willbridge, Oregon 15,000 

Baltimore, Maryland 14,200 

Richmond Beach, Washington 5,500 

Total 1,p484,700 

Exxon Corp. 

Exxon Co. U.S.A. 

Baytown, Texas 494,000 

Baton Rouge, Louisiana 455,000 

Benicia, California 109,000 

Linden, New Jersey 100,000 

Billings, Montana 42,000 

Total - 1,200,000 

Texaco Inc. 

Texaco Refining 8P Marketing Inc.' 

Port Arthur, Texas 326,000 

Convent, Louisiana 225,000 

Delaware City, Delaware' 140,000 

Westville, New Jersey 90,000 

El Dorado, Kansas' 80,000 

Lawrenceville, Illinois 79,000 

Anacortes, Washington 78,000 

Wilmington, California 75,000 

Bakersfield, California* 38,000 

Port Neches, Texas 31,000 

Amarillo, Texas 20,000 

El Paso, Texas 17,000 

Total 1,199,000 

Shell Oil Co. 

Wood River, Illinois 250,000 

Deer Park, Texas 250,000 

Norco, Louisiana 218,000 

Wilmington, California 93,000 

-3 Martinez, California

 91-*,tJV 

Anacortes, Washington 72,000 

Odessa, Texas 30,600 

Total 1,005,000 

See footnotes at end of table. 

Refiner 

Standard Oil Co. of Indiana 

Amoco Oil Co. 

Texas City, Texas 

Whiting, Indiana 

Mandan, North Dakota 

Yorktown, Virginia 

Casper, Wyoming 

Salt Lake City, Utah 

Savannah, Georgia 

Total 

Gulf Oil Corp. 

Gulf Refining & Marketing Co.4. 

Port Arthur, Texas 

Belle Chasse (Alliance), Louisiana 

Philadelphia, Pennsylvania 

Cincinnati (Cleves), Ohio 

Total 

Atlantic Richfield Co. 

Houston, Texas 

Carson (Watson), California 

Ferndale (Cherry Point), Washington 

Philadelphia, Pennsylvania 

Prudhoe Bay (North Slope), Alaska 

Total 

Mobil Oil Corp. 

Beaumont, Texas 

Joliet, Illinois 

Torrance, California 

Paulsboro, New Jersey 

Ferndale, Washington 

Total 

U.S. Steel Corp. 

Marathon Petroleum Co.' 

Garyville, Louisiana 

Robinson, Illinois 

Texas City, Texas 

Detroit, Michigan 

Total 

Unocal Corp* 

Lemont (Chicago), Illinois 

Nederland (Beaumont), Texas 

Wilmington. California 

Rodeo (San Francisco), California 

Arroyo Grande (Santa Maria), California 

Total 

Barrels Per 

Calendar Day 

415,000 

360.000 

58.000 

51.000 

48.000 

40,000 

24,000 

986,000 

406,900 

198,500 

174,100 

43,700 

823,200 

260,000 

215,000 

146,000 

125,000 

22,000 

768,000 

275,000 

180,000 

123,500 

100,000 

71,500 

750,000 

255,000 

195,000 

69,500 

68,500 

588.000 

151,000 

120,000 

108,000 

70.000 

41,000 

490,000 
ro 

o 

Table 4. 

Refiner's Operable Crude OU Distillation Capacity as of January 1,1965 (continued) 

**» 

I I 

a 

I 

f 

r 

« 

3* 

**» 

a 

a 

Rpafiner 

Standard Oil Co. of Ohio 

Lima, Ohio 

Toledo, Ohio 

BP Oil Corp. 

Marcus Hook, Pennsylvania 

Total 

E. I. du Pont de Nemours & Co. 

Conoco, Inc. 

Westlake (Lake Charles), Louisiana 

Ponca City, Oklahoma 

BiVmgs. Montana 

Commerce City (Denver), Colorado 

Atvin/Texas City, Texas 

Santa-Maria, California 

Egan (Acadia), Louisiana 

Total 

Sun Co. Inc. 

Marcus Hook, Pennsylvania 

Toledo, Ohio 

Tulsa, Oklahoma 

Total 

Ashland Oil Inc. 

Catlettsburg, Kentucky 

St. Paul, Minnesota 

Canton, Ohio 

Freedom, Pennsylvania 

Total 

Southland Corp. 

Citgo Petroleum Corp 

Lake Charles, Louisiana 

Phillips Petroleum Co. 

Sweeny, Texas 

Borger, Texas 

Woods Cross, Utah 

Total 

Koch Industries 

Koch Refining Co. 

St. Paul(Rosemont), Minnesota 

Corpus Christi, Texas 

Total 

Union Pacific Corp. 

Champlin Petroleum Co. 

Corpus Christi, Texas 

Wilmington, California 

Total 

Barrels Per 

Calendar Day 

168,000 

120,000 

168,000 

456,000 

156,500 

134,000 

48.500 

41,500 

33,274 

9,500 

6,500 

429,774 

155,000 

118,000 

85,000 

358,000 

213,400 

67,143 

66„000 

6,800 

353,343 

320,000 

175,000 

100,000 

25,000 

300,000 

137,000 

125.000 

262,000 

157,000 

60.000 

217,000 

Refiner 

Tosco Corp. 

Martinez (Avon), California 

El Dorado, Arkansas 

Total 

Coastal Corp., The 

Coastal States Petroleum Co. 

Corpus Christi, Texas 

Pacific Refining Co. Inc. 

Hercules, California 

Derby Refining Co. 

Wichita, Kansas 

Total 

Kerr-McGee Corp. . 

Kerr-McGee Refining Corp.' 

Wynnewood, Oklahoma 

Dubach, Louisiana 

Cotton Valley, Louisiana 

Southwestern Refining Co. Inc. 

Corpus Christi, Texas 

Total 

American Petrofina Inc. 

American Petrofina Co. of Texas 

Port Arthur, Texas 

Big Spring, Texas 

Total 

Total Petroleum North America Ltd. 

Total Petroleum Inc. 

Ardmore, Oklahoma 

Arkansas City, Kansas 

Alma, Michigan 

Total 

Tenneco Oil Co. 

Chalmette, Louisiana 

Murphy Oil U.S.A. Inc. 

Meraux, Louisiana 

Superior, Wisconsin 

Total 

Earl Holding Co. 

Sinclair Oil Corp. 

Sinclair, Wyoming 

Tulsa, Oklahoma 

Little America Refining 

Evansville (Casper), Wyoming 

Total 

Barrels Per 

Calendar Day 

126,000 

47,000 

173,000 

87.500 

55.000 

28.800 

171,300 

43,000 

10,000 

7,800 

104,000 

164,800 

90,000 

60,000 

150,000 

62,000 

42,500 

40,000 

144,500 

133.000 

90,200 

39,000 

129,200 

53.000 

50.000 

24.500 

127.500 

See footnotes at end of table. 
Tabl

e 4. 

Refiner's Operable Crude Oil Distillation Capacity as of January 1,1965 (continued) 

f 

m 

% •o •? 

fc 

a 

a 

c 

a •a 

i 

« 

§ 

I 

Refiner 

Diamond Shamrock Corp. 

Diamond Shamrock Refining & Marketing Co. 

Sunray, Texas 

Three Rivers, Texas* 

Total 

Agway Petroleum Corp. 

Texas City Refining Inc. 

Texas City, Texas 

Mid America Pipe Line System 

Mapco Petroleum Inc. 

Memphis, Tennessee 

North Pole, Alaska 

Total 

Apex Oil Co. 

Clark Oil & Refining Corp. 

Blue Island, Illinois 

Hartford (Wood River), Illinois 

Total 

Total 

Companies with Capacity 

30,001 to 100,000 B/CD 

Crown Central Petroleum Corp. 

Pasadena, Texas. 

Amerada Hess Corp. 

Port Reading, New Jersey* 

Purvis, Mississippi 

Total 

Farmland Industries, Inc. 

Coffeyville, Kansas 

Phillipsburg, Kansas 

Total 

Louisiana Land & Exploration Co. 

Mobile, Alabama 

National Cooperative Refinery Association 

McPherson, Kansas 

United Refining Co.' 

Warren, Pennsylvania 

Vulcan Refining Co. 

Cordova, Alabama 

Total 

Barrels Per 

Calendar Day 

79,000 

47,000 

126,000 

H9.600 

60,000 

46,500 

106,500 

57,000 

47,500 

104,500 

13,939,917 

100,000 

68.000 

30,000 

98,000 

56,500 

26,400 

82,900 

80,000 

70.000 

60,000 

/ 

9,500 

69,500 

Refiner 

Paramount Petroleum Corp. 

Paramount, California

10 

Bakersfield, California" 

Total 

Charter Oil Co. 

Charter International Oil Co. 

Houston, Texas 

Pennzoil Co. Inc. 

Shreveport, Louisana" 

Rouseville, Pennsylvania 

Total 

RMT Properties Inc." 

Cheyenne, Wyoming 

Salt Lake, Utah 

Total 

Tesoro Petroleum Corp. 

Kenai, Alaska 

Texas Eastern Corp. 

La Gloria Oil & Gas Co. 

Tyler, Texas 

Placid Oil Co. 

Placid Refining Co. 

Port Allen, Louisiana 

Seaview Petroleum Inc. 

Paulsboro, New Jersey 

Rock Island Refining Corp. 

Indianapolis, Indiana 

Pride Refining Inc. 

Abilene, Texas 

Cirillo Brothers Oi! Co. 

Cibro Petroleum Products Inc. 

Albany, New York 

Triad Terminal Corp." 

Edgington Oil Co. Inc. 

Long Beach, California 

Cenex" 

Laurel, Montana 

Thrifty Oil Co. 

Golden West Refining Co. 

Santa Fe Springs, California 

Barrels Per 

Calendar Day 

46,500 

21,500 

68,000 

65,000 

46,200 

15,700 

61,900 

33,600 

25,000 

58,600 

48,500 

46,000 

45,000 

44,400 

43,200 

42,750 

41,850 

41,600 

41,450 

40,600 

See footnotes at end of table. 
ro 

ro 

? 

"f i. 

I i m 

e 

a 

• *. 

a 

a 

c 

a 

-* 

tt 

8 •c 

0 1 

^ a 

? >org\ -m. 

a 

i 1 ition A 

| 

5* 

8* 

5 a 

§ 

Table 4. i 

Refiner* Operable Crude OU Distiltation Capacity as of January 1,1965 (continued) 

Barrels Per 

Refiner Calendar Day 

Hunt Oil Co. 

Tuscaloosa, Alabama 33,500 

American Ultramar Ltd. 

Beacon Oil Co. 

Hanford, California 17,300 

Golden Eagle Refining Co. Inc. 

Carson, California 16,170 

Total 33,470 

Pester Refining Co. 

El Dorado, Kansas 33,250 

Holly Corp. 

Navajo Refining Co. 

Artesia, New Mexico 30,400 

Total 1,319,870 

Companies with Capacity 

10,001 to 30,000 B/CD 

Fletcher Oil & Refining Co. 

Carson, California 29,500 

Gary Energy Corp. 

Gary Refining Corp.'* 

Fruita, Colorado 15,200 

Bloomfield Refining Co." 

Bloomfield, New Mexico 13,700 

Total 28,900 

International Processors 

St. Rose, Louisiana 28,356 

Mobile Bay Refining Co. 

Chickasaw, Alabama 26,600 

Time Oil Co. 

U.S. Oil & Refining Co. 

Tacoma, Washington 26,p400 

Asamera Oil (US) Inc. 

Commerce City (Denver), Colorado 26,000 

Crysen Corp. 

Woods Cross, Utah 12.500 

Tacoma, Washington" 11,900 

Total 24.400 

San Joaquin Refining Co. Inc. 

Bakersfield, California 24,300 

Refiner 

Quaker State Oil Refining Corp. 

Newwell (Congo), West Virginia 

Bradford (Smethport), Pennsylvania 

St. Mary's (Ohio Valley), West Virginia 

Total 

Kern Oil & Refining Co. 

Bakersfield, California 

Pauley Petroleum Inc. 

Newhall Refining Co. Inc. 

Newhall, California 

Indiana Farm Bureau Cooperative Association 

Mount Vernon, Indiana 

Ergon Inc. 

Vicksburg, Mississippi 

Texas NAPCO Inc. 

St James, Louisiana 

E-2 Serv. Inc. 

Amber Refining Inc. 

Fort Worth, Texas 

Gladieux Refinery Inc. 

Fort Wayne, Indiana 

West Coast Oil Co. 

Oildale, California 

Giant Industries Inc. 

Giant Refining Co." 

Gallup (Ciniza), New Mexico 

MacMillan Petroleum Co. 

Signal Hill (Long Beach), California 

Norphlet, Arkansas 

Total 

VGS Corp. 

Southland Oil Co. 

Sandersville, Mississippi 

Lumberton, Mississippi 

Total 

Calcasieu Refining Co.**3 

Lake Charles, Louisiana 

See footnotes at end of table. 

Barrels Per > 

Calendar Day 

12,150 

6,700 

4,520 

23,370 

21,400 

21,400 

21,200 

20,600 

20,000 

19,700 

19,000 

19,000 

18,000 

11,000 

5,880 

16,880 

11,000 

5,800 

16,800 

14,000 
Table 4. 

Refiner's Operable Crude OU Distillation Capacity as of January 1,1965 (-continued) 

ro 

oo 

Refiner 

Huntway Refining Co. 

Benicia (Van Nuys), California" 

Wilmington, California 

Total 

Wyoming Refining Co." 

Newcastle, Wyoming 

World Oil Co. 

Sunland Refining Co. 

Bakersfield, California 

Flying J. Petroleum Inc. 

Cutbank, Montana 

Williston, North Dakota 

Total 

Total 

-Companies with Capacity 

10,000 B/CD or Less 

Mitchell Energy Corp.-

Liquid Energy Corp. 

Bridgeport, Texas 

Coastal Petroleum Refiners Inc." 

Bakersfield (Paloma), California 

Howell Corp. 

Howell Hydrocarbons Corp.'4 

San Antonio, Texas 

Gibson Oil & Refining Co. Inc. 

Bakersfield, California 

Moore & Munger Inc. 

Cross Oil & Refining Co. 

Smackover, Arkansas 

Thagard Oil Co. 

Lunday Thagard Oil Co. 

South Gate, California 

Anchor Gasoline Corp. 

Canal Refining Co. 

Church Point, Louisiana 

Linmar Ventures/Theo Davies 

Seagull Refining Co." 

Roosevelt, Utah 

Barrels Per 

Calendar Day 

7,300 

5,500 

12,800 

12,555 

12,000 

5,600 

5,000 

10,600 

513,761 

10,000 

10,000 

9,900 

9,500 

9,400 

8,100 

8,000 

8,000 

Refiner 

Lakeside Refining Co. 

Kalamazoo, Michigan 

Crystal Refining Co. 

Carson City, Michigan 

Total 

Laketon Refining Corp. 

Laketon, Indiana 

Allied Materials Corp. 

Stroud, Oklahoma 

Claiborne Gasoline Co. 

Lisbon, Louisiana 

Witco Chemical Corp. 

Bradford, Pennsylvania 

Montana Refining" 

Great Falls, Montana 

Thriftway Co. 

Farmington (Bloomfield), New Mexico 

Vicksburg Refining Inc. 

Vicksburg, Mississippi 

Morrison Petroleum Co. 

Woods Cross, Utah 

Somerset Refinery Inc. 

Somerset, Kentucky 

Kenco Refining Inc. . 

Wolf Point Montana 

Tropicana Energy Co. 

Fort Worth (Euless), Texas 

Nevada Refining Co. 

Tonopah, Nevada 

Young Refining Corp. 

Douglasville, Georgia 

Calumet Industries Inc. 

Calumet Refining Co. 

Princeton, Louisiana 

Oxnard Refinery 

Oxnard, California 

Barrels Per 

Calendar Day 

5,000 

3,000 

8,000 

7,900 

7,600 

7,500 

6,841 

6,300 

6,100 

6,000 

6,000 

5,500 

4,700 

4,650 

4,500 

4,500 

4,400 

4,000 

See footnotes at end of table. 
Table 4. 

Refiner's Operable Crude OH Distillation Capacity as of January 1,1965 (continued) 

? 

i 

ft 

e 

» 

a 

« 

m 

3 

D 

a 

f 

m i 

i 

3 

6 

a 

s 

fc 

I 

3" 

J 

Refiner 

Barrels Per 

Calendar Day 

Crystal Oil Co. 

Stephens, Arkansas 

B-T Energy Corp 

Louisville, Kentucky 

GNC Energy Corp. 

Greensboro, North Carolina 

Petromax Refining Co. Inc. 

Channelview (Houston), Texas 

Kentucky Oil & Refining Co. 

Troy, Indiana 

Betsy Lane, Kentucky 

Total 

Flint Chemical Co. 

San Antonio, Texas 

3.200 

3,000 

3,000 

2,000 

1,000 

600 

1,600 

1,500 

Refiner 

Barrels Per 

Calendar Day 

Motor Oils Refining Co." 

McCook, Illinois 

Petrolite Corp. 

Kilgore, Texas 

Virginia Oil & Refining Co. Inc. 

Jonesville, Virginia 

Mountaineer Refining Co. Inc. 

La Barge, Wyoming 

American Refining Group Inc. 

Indianola, Pennsylvania 

Total 

United States Total 

1,000 

1,000 

1,000 

350 

180 

185,221 

15,658,769 

'Formerly Standard Oil Co. of California 

'Formerly Texaco Inc. 

'Formerly Getty Refining 4 Marketing Co. 

"Formerly Gulf Oil Corp. 

•Formerly Marathon Oil Co. 

•Formerly Union Oil Co. of California 

'Formerly Kerr-McGee Corp. 

•Formerly Sigmor Corp. 

•Formerly Coral Petroleum Inc. 

'"Formerly Pacific Oasis Corp. 

"Formerly Independent Valley Energy Co. 

"Formerly Atlas Processing Co. 

"Formerly Husky Oil Co. 

•Refinery was reactivated during 1984. 

Source: Form EIA-820 

"Formerly Penn Central Energy Corp. 

"Formerly Farmers Union Central Exchange Inc. 

"Formerly Gary Western Co. 

"Formerly Plateau Inc. 

"Formerly Sound Refining Inc. 

"Formerly Giant Industries Inc. 

"Formerly CPI Oil & Refining Inc. 

"Formerly Huntway Refining Co. of Northern California 

"Formerly Hermes Products Co. 

"Formerly Coastal Petroleum Co. 

"Formerly Howell Corp. 

"Formerly Simmons Refining Corp. 

"Formerly Moreco Energy Inc. 
Table 5. 

Input/Production of Petroleum Products at Refineries and Gasoline Blendkig Plants by PAD District, 

Actual 1964 and -Projected 1965 Mid 1986 (Barrels Per Calendar Day) 

3 i i 

s 

0 

fc 

a 

a uel •m 994. 

S 

SumeL i ^ 

na 

3" 

? irmmt Ion Admlnlotrot 

Input/Production 

rnput 

Crude Oil Unci. Lease 

Condensate)' 

Low Sulfur 

Medium Sulfur 

High Sulfur 

Natural Gaa Plant Liquids 

Other Hydrocarbons 

Hydrogen / Alcohol 

Unfinished Oils (Nell 

Gasoline Blending 

Components (Net! 

Total Input 

Production 

Finished Motor Gasoline 

Finished Leaded 

Finished Unleaded 

Jet Fuel 

Naphtha-Type 

Kerosene-Type 

Kerosene 

Distillate Fuel Oil 

Residual Fuel Oil 

Asphalt and Road Oil 

Lubricating Oils 

Wax 

Petroleum Coke 

Special Naphthas 

Liquefied Petroleum Gases 

Al Other Products' 

Toul Production 

PAD District 1 

19B4 

1.106,948 

NA 

NA 

NA 

6.440 

2.049 

119.781 

15.757 

1,24*.l75 

586.961 

184,167 

402,784 

56,573 

21,770 

34.803 

8.115 

281,101 

121.268 

84.292 

19.383 

2.426 

36.202 

1,314 

38.943 

70..423 

1.30S.M2 

'Low Sulfur: 0.-50% and under by weight. 

Medium Sullur: 0.51% to 1.00% by weight. 

High Sulfur: Over 1 00% by weight. 

1966 

1.232.546 

712.071 

110.394 

410.080 

9,081 

6.081 

135.866 

20,970 

1.404,662 

664.298 

182.220 

482.078 

65.102 

21.400 

43.702 

11.556 

251,663 

184,063 

77,600 

24.651 

2.884 

32,634 

813 

45.683 

109.856 

1.470 ,* n 

1986 

1.179.071 

670,501 

108.600 

399.970 

8.618 

6.700 

129.079 

19.896 

1,343.314 

649,929 

154,439 

495,490 

64.463 

20,750 

43.713 

11.633 

249.469 

133.175 

78,513 

24.823 

2,980 

32.433 

825 

45.448 

108.239 

1,401 ,*30 

PADO'strictll 

1964 

2.761.049 

NA 

NA 

NA 

164.027 

6.590 

18.410 

17,237 

2.1*7,314 

1.685,251 

723.356 

961.896 

171.666 

31,628 

140.038 

23.508 

663.153 

70.932 

119,350 

26.290 

1,169 

100.292 

13.658 

75.929 

146,743 

3.0*7,M3 

1886 

2,846.666 

1,860,401 

164,077 

832.188 

111.432 

11,527 

20,562 

56.617 

3.IMM04 

1,728.568 

689.523 

1.039,045 

174,106 

30.347 

143.759 

30.620 

633.840 

72.959 

110.827 

29,301 

2.647 

76.198 

11.549 

78.701 

179.469 

3.MS.7K 

'includes finished aviation gasoline, miscellaneous products, petrochemical feedstocks and still gas 

NA = Not Available 

Note: Totals may not equal sum of components due to independent rounding. 

Source: 1984 Actual - Form EIA 810. 

1385, 1986 projections Form EIA-820 

1986 

2.824.399 

1,781,458 

167,110 

875.831 

109,413 

11,817 

34.476 

58.586 

3,03*.701 

1,731.068 

621.912 

1.109,157 

173,774 

30,930 

142,844 

32,738 

617,476 

72,260 

108.919 

29.657 

2,666 

77,571 

13.199 

81.263 

173.507 

3.114,00* 

PAD District III 

1984 

5.536.898 

NA 

NA 

NA 

281.525 

24.831 

231,066 

78.276 

4,161,6*6 

2,924.812 

1.121.970 

1.802.842 

569,724 

96,298 

473,426 

75.686 

1,244,448 

343.866 

97.508 

101.784 

8.180 

180.194 

35,052 

202.057 

609.844 

M*3,1 H 

1985 

5.660.259 

2.879.757 

339.942 

2,430.560 

374.366 

218.263 

194.162 

122,335 

t,6G*,376 

3.065,111 

1.102.808 

1,982,303 

609,645 

94.325 

515,320 

74.593 

1,298.132 

282.436 

102,031 

104,892 

9.912 

170.886 

39.930 

289,681 

694,137 

•.7*1 J M 

1986 

5.689,246 

2.815.328 

368.758 

2.515.159 

370.150 

221,299 

217,010 

111,468 

MOo.773 

3,112.461 

917.756 

2,194.706 

610.412 

92,632 

517.780 

81.8S8 

1,317.934 

310.852 

99.059 

110.520 

11.237 

173.968 

42.402 

303,271 

667,617 

«.*41.Bt1 

PAD District IV 

1984 

435.609 

NA 

NA 

NA 

15.705 

79 

-6.667 

1.224 

446.S51 

232.566 

133.770 

98.795 

37,420 

14.568 

22.852 

820 

118.549 

10.391 

24.221 

921 

631 

8.779 

74 

3.538 

17.563 

466,471 

1986 

438.074 

231.843 

75,384 

130.847 

15.006 

5.666 

-3.447 

6.619 

4*1,107 

234,138 

131.731 

102,405 

43.343 

16.335 

27.008 

1,568 

114.369 

14.032 

27,944 

1.050 

800 

6,145 

130 

7,372 

12.822 

4*3.701 

1986 

450.236 

240.663 

78,370 

131,212 

15.673 

5,217 

-2,930 

6,332 

474.627 

239.441 

132.143 

107,298 

51.899 

22.996 

28.904 

1.752 

118.602 

14.730 

27,331 

1.060 

800 

6.728 

130 

8.549 

12.288 

4*3,300 

PAD District V 

1984 

2,206,710 

NA 

NA 

NA 

32.363 

11.730 

58.609 

2.368 

2,310.770 

1,023,724 

407.866 

615.868 

296.647 

48.311 

248.336 

6.101 

382,331 

344,770 

60.801 

10.784 

1314 

113,481 

3,738 

42,101 

148,680 

•t.436,473 

1985 

2.315,566 

244.425 

512.142 

1.568.988 

27,664 

37.261 

-17.946 

10.640 

2J73.1S4 

1,051,349 

372,400 

678.949 

314.185 

46.966 

267.220 

9.038 

401.326 

325.462 

68.105 

22.820 

1,800 

96.560 

4.666 

36.416 

126.141 

2.4SM67 

1986 

2.374.945 

210.623 

B31.471 

1.632.861 

24,194 

48.618 

-36.360 

17.622 

2,<43J)1t 

1,077,192 

371,330 

705.862 

320.822 

47,311 

273.511 

9.594 

404.689 

339.836 

72,762 

24.820 

2.100 

99.066 

4.712 

35.903 

122.100 

2JM1,5K 

United States 

1984 

12.044.216 

NA 

NA 

NA 

500.060 

46,279 

421,189 

114,862 

13.12S£M 

6,463,303 

2,571.128 

3.882.175 

1,132.032 

212,576 

919.466 

114,230 

2,679.582 

891.227 

386.172 

159.161 

14.721 

438.948 

53.836 

362.568 

993.254 

13J71.S3* 

1985 

12.483,099 

5,918,497 

1,201.939 

5.362.663 

537.538 

278.787 

329.196 

217.181 

13^46^02 

6.763.462 

2.478.682 

4.284.780 

1,206,381 

209.372 

997.009 

127.375 

2.699.320 

878.952 

386.507 

182.714 

18,043 

384.423 

57.077 

457.853 

1.122.426 

14.2M.SS 

1986 

12.517.895 

5.718.563 

1.2-44.309 

5.566.023 

S28.048 

293.651 

341,875 

213.915 

13,*S6,3M 

6.810,092 

2.197.580 

4,612.512 

1,221.370 

214.618 

1,006.752 

137.575 

2,708,170 

870,853 

386.684 

190,870 

19.783 

389,766 

61.268 

474.434 

1.063.751 

14,354.C1« 

ro 

cn 
ro 

Table 6. 

Working Storage Capacity' at Refineries and Gasoline Bl<anding Plants by PAD District and State as of January 1,11 

(Thousand Barrels) 

*"T i 

i 

"•S fc 

a 1 

f 

! 

? 

fc I 

ai5 

District 

and 

Slate 

Delaware. Maryland 

Florida. Georgia 

Virginia 

New J-araey 

New York 

North Carolina 

Pennsylvania 

West Virginia 

PAD District 1 Total 

Illinois 

Indiana 

Kansas 

Kentucky, Tennessee 

Michigan 

Minnesota, Wisconsin 

Missouri. Nebraska 

North Dakota 

Ohio 

Oklahoma 

PAD District II Total 

Alabama 

Arkansas 

Louisiana 

Mississippi 

New Mexico 

Texas 

PAO District III Total 

Colorado 

Montana 

Utah 

Wyoming 

PAD District IV Total 

Alaska 

California 

Washington 

Other States' 

PAD District V Total 

United Stat** Total 

Crude 

Oil 

2.714 

2.285 

8.564 

595 

0 

9.934 

217 

24,30* 

7.131 

3.179 

2.815 

1.931 

1,148 

2.917 

0 

408 

2.556 

4,167 

2*461 

2,289 

1.376 

21.292 

3.870 

864 

49.252 

7*443 

401 

1.545 

1.342 

1.458 

4.74* 

1,085 

32.429 

7.396 

2,536 

43,44* 

1774*6 

Finished 

Leaded 

132 

294 

1.945 

297 

96 

1.987 

68 

*jn» 

3.381 

1.803 

2.733 

753 

495 

1.383 

285 

357 

1.341 

2.683 

15,214 

260 

104 

3,172 

696 

220 

10,812 

16.264 

452 

746 

711 

1,174 

3.0S3 

165 

5.287 

1.370 

161 

*,M3 

46,363 

Motor Gasoline 

Finished 

Unleaded 

686 

378 

2.456 

208 

22 

3.097 

47 

•4*2 

3.661 

2,106 

2.059 

861 

523 

870 

259 

265 

1.745 

2,375 

14,724 

326 

149 

4.565 

1.268 

157 

13.019 

11,4*4 

205 

412 

391 

678 

1,(M 

96 

7,262 

1,255 

87 

1,700 

61,4** 

Total 

817 

672 

4.400 

'505 

118 

5,084 

115 

11,711 

7.042 

3.909 

4,792 

1.614 

1.018 

2.253 

544 

622 

3.086 

5.058 

2M3 * 

586 

253 

7.737 

1.964 

377 

23.831 

34,74* 

657 

1,158 

1.102 

1.852 

4.7M 

261 

12,549 

2.625 

248 

is.tn 

*M4 * 

Gasoline 

Blending 

Components 

1,706 

483 

4.168 

60 

55 

2.281 

0 

•.752 

5.205 

3.248 

1.276 

468 

517 

634 

0 

576 

2.246 

3.080 

17,260 

585 

138 

9.462 

1.820 

648 

21,176 

3341* 

565 

1.670 

1.076 

1.403 

4,714 

561 

12.963 

2,219 

208 

16,161 

M.4M 

Middle 

Distillates 

2.623 

906 

9.598 

539 

47 

4.703 

95 

1*41* 

7.201 

5.536 

3.615 

1.299 

1.794 

2,797 

26 

769 

2.340 

5.150 

30,527 

612 

662 

15,694 

3,051 

688 

22.254 

42.161 

405 

1.334 

1,186 

1.661 

4,5** 

734 

8.306 

2.061 

227 

11427 

107,*01 

Residual 

Fuel Oil 

119 

396 

3.447 

t,454 

0 

2.712 

43 

1,171 

1.641 

2.514 

563 

584 

701 

863 

0 

73 

497 

704 

(.130 

864 

90 

8.196 

576 

126 

13,137 

224** 

738 

249 

451 

592 

2.030 

1.124 

13.652 

1.330 

671 

1*,777 

6*,0*7 

Products 

Asphalt 

and Road 

Oil 

722 

383 

914 

188 

0 

1.020 

0 

3.227 

1.971 

2.266 

962 

1.215 

861 

2,571 

0 

0 

910 

1,218 

11413 

481 

624 

1.359 

1.134 

426 

2.522 

•,64* 

460 

1.280 

211 

2,314 

4,256 

57 

3.223 

401 

570 

4,261 

30,242 

Lubricating Oils 

0 

0 

1.268 

0 

0 

2.3S3 

261 

3,*S2 

963 

570 

12 

155 

0 

0 

0 

0 

259 

899 

246* 

0 

126 

3.106 

0 

0 

8.463 

11.M4 

0 

0 

0 

33 

33 

0 

2.189 

0 

0 

2,1** 

20,*S* 

Propane/ 

Propylene 

489 

224 

247 

56 

0 

109 

0 

1.127 

1.145 

35 

2.667 

507 

1.152 

33 

13 

5 

591 

263 

•,411 

9 

2 

1.314 

55 

8 

6.025 

7,413 

4 

18 

140 

12 

174 

5 

326 

16 

16 

3*3 

15.4S* 

Butane/ 

Butylene 

33 

78 

389 

0 

0 

1,061 

0 

1,861 

907 

928 

362 

27 

-493 

84 

2 

28 

1,389 

404 

4,124 

12 

6 

5.371 

73 

21 

5.315 

10,7*1 

6 

168 

39 

122 

336 

19 

1.173 

150 

73 

1,41* 

1*,723 

Jet Fuel 

NaphthaType 

309 

35 

0 

138 

0 

441 

0 

•23 

0 

762 

0 

267 

63 

107 

0 

38 

223 

488 

1*4* 

285 

14 

499 

120 

301 

2,745 

34*4 

200 

127 

107 

114 

64* 

131 

1.229 

0 

106 

1,4*1 

•44 * 

KeroseneType 

0 

0 

1,527 

291 

0 

1.314 

0 

3.132 

1.898 

732 

273 

565 

26 

31 

0 

90 

567 

774 

444* 

275 

0 

3.742 

800 

113 

6.532 

11,4*2 

132 

268 

139 

183 

722 

298 

4.059 

1,118 

153 

642* 

264*0 

Al 

Other 

Products' 

1.454 

433 

7.855 

741 

3 

6.891 

0 

17477 

10.437 

5.054 

3.930 

1.731 

1.729 

901 

0 

45 

4.105 

4.918 

32460 

250 

4 

17.454 

643 

612 

67,662 

M.82S 

503 

1.123 

606 

1.129 

34*1 

146 

19.432 

2.171 

52 

21401 

1*2,014 

Total 

Products 

7.464 

2.937 

29.413 

3.469 

106 

22,875 

399 

7*4*3 

31.368 

21.644 

13.660 

6.818 

7.328 

8.011 

41 

1.624 

13.117 

17.898 

161,446 

3.373 

1.666 

66.186 

8.272 

2.843 

156.831 

77240* 

3,003 

6.237 

3.956 

7.563 

25427 

3,075 

66.561 

9.466 

2.076 

••461 

•254*6 

Total Crude 

OH and 

Products 

10.986 

5.894 

42,377 

4.569 

223 

37.893 

731 

1*2472 

45.641 

28.732 

21.267 

10.363 

9.492 

13.181 

586 

2.654 

18.758 

27.123 

1774** 

6.248 

3.285 

95.215 

14.106 

4.084 

228.914 

3*1462 

4.061 

8.940 

6.399 

10.873 

30473 

4.421 

111.529 

19.487 

4.860-

1404*7 

"WZ.TS* 

'Working Storage Capacity - the difference in volume between the maximum safe fill capacity and tank bottoms. 

3

 A It Other Products includes ethane/ethylene, isobutane, pentanes plus, other hydrocarbons, hydrogen, alcohol, unfinished oils, finished aviation gasoline, special naphthas, wax, petroleum coke, still gas, 

petrochemical feedstocks and miscellaneous products. 

Hawaii, Nevada and Oregon. 

4

Includes 50,272 thousand barrels storage capacity at shutdown refineries. 

Source: Form EIA-820. 
p 

1 

I 

i i 

• 

i 

> 

t 

w 

1 

1 

i 

Q 

a k. 

5 

1 

1 •m 

*+ 

J 

J 

1 Admlnim <ral r 

Table 7. 

Shell Storage Capacity' at Refineries and Gasoline Blendlno Plants 

(Thousand Barrels) 

District 

and 

State 

Delaware, Maryland 

Florida, Georgia 

Virginia 

New Jersey 

•New York 

North Carolina 

Pennsylvania 

West Virginia 

PAD District 1 Total 

Illinois 

Indiana 

Kansas 

Kentucky, Tennessee 

Michigan 

Minnesota, Wisconsin 

Missouri. Nebraska 

North Dakota 

Ohio 

Oklahoma 

PAD District 11 Total 

Alabama 

Arkansas 

Louisiana 

Mississippi 

New Mexico 

Texas 

PAD District III Total 

Colorado 

Montana 

Utah 

Wyoming 

PAD District IV Total 

Alaska 

California 

Washington 

Other Slates3 

PAD District V Total 

United States Total 

Crude 

Oil 

3.182 

2,647 

10.035 

694 

0 

11,623 

278 

2S.46* 

8,387 

3.694 

3.070 

2.066 

1,221 

3.252 

0 

482 

2.851 

4.775 

29,7*8 

2.657 

1.532 

26.222 

4.304 

986 

57,991 

•3,6*2 

462 

1,737 

1,549 

1.560 

6.30* 

1.151 

38.016 

8.448 

2.S8S 

60403 

207.4*0 

Finished 

Leaded 

156 

344 

2.280 

313 

107 

2.222 

87 

640* 

3.997 

1.997 

2.927 

797 

531 

1.489 

291 

428 

1.505 

2.899 

1*4*1 

315 

116 

3.815 

763 

269 

12.260 

1743* 

488 

818 

809 

1.331 

3,44* 

177 

6.042 

1.498 

173 

7410 

51444 

1

 Shell Storage Capacity - the design capacity of the tank. 

*AH Other Products includes ethane/ethylene. 

petrochemical feedstocks and mis 

Hawaii, Nevada and Oregon. 

4

lnckjdes 54.563 thousand barrels 

Source: Form EIA-820 

ro 

Motor Gasoline 

Finished 

Unleaded 

774 

443 

2.960 

219 

24 

3,485 

56 

74*1 

4.388 

2,401 

2.217 

916 

556 

956 

260 

333 

1.980 

2.572 

1*47* 

378 

166 

5,734 

1,425 

194 

14.813 

22.710 

227 

458 

446 

764 

14*6 

101 

8.435 

1.423 

33 

10,062 

St.lM 

Total 

930 

787 

5.240 

532 

131 

5.707 

143 

13,470 

8.385 

4.398 

5,144 

1.713 

1.087 

2.444 

551 

761 

3.485 

5,471 

33,43* 

693 

282 

9.549 

2.188 

463 

27.073 

4044* 

715 

1,276 

1,255 

2.095 

5441 

278 

14,477 

2.921 

406 

17442 

110,440 

isobutane, pentanes plus, other hydrocarbons 

cellaneous products. 

storage capacity at shutdown refineri-ss. 

Gasoline 

Blending 

Components 

2,050 

592 

4,930 

62 

56 

2.580 

0 

10470 

6.054 

3.702 

1.441 

498 

561 

675 

0 

961 

2.515 

3.247 

1»,*64 

680 

148 

11.853 

1.933 

722 

24,670 

3*.M* 

613 

1,835 

1,230 

1.597 

S.275 

591 

14.816 

2.508 

223 

11,13* 

•3,243 

by PAD District and State a* 

Middle 

Oistillates 

3.139 

1.045 

10.540 

573 

52 

5.096 

122 

20,66* 

7.828 

6.153 

3.859 

1.389 

1.894 

2.932 

28 

1.068 

2.526 

5.495 

33,1*2 

731 

704 

17.600 

3.291 

661 

24.799 

47,786 

426 

1,457 

1.350 

1.781 

5.014 

768 

9.367 

2.261 

242 

1243* 

ii*.ia * 

Residual 

Fuel oa 

131 

473 

3.898 

1,551 

0 

3.008 

63 

*,124 

1.754 

2.747 

621 

621 

742 

913 

0 

85 

530 

750 

8,7*3 

1.024 

100 

9.015 

631 

141 

15.320 

21.231 

775 

269 

505 

634 

2.1*3 

1,172 

15.006 

1.446 

695 

1*41* 

*4,*20 

Products 

Asphalt 

and Road 

Oil 

835 

406 

1,013 

221 

0 

1.178 

0 

3463 

2,106 

2,448 

1,022 

1.293 

889 

2,756 

0 

0 

965 

1.307 

12.7*4 

610 

692 

1.607 

1.233 

447 

2,797 

74** 

466 

1,394 

234 

2.525 

441 * 

59 

3.595 

424 

599 

4477 

33,121 

hydrogen, alcohol, unfinished oils, finished aviation gaso 

of January 1,1966 

Lubricating Oils 

0 

0 

1.318 

0 

0 

2.393 

281 

3412 

996 

630 

12 

163 

0 

0 

0 

0 

266 

942 

3.00* 

0 

138 

3,396 

0 

0 

9.304 

1243* 

0 

0 

0 

37 

37 

0 

2.345 

0 

0 

2446 

22421 

Propane/ 

Propylene 

579 

239 

302 

61 

0 

115 

0 

14»* 

1.263 

39 

2.672 

534 

1.395 

38 

15 

6 

640 

274 

•47 * 

10 

2 

1.357 

58 

9 

6.987 

•.423 

4 

19 

155 

13 

1*1 

5 

364 

18 

21 

40* 

17,1*4 

ine. special naphthas, wax 

Butane/ 

8utytene 

36 

89 

494 

0 

0 

1.077 

0 

1.*M 

962 

988 

470 

28 

580 

85 

2 

38 

1.470 

421 

6,044 

15 

7 

5.636 

77 

23 

6.145 

11403 

6 

176 

56 

126 

3*4 

20 

1.274 

157 

86 

1437 

20.644 

Jet Fuel 

NaphthaType 

368 

36 

0 

144 

0 

482 

0 

1431 

0 

856 

0 

286 

70 

114 

0 

43 

235 

546 

2,160 

350 

15 

563 

141 

337 

3.197 

4,M3 

212 

144 

135 

122 

•13 

139 

1.457 

0 

108 

1.704 

10.100 

petroleum coke, still gas. 

KeroseneType 

0 

0 

1,684 

306 

0 

1,512 

0 

3.602 

2,059 

866 

289 

646 

28 

33 

0 

103 

805 

862 

6,4*0 

325 

0 

4,209 

900 

127 

7.534 

13,0*6 

142 

295 

176 

199 

(12 

311 

4,570 

1.237 

157 

•476 

2S.1M 

All 

Other 

Products* 

1.729 

510 

8.853 

780 

3 

7.663 

0 

1143* 

11.653 

5.779 

4.310 

1.823 

1.816 

976 

0 

68 

4.546 

5.380 

3*461 

265 

5 

20.680 

699 

677 

76.647 

M473 

549 

1,260 

661 

1.280 

3.760 

153 

22.638 

2.509 

56 

2646* 

1*34«* 

Total 

Products 

8.867 

3.390 

33.032 

3.698 

111 

25.106 

466 

M.140 

34,675 

24.207 

14.696 

7.281 

7.975 

8.522 

45 

2.362 

14.298 

19.214 

1M.714 

4.010 

1.811 

75.916 

8.963 

3.144 

177.300 

3114*2 

3.193 

6.849 

4.502 

8.314 

2I.1M 

3,218 

75,432 

10.560 

2.187 

10*431 

703.7*4 

Total Crude 

Oil and 

Products 

12,979 

6.824 

48.307 

4.924 

242 

42.436 

887 

114.SSS 

51.447 

32.299 

22.910 

11.060 

10.283 

14.218 

596 

3.605 

20.634 

29.460 

19*412 

7.360 

3,625 

111.687 

15.455 

4.593 

262.364 

406,0*4 

4.370 

9.862 

7.306 

11.969 

33,607 

4.647 

127.925 

21.929 

5.041 

1SS.S42 

*»11444 
s 

i 

JT 

ro 

oo 

Table 8. 

Operable Capacity of Petroleum Refineries, January 1,1981 to January 1,1966 

(Barrels per Stream Day, Except Where Noted) 

Charge Capacity Production Capacity 

PAD 

District 

Crude 

0*3 (illation 

Vacuum 

Distillation 

Thermal 

Operation 

Catalytic 

Cracking 

(Fresh) 

Catalytic 

Cracking 

(Recycled) 

Catalytic 

Reforming 

Catalytic 

Hydrocracking 

Catalytic 

Hydrotreating Alkyiation Asphalt Aromatics 

Isomerization 

Lubricating Oils Hydrogen Petroleum 

(MMCFD) Coke 

? 

I 

•v? 

a 

a 

V 

e 1 

As of January 1. 1981 

As of January 1.1982 

As ot January 1,1983 

As of January 1. 1984 

As of January 1. 1985 

As of January 1. 1966 

Projected Net Change 

PAD District I 

Projected Net Change 

PAO District II 

Projected Net Change 

PAO Oistrict III 

Projected Net Change 

PAD District IV 

Projected Net Change 

PAD District V 

Projected Net Change 

19.763,212 

19.018.024 

17.870,694 

17.069.205 

16.504.465 

16.387.892 

-116.573 

1.676.700 

0 

3,349.103 

-160.000 

7.527,389 

-J3.720 

603,500 

0 

3,231,200 

57.147 

7.033.094 

7,197,190 

7.180.258 

7.166.470 

6.997.925 

6.959,925 

-38.000 

826.975 

0 

1.270.380 

-40,100 

3.110,020 

2.000 

199.150 

0 

1.553,400 

100 

1,587,100 

1.781,600 

1.715.400 

1.851.8X 

1.868,200 

1.835.900 

-22.300 

102.000 

0 

344.500 

0 

818,500 

-16.000 

31,700 

0 

539,200 

-6.300 

5.542.500 

5.473.600 

5.402.400 

5.310.250 

5.231.750 

5.200.750 

-31.000 

621.800 

0 

1.195.500 

-39.000 

2.501,100 

7,000 

191.900 

1.000 

690,450 

0 

593.665 

562.296 

488.225 

491,575 

506,575 

•494,175 

-12,400 

71.800 

0 

127.300 

-10.000 

211.125 

-2.400 

33.900 

0 

50.050 

0 

4.097.912 

3.966.260 

3.917.675 

3.907.450 

3.749,850 

3.704.750 

-45,100 

401,470 

0 

865.800 

-43.400 

1.683.000 

-3.400 

118.150 

1.200 

646.330 

SOO 

909.230 

892. I X 

883.130 

961.830 

1.053.430 

1.054,930 

1.500 

78.440 

0 

156.690 

0 

397,700 

0 

10.900 

0 

411.200 

1.500 

8.486.921 

8.539.385 

8.354.422 

9.009.478 

8.896.636 

8,908.536 

11.900 

1.026.636 

3.500 

1,702.750 

3.900 

4,473,710 

11.800 

226.200 

-7.300 

1.479.240 

0 

973.520 

984.380 

960.050 

944.780 

917.405 

931,705 

14.300 

74.500 

3,000 

251.200 

9,400 

443.076 

1.900 

31.130 

0 

131.800 

0 

764.879 

740,339 

721,636 

799.839 

766.913 

767.588 

675 

240.830 

-2.700 

194.941 

775 

36.000 

0 

127,933 

2.600 

237.042 

218.476 

214,551 

221.751 

7.200 

12.672 

0 

42.245 

0 

163.334 

7.200 

0 

0 

3.500 

0 

130.570 

161.920 

212.000 

208.400 

218.800 

237.300 

18.500 

25.000 

0 

64.800 

500 

122.800 

18.000 

8.100 

0 

16.600 

0 

234.022 

241.896 

241.058 

240.655 

242.539 

242.159 

-380 

40.049 

0 

36.400 

0 

137.770 

-380 

1.540 

0 

26.400 

0 

2.054 

1.956 

2.298 

2.444 

2.572 

2.608 

36 

101 

0 

187 

39 

1.275 

- 3 

27 

0 

1.018 

0 

276.005 

267.025 

295.780 

407.262 

423,553 

426.713 

3.160 

33.475 

0 

84.285 

2,710 

186.970 

-500 

10,990 

0 

110.993 

950 

? 

•a 

Source: Form EIA-820. 
fc 

r 

"f 

t 

3 

Table 9. 

Refinery Crude Oil Distillation Capacity and Utilization, by Month, 1964 

(Thousand Barrels per Day, Except Where Noted) 

District January February March April May June 

Yearly 

July August September October November December Averages 

I 

m 

% 

«•*. 

a a e a 

• 

e 

a 

PAD District I 

Operating 

Idle 

PAD District II 

Operating 

Idle 

PAD District III 

Operating 

Idle 

PAD District IV 

Operating 

Idle 

PAD District V 

Operating 

Idle 

United States Total 

Operating 

Idle 

Gross Input 

Operating Ratio' 

(percent) 

1,578 

1.-409 

169 

3,485 

3,281 

205 

7,391 

6,760 

631 

557 

529 

28 

3,125 

2,859 

266 

16,137 

14,838 

1,299 

11,767 

72.9 

1.578 

1,370 

209 

3,485 

3,254 

231 

7,387 

6,742 

645 

557 

529 

28 

3,136 

2,783 

354 

16,144 

14,678 

1,466 

12,276 

76.0 

1,578 

1,379 

199 

3,485 

3,299 

186 

7,387 

6,722 

665 

557 

529 

28 

3,106 

2,861 

245 

16.114 

14,791 

1,323 

12,071 

74.9 

1,578 

1,030 

548 

3,486 

3,291 

195 

7,387 

6,759 

628 

565 

481 

84 

3,106 

2,834 

272 

16,123 

14,396 

1,727 

12,077 

74.9 

1,578 

1,257 

321 

3.486 

3,163 

323 

7,348 

6,824 

523 

558 

530 

28 

3,099 

2,876 

223 

16,068 

14,650 

1,419 

12,437 

77.4 

1,578 

1,367 

211 

3,-486 

3,247 

239 

7,348 

6,918 

430 

558 

530 

28 

3,099 

2,903 

196 

16,069 

14,964 

1,104 

12,418 

77.3 

1,578 

1,367 

211 

3,502 

3,274 

228 

7,348 

6,660 

688 

558 

530 

28 

3,099 

2,864 

235 

16.085 

14,695 

1,390 

12,176 

75.7 

1,578 

1,412 

166 

3,502 

3,148 

353 

7,341 

6,736 

606 

558 

530 

28 

3,060 

2.875 

186 

16,040 

14,700 

1,339 

12,535 

78.2 

1,578 

1,412 

166 

3.490 

3,132 

358 

7,308 

6,715 

594 

558 

530 

28 

3.060 

2.848 

213 

15,994 

14,636 

1,359 

12,475 

78.0 

1,579 

1,410 

169 

3,491 

3,062 

429 

7,331 

6.498 

833 

568 

540 

28 

3,061 

2,849 

213 

16,031 

14,359 

1,672 

12,151 

75.8 

1,582 

1,413 

169 

3,491 

3,164 

327 

7,211 

6,398 

814 

568 

540 

28 

3,023 

2,841 

181 

15,875 

14,356 

1,520 

12,256 

77.2 

1,582 

1,413 

169 

3,444 

3,130 

314 

7,137 

6,513 

624 

560 

540 

20 

3,023 

2,783 

239 

15,746 

14.379 

1,367 

11,968 

76.0 

1,579 

1,353 

226 

3,486 

3,204 

282 

7,327 

6,687 

640 

560 

528 

32 

3,083 

2,848 

235 

16,036 

14,620 

1.415 

12,217 

76.2 

'Represents gross input divided by operable capacity, at the beginning of the month. 

Note: Total may not equal sum of components due to independent rounding. 

Source: Form EIA-810. 

ro 
GO 

o 

Table 10. 

Refineries Shutdown During 1964 

District/Refinery Location 

Crude 

Distillation 

Capacity 

(B/CD) 

Total 

Downstream 

Capacity 

(B/SD) 

Date 

of Last 

Operation 

Date 

Shutdown 

Years in 

Operation 

PAD District I 

Ashland Oil Inc. Buffalo

, New York 64,000 106,500 7/82 12/84 36H 

I 

m 

% 

*o_ 

fc 

a 

a 

s tt tt 4k •a 

tt 

PAD District II 

Ashland Oil Inc. 

Ashland Oil Inc. 

Oklahoma Refining Co. 

Oklahoma Refining Co. 

Tonkawa Refining Co. 

Tosco Corp. 

Total 

PAD District III 

Caribou-Four Corners Inc. 

Celeron Oil & Gas Co. 

Dorchester Refining Co. 

Eddy Refining Co. 

Hill Petroleum Co. 

Mid-Gulf Energy Corp. 

Port Petroleum Inc. 

Quintana Petrochemical Co. 

South Hampton Refining Co. 

Southern Union Refining Co. 

Tesoro Petroleum Corp. 

Warrior Asphalt Co. 

Total 

PAD District IV 

Caribou-Four Corners Inc. 

Findlay, Ohio 

Louisville, Kentucky 

Cyril, Oklahoma 

Thomas, Oklahoma 

Arnett, Oklahoma 

Duncan, Oklahoma 

Farmington, New Mexico 

Mermentau, Louisiana 

Mt. Pleasant, Texas 

Houston, Texas 

Krotz Springs, Louisiana 

Ingleside, Texas 

Stonewall, Louisiana 

Corpus Christi, Texas 

Silsbee, Texas 

Lovington, New Mexico 

Carrizo Springs, Texas 

Holt, Alabama 

Woods Cross, Utah 

20,400 

25,200 

12,750 

11,600 

12,000 

47,000 

128.960 

2.200 

11,000 

26,500 

3,250 

57,400 

39,400 

3,200 

33,300 

18,100 

36,100 

26,100 

5,500 

262,060 

8,000 

29,000 

23,100 

0 

6,000 

85,000 

151,100 

2,400 

0 

38,800 

0 

62,000 

20,000 

0 

54,000 

28,000 

18,500 

3,500 

2,000 

229,200 

2/82 

4/82 

12/84 

12/84 

6/84 

6/83 

5/82 

2/83 

9/84 

10/84 

9/84 

10/83 

12/83 

7/84 

12/82 

8/84 

7/84 

8/83 

12/84 

12/84 

12/84 

12/84 

9/84 

12/84 

8/84 

8/84 

12/84 

11/84 

11/84 

5/84 

2/84 

9/84 

12/84 

11/84 

12/84 

12/84 

36 + 

36+ 36 + 

4 

16 35 19 

6 

36 + 

36 + 

6 

6 

4 

30 24 

8 

27 30 

8,400 8.200 12/82 12/84 

21 

! 

fc 

I 3* 5" 

5 

I 

PAD District V 

Anchor Refining Co. Inc. 

ECO Petroleum Inc. 

Marlex Oil & Refining Co. 

Powerine Oil Co. 

Tosco Corp. 

U.S.A. Petrochemical Corp. 

Total 

United States Total 

McKittrick, California 

Long Beach, California 

Los Angeles, California 

Santa Fe Springs, California 

Bakersfield, California 

Ventura, California 

9,000 

0 

21,100 

44,120 

38,800 

24,000 

137,020 

600,420 

7,000 

7,000 

0 

100,100 

80,000 

7,000 

201,100 

696,100 

11/82 

7/81 

1/84 

6/84 

11/83 

12/84 

2/84 

3/84 

3/84 

8/84 

11/84 

12/84 

6 

8 

7 34 33 

7 

B/CD = Barrels per Calendar Day. 

B/SD = Barrels per Stream Day. 

Source: Form EIA-820. 
Table 11. 

mw ana n*ac uvatsu nnmn H uunny iiw 

District/Refinery Location 

Crude Distillation 

Capacit* 

B/CD 

Operating Idle 

Total 

Downstream 

Capacity 

B/SD 

Date 

of Last 

Operation 

Date 

Operable 

NEW 

PADDtstrictl 

Virginia Oil & Refining Co. Inc. 

REACTIVATED 

PAD District I 

Amerada Hess Corp. 

United States Total 

Jonesville, Virginia 

Port Reading, New Jersey 

1.000 

0 

1.000 

68.000 

68,000 

75,000 

75,000 

12/74 

12/84 

12/84 

B/CD = Barrels per Calendar Day. 

B/SD - Barrels per Stream Day. 

Source: Form EIA-820. 

i 

7 I 

fc I 

3* 

s-

? 

! 
Tabl

e 12. 

Refineries Shutdown since January 1,1961 

ro 

District/Refinery Location 

Crude 

Distillation 

Capacity 

(B/CD) 

15,000 

64.000 

11,900 

13,400 

5.600 

28.400 

43.000 

0 

15,000 

196,300 

104,000 

104,000 

20,400 

25,200 

53,800 

23,500 

5,600 

1,200 

20,000 

9,500 

126,000 

1,000 

50,300 

19,000 

5,000 

7,600 

3,000 

50,000 

5,000 

12,750 

11,600 

25,000 

80,000 

72,000 

11,500 

12,000 

47,000 

1,800 

907,750 

Total 

Downstream 

Capacity 

(B/SD) 

0 

106.500 

0 

0 

2,000 

0 

67,000 

2,980 

10.000 

188,480 

185,500 

127,000 

8,000 

29,000 

58,500 

25,700 

3,650 

0 

0 

0 

190,000 

0 

61,800 

12,150 

0 

0 

1,800 

83,900 

0 

23.100 

0 

13.200 

156.700 

136,000 

3,200 

6,000 

85,000 

1,800 

1,212,000 

Date 

of Last 

Operation 

1/82 

7/82 

7/81 

7/81 

12/82 

5/81 

5/81 

12/83 

12/81 

5/82 

5/81 

2/82 

4/82 

6/83 

5/81 

5/82 

1/81 

5/80 

4/81 . 

5/81 

2/81 ' 

6/81 

12/82 

12/80 

12/81 

3/81 

9/83 

2/81 

12/84 

12/84 

6/82 

8/82 

4/81 

9/81 

6/84 

6/83 

2/81 

Date 

Shutdown 

3/82 

12/84 

12/81 

12/81 

12/82 

10/81 

7/81 

12/83 

4/82 

-6/82 

10/81 

12/84 

12/84 

12/83 

9/81 

6/82 

2/82 

9/81 

2/82 

6/82 

4/81 

11/81 

11/83 

2/81 

6/82 

7/82 

9/83 

2/82 

12/84 

12/84 

12/82 

9/82 

10/81 

2/82 

9/84 

12/84 

3/81 

Years in 

Operation 25 + 36 + 

8 

7 25 + 

2 

25 + 

25 + 

25 + 

25+ 25 + 36 + 36 + 25 + 

5 

25 + 

4 

25 + 

25 + 

25 + 

22 25 + 

6 

23 25 + 25 + 25 + 

7 

36 + 

4 

25 + 

25 + 

25 + 25 + 16 35 25 •» 

sr 

o 

I 

fc 

a i 4k 

I 

? 

« 

a f 

I 

fc I 

3 5* 

PAD District I 

Amoco Oil Co. 

Ashland Oil Inc. 

ATC Petroleum Inc. 

ATC Petroleum Inc. 

Elk Refining Co., div. 

of Pennzoil Co. Inc. 

Manatee Energy Co. 

Mobil Oil Corp. 

Quaker State Oil 

Refining Corp. 

Seminole Refining Inc. 

Total 

PAD District II 

Amoco Oil Co. 

Amoco Oil Co. 

Ashland Oil Inc. 

Ashland Oil Inc. 

Champlin PetroleUm Co. 

Conoco Inc. 

CRA, Inc. 

Dillman Oil Recovery Inc. 

Dow Chemical U.S.A. 

E2 Serv Refining Inc. 

Energy Cooperative Inc. 

Energy Development 

Gulf Oil Corp. 

Hudson Refining Co. Inc. 

Indiana Refining Inc. 

Industrial Fuel & Asphalt of Indiana Inc. 

Mid-America Refining Co. 

Inc. 

Mobil Oil Corp. 

Northland Oil & Refining 

Co. 

Oklahoma Refining Co. 

Oklahoma Refining Co. 

Okmulgee Refining Co. 

Phillips Petroleum Co. 

Texaco Inc. 

Texas American 

Petrochemical Inc. 

Tonkawa Refining Co. 

Tosco Corp. 

Wireback Oil Co. 

Total 

Baltimore, Maryland 

Buffalo, New York 

Wilmington, Noah Carolina 

Newington, New Hampshire 

Falling Rock, West Virginia 

Port Manatee, Florida 

Buffalo, New York 

Emlenton, Pennsylvania 

St. Marks, Florida 

Sugar Creek, Missouri 

Wood River, Illinois 

Findlay, Ohio 

Louisville, Kentucky 

Enid, Oklahoma 

Wrenshall, Minnesota 

Scottsbluff, Nebraska 

Oblong, Illinois 

Bay City, Michigan 

Shallow Water, Kansas 

East Chicago, Indiana 

Crossville, Illinois 

Toledo, Ohio 

Cushing, Oklahoma 

Princeton, Indiana 

Hammond, Indiana 

Chanute, Kansas 

Augusta, Kansas 

Dickinson, North Dakota 

Cyril, Oklahoma 

Thomas, Oklahoma 

Okmulgee, Oklahoma 

Kansas City, Kansas 

Lockport, Illinois 

West Branch, Michigan 

Arnett, Oklahoma 

Duncan, Oklahoma 

Plymouth, Illinois 

See footnotes at end of table. 
Tabl

e 12. 

Refineries Shutdown since January 1,1981 (continued) 

District/ Refinery Location 

Crude 

Distillation 

Capacity 

(B/CD) 

Total 

Downstream 

Capacity 

(B/SD) 

Date 

of Last 

Operation 

Date 

Shutdown 

Years in 

Operation 

0 

a 

i 

"O •? fc 

a 

a 

e 8f 

a 

o 

a 

fc 

a 

3 

3 

CO 

•00 

PAO District III 

Adobe Refining Co.. div. 

of Funding Systems 

Refining Corp. 

Bayou State Oil Corp. 

Brio Refining Inc. 

Bronco Refining Co. 

Carbonit Refining Co. 

Caribou-Four Corners Inc. 

Celeron Oil & Gas Co. 

Clinton Manges 

Copano Refining Co. 

Dorchester Refining Co. 

Dow Chemical U.S.A. 

Eagle Refining Corp. 

Eddy Refining Co. 

Erickson Refining Corp. 

Evangeline Refining Co. 

GHR Energy Corp. 

Giant Industries Inc. 

Gulf Oil Corp. 

Hill Petroleum Co. 

Independent Refining Corp. 

Lake Charles Refining Co. 

Listo Refining Co. 

Longview Refining Co. 

Mallard Resources Inc. 

Marion Corp. 

McTan Refining Corp. 

Mid-Gulf Energy Corp. 

Natchez Refining Co. 

Petraco-Valley Oil 

Refining Co. 

Pioneer Refining Ltd. 

Placid Oil Co. 

Port Petroleum Inc. 

Quintana Petrochemical Co. 

Quitman Refining Co. 

Rio Grande Crude Refining 

Rio Grande Recovery 

Systems Inc. 

Schulze Processing Inc. 

Sentry Refining Inc. 

Shepard Oil Co. 

Shore, Inc. 

Sooner Refining Co. 

South Hampton Refining Co. 

Southern Union Refining Co. 

La Blanca, Texas 

Hosston, Louisiana 

Friendswood, Texas 

Houston, Texas 

Hearne, Texas 

Farmington, New Mexico 

Mermentau, Louisiana 

Palestine, Texas 

Ingleside, Texas 

Mt. Pleasant, Texas 

Freeport, Texas 

Jacksboro, Texas 

Houston, Texas 

Pt. Neches, Texas 

Jennings, Louisiana 

Good Hope, Louisiana 

Farmington, New Mexico 

Venice, Louisiana 

Krotz Springs, Louisiana 

Winnie, Texas 

Lake Charles, Louisiana 

Donna, Texas 

Longview, Texas 

Gueydan, Louisiana 

Theodore, Alabama 

St. James, Louisiana 

Ingleside, Texas 

Natchez, Mississippi 

Brownsville, Texas 

Nixon, Texas 

Mont Belvieu, Texas 

Stonewall, Louisiana 

Corpus Christi, Texas 

Quitman, Texas 

Brownsville, Texas 

Brownsville, Texas 

Tallulah, Louisiana 

Corpus Christi, Texas 

Jennings, Louisiana 

Kilgore, Texas 

Darrow, Louisiana 

Silsbee, Texas 

Monument, New Mexico 

5.200 

3,000 

12,500 

2,250 

11,000 

2,200 

11,000 

6,000 

11,100 

26.500 

190,000 

1,800 

3,250 

30,000 

4,500 

300,000 

13,500 

28,700 

57,400 

50,000 

28,000 

3,500 

14,000 

7,400 

25,000 

19,300 

39,400 

16,000 

12,300 

15,000 

8.500 

3,200 

33,300 

6,600 

9,500 

1,000 

1,760 

25,000 

10,000 

550 

8,000 

18,100 

5,400 

0 

0 

0 

0 

0 

2,400 

0 

0 

0 

38,800 

143,000 

0 

0 

0 

0 

433,000 

5,000 

46,300 

62,000 

63,000 

0 

0 

14,000 

0 

14,500 

0 

20,000 

0 

0 

15,900 

o 

0 

54,000 

0 

0 

0 

0 

0 

0 

0 

32,000 

28,000 

0 

11/81 

1/81 

9/82 

4/81 

2/81 

5/82 

2/83 

7/81 

9/81 

9/84 

8/81 

3/81 

10/84 

12/81 

12/82 

12/82 

5/82 

4/81 

9/84 

10/81 

4/81 

7/82 

12/81 

11/83 

3/83 

7/81 

10/83 

6/82 

3/83 

4/83 

1/82 

12/83 

7/84 

4/82 

6/81 

5/81 

5/81 

1/82 

5/81 

3/83 

1/82 

12/82 

1/81 

12/81 

3/82 

12/82 

7/82 

12/81 

8/84 

8/84 

7/82 

2/82 

12/84 

6/82 

7/82 

11/84 

8/83 

12/82 

9/83 

11/82 

12/81 

11/84 

8/83 

2/82 

12/82 

4/82 

12/83 

9/83 

8/83 

5/84 

9/82 

12/83 

12/83 

7/82 

2/84 

9/84 

6/82 

6/82 

2/82 

8/82 

2/82 

2/82 

7/83 

2/82 

12/84 

10/81 

25 + 

25 + 

4 

1 

6 

19 

6 

25 + 

4 

36 + 

1 

1 

36 + 

4 

25 + 

15 

7 

13 

6 

23 

2 

4 

25 + 

4 

15 

6 

6 

2 

5 

9 

2 

4 

30 

4 

3 

2 

4 

4 

4 

3 

2 

24 25 + 

See footnotes at end of table. 
( A . 

7 troloui 

3 tt 

e 

| 

? 

a nuel • • 

tt 4k 

•a Volui 

1 ** 

s 

• "« 

3 

2 'motion A 9-

3 

a 8" 

a 

s 

Table 12. 

Refineries .Shutdown since January 1,1981 (continued) 

District/ Refinery 

Southern Union Refining Co. 

Southland Oil Co. 

Tesoro Petroleum Corp. 

T & S Refining Co. 

Texas Refining Co. 

Texas Standard Refining 

Inc. 

Thriftway Oil Co. 

Tipperary Refining Co. 

Warrior Asphalt Co. 

Wickett Refining Co. 

Total 

PAD District IV 

Caribou-Four Corners Inc. 

C & H Refinery Inc. 

Glacier Park Co. 

Glenrock Refinery Inc. 

Husky Oil Co. 

Sage Creek Refining Co. 

Silver Eagle Oil Inc. 

Southwestern Refining Co. 

Texaco Inc. 

Total 

PAD District V 

Anchor Refining Co. Inc. 

Arizona Fuels Corp. 

ECO Petroleum Inc. 

Demenno-Kerdoon 

Marlex Oil & Refining Co. 

Powerine Oil Co. 

Quad Refining Corp. 

Road Oil Sales Inc. 

Sabre Oil & Refining Inc. 

Tosco Corp. 

United Independent Oil Co. 

U.S.A. Petrochemical Corp. 

Total 

United States Total 

IS) = Less than One Year. 

B/CD = Barrels per Calendar Day. 

B/SD = Barrels per Stream Day. 

Source: Form EIA-820. 

Location 

Lovington, New Mexico 

Yazoo City, Mississippi 

Carrizo Springs, Texas 

Jennings, Louisiana 

Midland, Texas 

Houston, Texas 

Graham, Texas 

Ingleside, Texas 

Holt, Alabama 

Wickett, Texas 

• 

Woods Cross, Utah 

Lusk, Wyoming 

Osage, Wyoming 

Glenrock, Wyoming 

Cody, Wyoming 

Cowley, Wyoming 

La Barge, Wyoming 

La Barge, Wyoming 

Casper, Wyoming 

McKittrick, California 

Fredonia, Arizona 

Long Beach, California 

Compton, California 

Los Angeles, California 

Santa Fe Springs, California 

Bakersfield, California 

Bakersfield, California 

Bakersfield, California 

Bakersfield, California 

Tacoma, Washington 

Ventura, California 

Crude 

Distillation 

Capacity 

(B/CD) 

36.100 

5,500 

26,100 

10,500 

2,500 

1.800 

1,184 

7,320 

5,500 

8,000 

1,186,214 

8,400 

180 

10,000 

6,000 

11,500 

1,000 

1,500 

1,040 

21,000 

60,620 

9,000 

6,000 

0 

10,000 

21,100 

44,120 

7,000 

6,000 

10,000 

38,800 

730 

24,000 

176,750 

2,526,634 

Total 

Downstream 

Capacity 

(B/SD) 

18,500 

3,080 

3,500 

0 

0 

0 

0 

0 

2,000 

0 

999.180 

8,200 

0 

* 0 

0 

17,800 

0 

0 

0 

35,500 

61,500 

7.000 

0 

7,000 

2,000 

0 

100,100 

0 

0 

0 

80,000 

0 

7,000 

203,100 

2,664,260 

Date 

of Last 

Operation 

8/84 

2/81 

7/84 

7/81 

4/81 

1/81 

4/81 

1/82 

8/83 

1/76 

12/82 

1/81 

2/81 

4/81 

6/82 

1/82 

10/82 

4/81 

3/82 

11/82 

2/83 

7/81 

1/83 

1/84 

6/84 

8/80 

1/81 

4/81 

11/83 

7/80 

12/84 

Date 

Shutdown 

11/84 

7/81 

12/84 

3/82 

6/81 

10/81 

11/83 

3/82 

12/84 

2/82 

12/84 

2/82 

3/82 

9/81 

9/82 

6/82 

8/83 

8/81 

7/82 

2/84 

9/83 

3/84 

8/83 

3/84 

8/84 

10/81 

12/81 

11/82 

11/84 

3/82 

12/84 

Years in 

Operation 

8 

25 + 

27 

2 

1 

(S) 25 + 

4 

30 25 + 21 25 + 

4 

5 

25 + 

17 

9 

7 

25 + 

--

6 

11 

8 

6 

7 

34 

2 

9 

10 33 

7 

7 
Tabl

e 13. 

Since 1961 

! 

t 

fc 

a 

a 

s 

tt 

tt *, 

f 

« 

o 

§ 

fc 

I 

3 a* 

a 5* 

a 

oo 

Former Owner 

Beacon Oil Co. 

Hanford, California 

Celeron Oil & Gas Co. 

Mermentau, Louisiana 

Cities Service Co. 

Lake Charles, Louisiana 

Occidental Petroleum 

Lake Charles, Louisiana 

Clark Oil & Refining Corp. 

Blue Island, Illinois 

Hartford (Wood River), Illinois 

Total 

CPI Oil & Refining Corp. 

Lake Charles, Louisiana 

Dorchester Refining Corp. 

Mt. Pleasant, Texas 

White Deer, Texas 

Total 

Earth Resources Co. 

Memphis, Tennessee 

North Pole, Alaska 

Total 

Edgington Oil Co. Inc. 

Long Beach, California 

Getty Refining & Marketing Co. 

Delaware City, Delaware 

El Dorado, Kansas 

Bakersfield, California 

Total 

Gulf Oil Corp. 

Sante Fe Springs, California 

Gulf States Oil & Refining Co. 

Corpus Christi, Texas 

Hermes Products Co. 

Newcastle, Wyoming 

Total 

Crude 

Distillation 

Capacity 

B/CD 

17.300 

11,000 

320,000 

320,000 

66.500 

63,600 

130,100 

13,500 

26,500 

0 

26,500 

49,500 

45,323 

94,823 

41,600 

140,000 

80.577 

48.400 

268,977 

51,500 

38,000 

12.555 

New Owner 

American Ultramar Ltd. 

Goodyear Tire & Rubber Co. 

Occidental Petroleum 

Southland Corp. 

Apex Oil Co. 

Calcasieu Refining Co. 

Damson Gas Processing Corp. 

Mid-American Pipeline System 

Triad Terminal Corp. 

Texaco Inc. 

Thrifty Oil Co. 

Koch Industries, Inc. 

Wyoming Refining Co. 

Date of 

Sate 

11/81 

6/83 

1/83 

9/83 

9/81 

11/84 

12/84 

5/82 

12/84 

12/84 

8/83 

1/83 

12/84 

See footnotes at end of table. 
co 

Oi 

Table 13. 

Refinery Sales Since 19M (continued) 

9 

tt 

I 

fc 

a i 4k 

tt 

fc 

I 3" 8* 

? I 

Former Owner 

Husky Oil Co. 

Cheyenne, Wyoming 

North Salt Lake, Utah 

Total 

Independent Valley Energy Co. 

Bakersfield, California 

Marathon Oil Co. 

Garyville, Louisiana 

Robinson, Illinois 

Texas City, Texas 

Detroit, Michigan 

Total 

Monsanto Co. 

Alvin/Texas City, Texas 

Conoco, Inc. 

West Lake, Louisiana 

Ponca City, Oklahoma 

Billings, Montana 

Paramount, California 

Alvin/Texas City, Texas 

Denver, Colorado 

Santa Maria, California 

Egan, Louisiana 

Total 

E.I. du Pont de Nemours &. Co. 

Paramount, California 

Mt. Airy Refining Co. 

Mt. Airy, Louisiana 

Pacific Oasis Corp. 

Paramount, California 

Phillips Petroleum Co. 

Great Falls, Montana 

Plateau Inc. 

Bloomfield, New Mexico 

Plateau Inc. 

Roosevelt, Utah 

Total 

Crude 

Distillation 

Capacity 

B/CD 

28,800 

25,000 

53.800 

27.000 

255,000 

195,000 

69,500 

68.500 

588,000 

37,194 

156,500 

133.700 

52,500 

•46,500 

37,194 

32,500 

9,500 

6,500 

474,894 

46,500 

23,000 

46,500 

6,300 

16,800 

7,500 

New Owner 

RMT Properties, Inc. 

Paramount Petroleum Corp. 

U.S. Steel 

Conoco, Inc. 

E.I. du Pont de Nemours & Co. 

Pacific-Oasis 

Apex Oil Co. 

Paramount Petroleum Corp. 

Texas Independent Oil Corp. 

Gary Energy Corp. 

Seagull Refining Co. 

Date of 

Sale 

12/84 

4/84 

1/82 

9/81 

9/81 

1/83 • 

9/81 

4/84 

3/81 

12/84 

4/84 

See footnotes at end of table. j ^ j ^ 
Tabl

e 13. 

Refinery Salaa Since 19*1 (continued) 

9 o 

tt 

e 

fc 

a 

i 

a 

tt 

« 

§ 

fc I 3* 5* 

§ 

Former Owner 

Quintana Petrochemical Co. 

Corpus Christi, Texas 

Shell Oil Co. 

Gallup. New Mexico 

Sigmor Corp. 

Three Rivers, Texas 

Sound Refining Inc. 

Tacoma, Washington 

Sun Co. Inc. 

Corpus Christi, Texas 

TARCO 

Euless, Texas 

Texaco, Inc. 

Sinclair, Wyoming 

Tonkawa Refining Co. 

Arnett, Oklahoma 

Uni Refining Co. 

Ingleside, Texas 

United Refining Co. 

Warren, Pennsylvania 

Western Refining Co. 

Woods Cross, Utah 

Winston Refining Co. 

Fort Worth, Texas 

Total 

Crude 

Distillation 

Capacity 

B/CD 

83,300 

18.000 

40,000 

6,000 

57,000 

4,650 

50,000 

12,000 

30,000 

60,000 

12,500 

20,000 

New Owner 

Coastal States Petroleum Co. 

Giant Industries Inc. 

Diamond Shamrock Corp. 

Crysen Corp. 

Koch Industries, Inc. 

Tropicana Energy Co. 

Sinclair Oil Corp. 

Ray Bell Oil Co. 

Texas Independent Oil Corp. 

Coral Petroleum 

Crysen Corp. 

E-2 Serv 

Date of 

Sale 

9/84 

4/82 

1/83 

1/82 

11/81 

12/83 

11/83 

6/83 

3/81 

3/81 

6/82 

2/81 

B/CD = Barrels per Calendar Day. 

Source: Form EIA-820. 

co 
CO OO 

Table 14. 

Refinery Recaipta of Crude OM by M-athod of Transportation by PAD District. 1984 

(Thousand Battels) 

PAO DISTRICTS 

o 

I 

fc 

a 

i 

i 

MBIIHJO 

Pipeline 

Domestic 

Foreign 

Tanker 

Domestic 

Foreign 

Barge 

Domestic 

Foreign 

Tank Cars 

Domestic 

Foreign 

Trucks 

Domestic 

Foreign 

Total 

Domestic 

Foreign 

Source: Form EIA-820 

United 

States 

7.925 

14.467 

42.212 

771.682 

3.322 

56.493 

5.009 

0 

S.326 

0 

63,794 

342,642 

781.366 

192.340 

15.671 

3.692 

15.8 

812.864 

196,032 

1,149.566 

140.734 

124.126 

447.190 

128.610 

5.908 

301 

0 

44.765 

0 

1.447.358 

593,832 

136,859 

11.780 

9.989 

0 

146.848 

11,780 

386.271 

6.468 

3E2.6S2 

71.887 

6.676 

130 

7.491 

0 

21.160 

0 

754.250 

78.486 

2.441.976 

365.789 

518.990 

790.759 

154.279 

86.223 

12.801 

0 

97.068 

0 

3.225.114 

1.222.771 

tt 

«sj 6* 

a 

fc I 

3 5* 

a 

Table 15. 

Fuels Consumed at RefMieries by PAD District, 1984 

(Thousand Barrels, Except Where Noted) 

' ~ PADOISTRICTS 

Commodity I II III 

Cmde Oil (including lease 

condensate) 0 80 69 

Distillate Fuel Oil 723 130 67 

Rat-dual Fuel Ci! 4.787 7.140 2,576 

Liquefied Petroleum Cases 489 2,186 1.719 

Natural Gas (million cubic 

feetl 27.022 67.919 378,524 

StHIGas 17,917 41,457 8S.734 

Marketable Petroleum Coke 1,299 0 0 

Catalyst Petroleum Coke 8.510 16,443 29.782 

Coal I thousand short tons! 154 68 125 

Purchased Electricity ImBlion 

kWhl 2,436 6.827 12.593 

Purchased Steam (million 

poundsl 10.611 -S32 10.794 

Hydrogen (million cubic lest) 0 788 0 

Other' 99 286 963 

1

 Other includes asphalt, finished motor gasoline, gasohne blending components, lubricating oils, naphthas, unfinished oUs. wax. and liquid sulfur. 

Source: Form EIA-820 

400 

13.946 

6.098 

0 

2.450 

0 

1.056 

0 

0 

0 

United 

States 

4 

531 

3.343 

3.625 

85.920 

41.024 

661 

8.481 

0 

6.442 

8.398 

5 

180 

153 

1.451 

18,814 

8.419 

573.330 

192.230 

1.950 

65.666 

347 

29.354 

30.635 

793 

1,6-27 
P.47 

Explanatory Notes 

Note 1: Data Collection Methodology 

Background 

Beginning In January 1983, the Energy Information Administration (EIA) unified Its petroleum supply data collection activities Into the Petroleum Supply Reporting 

System (PSRS). The PSRS represents a family of data 

collection survey forms, data processing systems and 

publication systems that have been consolidated to 

achieve comparability and consistency throughout. 

The survey forms that comprise the PSRS are: 

Form 

Number Name 

EIA-810 Monthly Refinery Report 

EIA-811 Monthly Bulk Terminal Report 

EIA-812 Monthly Product Pipeline Report 

EIA-813 Monthly Crude Oil Report 

EIA-814 Monthly Imports Report 

EIA-815 Monthly Shipments from Puerto Rico to 

the United States Report 

EIA-816 Monthly Natural Gas Liquids Report 

EIA-817 Monthly Tanker and Barge Movement Report 

EIA-820 Annual Refinery Report 

Forms EIA-810 through 817 comprise the Monthly 

Petroleum Supply Reporting System (MPSRS). These 

surveys collect detailed refinery and natural gas plant 

operations data; refinery, bulk terminal, natural gas 

plant and pipeline stocks data; crude oil and petroleum 

product Imports data; and data on movements of petroleum products and crude oil between (PAD) Petroleum 

Administration for Defense Districts. These surveys are 

the primary source of data for the "Summary Statistics" and "Detailed Statistics" sections of the PSA. A 

description of MPSRS survey forms follows in Explanatory Note 1.1. 

Data are also obtained on magnetic tape from the 

Bureau of the Census on a monthly basis. These tapes 

contain aggregated Import and export statistics that 

are used in the preparation of the PSA. A description of 

the Census data follows In Explanatory Note 1.2. 

Natural Qas Liquids Reporting Changes 

Beginning In January 1984, a number of changes In the 

reporting of natural gas liquids (NGL) were implemented. The modified system reflects supply and disposition of NGL on a component, rather than product, 

basis. 

From 1979 to 1983, the EIA collected and reported Information on the supply and disposition of nine NGL 

products. Beginning with January 1984, NGL supply 

and disposition data were reported on a five component 

basis to be consistent with recordkeeping practices 

used by the industry. The following table shows the 

product categories under the new and old basis. 

Product Basis vs. Component Basis Reporting 

1979-1983 Product Basis 

1. Ethane 

2. Ethane-Propane Mixtures 

3. Propane 

4. Butane-Propane Mixtures 

5. Butane 

6. Itobutane 

7. Unfractionated Stream 

a Natural Gasoline 

and Isopentane 

9. Plant Condensate 

1984 Component Basis 

1. Ethane 

• 

• 

2. Propane 

• 

• 

• 

3. Normal Butane 

• 

• 

4. Itobutane 

• 

5. Pentanes Plus 

• 

• 

Four PSRS surveys were modified beginning in January 

1984. They were: 

EIA-810 Monthly Refinery Report 

El A-811 Monthly Bulk Terminal Report 

EIA-812 Monthly Product Pipeline Report 

EIA-816 Monthly Natural Gas Liquids Report 

A fifth survey, the Form EIA-814, Monthly Imports Report (formerly Form ERA-60) was not modified. Adjustments are applied to NGL imports data to make them 

consistent with the revised reporting system (See Explanatory Note 12). 

Note 1.1: Monthly Petroleum Supply 

Reporting System (MPSRS) 

Background 

The MPSRS was Implemented in January 1983 as the result of an extensive effort to integrate the collection 

and processing of petroleum supply data that have 

been collected on other survey forms for many years. 

The collection of monthly petroleum supply statistics 

began as early as 1918 when the Bureau of Mines (BOM) 

began collecting data on refinery operations and crude 

40 

Petroleum 9upply Annuel 1994, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.48 

oil stocks and movements. The collection systems 

were further expanded to include natural gas plant 

liquids production and storage in 1925, imports of 

crude oil and petroleum products and storage and 

movement of petroleum products in 1959, and tanker 

and barge movements of crude oil and petroleum products In 1964. Since their inception, each survey has 

undergone numerous changes, but the MPSRS is the 

first effort to make them all consistent and comparable. 

Respondent Frame 

EIA-810: All petroleum refineries and blending plants 

located In the 50 States, District of Columbia, Puerto 

Rico, the Virgin Islands, Hawaiian Foreign Trade Zone, 

and Guam. Approximately 260 respondents report on 

the EIA-810. 

EIA-811: Every bulk terminal operating in the 50 

States, the District of Columbia, Puerto Rico, and the 

Virgin Islands. A bulk terminal is primarily used for storage and/or marketing of petroleum products and has a 

total bulk storage capacity of 50,000 barrels or more, 

and/or received petroleum products by tanker, barge, or 

pipeline. Bulk terminal facilities associated with a product pipeline are included. Approximately 320 respondents report on the EIA-811. 

EIA-812: All product pipeline companies that carry 

petroleum products (Including interstate, intrastate, 

and intracompany pipelines) in the 50 States, and the 

District of Columbia. Approximately 90 respondents report on the EIA-812. 

EIA-813: All companies which carry or store 1,000 barrels or more of crude oil. Included in this survey are 

gathering and trunk pipeline companies (including 

interstate, intrastate, and intracompany pipelines), 

crude oil producers, terminal operators, storers of 

crude oil, and companies transporting Alaskan crude 

oil by water in the 50 States and the District of Columbia. Approximately 180 respondents report on the 

EIA-813. 

EIA-814: All companies, including subsidiary or affiliated companies, that import crude oil, unfinished oils, 

and finished petroleum products into the United States 

and Puerto Rico. Approximately 1,500 respondents report on the EIA-814. 

EIA-815: All companies, including subsidiary or affiliated companies, that ship unfinished oils, and finished 

petroleum products to the United States from Puerto 

Rico. There are three respondents on the EIA-815. 

EIA-816: All facilities that extract liquid hydrocarbons 

from a natural gas stream (natural gas processing plant) 

and/or separate a liquid hydrocarbon stream into its 

component products (fractionator). Approximately 

1,050 respondents report on the EIA-816. 

EIA-817: All companies that have custody of crude oil 

or petroleum products transported by tanker or barge 

between PAD Districts or between the Panama Canal 

and the United States. 

For purposes of this report, custody is defined as 

physical possession of crude oil or petroleum products 

on a company owned tanker or barge. Also, companies 

which lease vessels or contract for the movement of 

crude oil or petroleum products on a tanker or barge between PAD Districts or between the Panama Canal and 

the United States are considered to have custody. Approximately 50 respondents report on the EIA-817. 

EIA utilizes a number of sources and methods to maintain the survey respondent lists. On a regular basis, survey managers review industry publications such as the 

Oil and Gas Journal and 0/7 Dally tor information on facilities or companies starting up or closing down operations. These sources are augmented by articles in 

newspapers, letters from respondents indicating 

changes in status and information received from survey 

systems operated by other offices. 

Every three years an extensive survey is conducted to 

completely refresh the frames. This involves consolidating information from every known source including 

State agencies, federal agencies (e.g., EPA, Corps of 

Engineers, Census Bureau, etc.), and private industry 

directories. The effort also includes the evaluation of 

the impact of potential frame changes on the historical 

time series of data published from these respondents. 

The results of this frame study are usually implemented 

In January to provide a full year under the same frame. 

Collection Methods 

The data for all of the MPSRS surveys are collected 

monthly. Completed forms are required to be postmarked by the 20th calendar day following the end of 

the report month, with the exception of the EIA-814 and 

EIA-815 which are due 15 work days following the end 

of the report month. Telephone follow-up calls are 

made to nonrespondents prior to the publication deadline, for their data. An automated mailing list is maintained and is used to monitor receipt of the forms. 

Imputing Missing Data 

Imputation is performed for companies that do not respond to EIA forms 810-813 and 816. For such companies, previous monthly values are used for current 

values. The previous month's ending stocks value is 

used for both the current month's beginning stocks 

and the current month's ending stocks. Data for nonrespondents on the EIA-814, 815, and 817 are not imputed. 

Response Rates 

The response rate is generally 99 to 100 percent by the 

time the data are first published. Nonrespondents are 

contacted in writing and reminded of their requirement 

to report. Companies that file late or fail to file are subject to criminal fines, civil penalties, and other sanctions as provided by Section 13 (i) of the FEA Act. 

41 

Potroloum Eupply Annuel 1994, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.49 

Note 1.2: Census Import (IM-145) and 

Export (EM-522 and EM-594) Data 

Background 

Each month the EIA purchases magnetic tapes of aggregated import and export statistics from the Bureau 

of the Census. These data tapes are the only source of 

export statistics and are used to augment the import 

data collected by the EIA. 

Import Statistics (IM-145) 

Coverage 

Census Import statistics used In the PSA reflect both 

government and nongovernment imports of merchandise from foreign countries and U.S. possessions into 

the United States (the 50 States and the District of 

Columbia), without regard to whether or not a commercial transaction Is Involved. The following types of 

transactions are excluded from the statistics. 

1. Merchandise in-transit . through the United 

States, when documented with Customs as an in-transit movement. 

2. U.S. merchandise that was held in foreign countries by the U.S. Armed Forces and is returned to the 

United States for the use of the Armed Forces. 

Source of Import Information 

The official U.S. Import statistics are compiled by the 

Bureau of the Census from copies of the import entry 

and warehouse withdrawal forms that importers are required by law to file with Customs officials (Customs 

Forms 7501,7505, and 7508). 

"The country reported In the statistics as the country of 

origin is defined as the country where the merchandise 

was grown, mined, or manufactured. In instances 

where the country of origin cannot be determined, the 

transactions are credited to the country of shipment. 

Export Statistics (EM-522 and EM-594) 

Coverage 

Census export statistics used in the PSA reflect both 

government and nongovernment exports of domestic 

and foreign merchandise from the United States (the 50 

States, and the District of Columbia) to foreign countries and U.S. possessions, without regard to whether 

or not the exportation Involves a commercial transaction. The following types of transactions are excluded 

from the statistics: 

1. Merchandise shipped in transit through the 

United States from one foreign country to another, 

when documented as such with U.S. Customs. 

2. Bunker fuels and other supplies and equipment 

for use on departing vessels, planes, or other carriers 

engaged in foreign trade. 

Source of Export Information 

The official U.S. export statistics are compiled by the 

Bureau of the Census. Exporters are required to file export documents with Custom's officials. 

Country and Area Destination 

The country of destination is defined as the country of 

ultimate destination or the country where the goods are 

to be consumed, further processed, or manufactured, 

as known to the shipper at the time of exportation. If 

the shipper does not know the country of ultimate destination, the shipment is credited to the last country to 

which the shipper knows that the merchandise will be 

shipped in the same form as it was when exported. 

Note 2: Supply 

The components of petroleum supply are field production, refinery production, Imports, and stock withdrawal 

or addition: 

Field Production is the sum of crude oil production (including lease condensate), natural gas processing 

plant production, and new supply (field production) of 

other liquids used by refineries. 

Crude oil production is based on data received from 

State conservation and revenue agencies. For further 

explanation, see Explanatory Note 3. 

Field production of natural gas plant liquids (NGPL), including finished petroleum products, is reported 

monthly on survey Form EIA-816, Monthly Natural Gas 

Liquids Report. Negative production will occur when 

the amount of a product produced during the month is 

less than the amount of that same product that is reprocessed (input) or reclassified to become another 

product during the same month. For survey description 

and other detail, see Explanatory Note 1.1. 

Refinery Production of petroleum products is reported 

monthly on survey Form EIA-810, Monthly Refinery Report. Published production of these products equals refinery production minus refinery input. Refinery production of unfinished oils and of motor and aviation 

gasoline blending components appears on a net basis 

under refinery input. Negative production will occur 

when the amount of a product produced during the 

month is less than the amount of that same product 

that is reprocessed (input) or reclassified to become 

another product during the same month. 

Imports of crude oil and petroleum products are reported monthly on Form EIA-814, Monthly Imports Report, 

and Form EIA-815, Monthly. Shipments from Puerto 

Rico to the United States Report. In addition, imports of 

NGL's are obtained from the Census Bureau Tabulation 

IM-145. The Census Bureau Tabulation IM-145 summarizes import data from Customs import declarations re42 

Potroloum 9upply Annuel 1984, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.50 

ported on Customs Forms 7501, 7505, and 7506. Additional data taken from the IM-145 are relatively small 

quantities of naphthatype and kerosene type jet fuels, 

distillate fuels oils, and residual fuel oils withdrawn 

from bonded storage for use in international trade. 

Even though these duty-free fuels are stored on United 

States shores, they did not enter the United States for 

domestic consumption and therefore are not included 

in the Form EIA-814 reporting system. 

Stock Withdrawal ( + ) or Addition (-) is calculated by 

subtracting stocks at the end of the month from stocks 

at the beginning of the same month. (Note: The beginning stocks of one month are equal to the ending 

stocks of the previous month.) A positive result ( + ) 

would represent a withdrawal from stocks. A negative 

result (-) would represent a buildup of stocks. For a 

description of survey forms used to make stock withdrawal or addition calculations see Explanatory Note 5. 

Unaccounted-for Crude Oil is a balancing item that represents the difference between crude oil supply and 

disposition. Crude oil supply is the sum of field production, imports, and stock withdrawals. Crude oil disposition is the sum of exports, refinery Input, losses, stock 

additions, and product supplied. Unaccounted-for 

crude oil is calculated by subtracting crude oil supply 

from crude oil disposition. A positive result indicates 

that refiners and exporters reported use of more crude 

oil than was reported to have been available to them. 

(This occurs, for example, when imports are undercounted due to late reporting or other problems.) A 

negative result would indicate that more crude oil was 

reported to have been supplied to refiners and exporters than they reported used. 

Note 3: Domestic Crude Oil Production 

EIA-810, Monthly Refinery. Report. Published inputs of 

unfinished oils and of motor and aviation gasoline 

blending components equal refinery input minus refinery output. Refinery inputs of finished petroleum products are reported on a net basis under refinery production. 

Exports of crude oil and petroleum products are compiled from Census Bureau tabulations EM-522 and 

EM-594. Exports Include crude oil shipments to Puerto 

Rico, the Virgin Islands, and the Hawaiian Foreign 

Trade Zone, which are obtained from refinery receipts 

reported on Form EIA-810, by refineries located in 

these places. 

Product Supplied for each product is calculated by 

summing field production plus refinery production, 

plus imports, plus stock withdrawal or minus stock addition, minus crude oil losses (plus net receipts when 

calculated on a PAD District basis), minus refinery input, minus exports. This formula ensures tiiat total disposition equals total supply. 

Product supplied indicates those quantities of petroleum products supplied for domestic consumption. Occasionally, the result for a product is negative because 

total disposition of that product exceeds total supply. 

Negative product supplied may occur for a number of 

reasons: (1) product reclassification has not been reported; (2) data were misreported or reported late; (3) in 

the case of calculations on a PAD District basis, the figure for net receipts was inaccurate because the coverage of interdistrict movements was imcomplete; and (4) 

products such as gasoline blending components and 

unfinished oils have entered the primary supply channels with their production not having been reported, 

e.g., streams returned to refineries from petrochemical 

plants. 

Data for the Crude OH Production System (COPS) are reported to the Department of Energy by the State conservation agencies. Data on the volume of oil produced 

on Federally-owned offshore leases are reported by the 

Minerals Management Service, U.S. Department of the 

Interior. All except eight of the producing States report 

data monthly. These States are Arkansas, Missouri, 

New York, Ohio, Pennsylvania, Utah, Virginia, and 

Wyoming. After the end of each calendar year, the 

monthly numbers are updated using the annual reports 

of the State conservation agencies and the Minerals 

Management Service. 

Note 4: Disposition 

The components of petroleum disposition are crude oil 

losses, refinery Inputs, exports, and products supplied 

for domestic consumption. 

Crude Oil Losses is the sum of crude oil losses at refiners, reported for all refineries on Form EIA-810, Monthly Refinery Report. 

Refinery inputs of crude oil, natural gas plant liquids, 

and other liquids are reported monthly on survey Form 

Product supplied for crude oil is the sum of crude oil 

burned on leases and by pipelines as fuel oil. These 

data are reported on Form EIA-813, Monthly Crude Oil 

Report. Prior to January 1983, crude oil burned on 

leases and by pipelines as fuel oil were reported as 

either distillate or residual fuel oil and included in product supplied for these products. 

Note 5: Stocks 

Primary stocks of crude oil are the sum of ending 

stocks reported monthly on Form EIA-810, Monthly Refinery Report, and on Form EIA-813, Monthly Crude Oil 

Report. Crude oil held in the Strategic Petroleum Reserve is included unless otherwise noted. Alaskan 

crude oil in transit is also included. Primary stocks of 

petroleum products are summed from data reported on 

Form EIA-816, Monthly Natural Gas Liquids Report, 

Form EIA-810, Monthly Refinery Report, Form EIA-811, 

Monthly Bulk Terminal Report, and on Form EIA-812, 

Monthly Product Pipeline Report. Primary stocks of petroleum products do not include either secondary 

stocks held by dealers and jobbers or tertiary stocks 

held by consumers. For survey descriptions and other 

details, see Explanatory Note 1.1. 

43 

Potroloum tupply Annuel 1994, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.51 

Note 6: Average Stock Levels 

The national Inventory (stocks) graphs for total petroleum products, crude oil, motor gasoline, distillate fuel 

oil, residual oil, and liquefied petroleum gases, in this 

publication include features to assist in comparing current inventory levels with past inventory levels and 

minimum operating levels are described below. 

The graphs displaying Inventory levels of crude oil and 

petroleum products, crude oil, motor gasoline, distillate guel oil, residual fuel oil, and liquefied petroleum 

gases, provide the reader with actual inventory data 

compared to an average range from the most recent 3-

year period running from January through December or 

from July through June. The ranges are updated every 

six months in April and October. The 3-year period is adjusted by dropping the oldest 6 months and including 

the most recent 6 months. The ranges also reflects seasonal variation determined from a longer time period. 

The seasonal factors, which determine the shape of the 

upper and lower curves, are updated annually in October, using the most recent year's final monthly data. 

The monthly seasonal factors are estimated by means 

of a seasonal adjustment technique developed at the 

Bureau of the Census (Census X-11). The seasonal factors are assumed to be stable (i.e., unchanging from 

year to year) and additive (i.e., the series is deseasonallzed by subtracting the seasonal factor for the appropriate month from the report inventory levels). The intent 

of the deseasonalization is to remove only annual variation from the data. Thus, a deseasonalized series would 

contain the same trends, cyclical components, and irregularities as the original data. The seasonal factors 

for distillate fuel oil, residual fuel oil, and liquefied petroleum gases, were derived using monthly data from 

1977-1983. In 1977, monthly stock levels of motor gasoline stayed at the same high level for the entire year. 

Since there was virtually no seasonal behavior in motor 

gasoline stocks that year, data for 1978-1983 were used 

in the determination of seasonal patterns for motor 

gasoline stocks. 

After seasonal factors are derived, data from the most 

recent 3-year period (January-December or July-June) 

are deseasonalized. The average of the deseasonalized 

36-month series determines the midpoint of the deseasonalized average band. The standard deviation of the 

deseasonalized 36-months is calculated adjusting for 

extreme data points. The upper curve of the average 

range Is defined as the average plus the seasonal factors plus the standard deviation. The lower curve is defined as the average plus the seasonal factors minus 

the standard deviation. Thus, the width, of the average 

range is twice the standard deviation. 

Note 7: Movements 

Movements of crude oil between PAD Districts are reported on Form EIA-817, Monthly Tanker and Barge 

Movement Report, and on Form EIA-813, Monthly 

Crude Oil Report. Petroleum product movements are reported on Form EIA-817, Monthly Tanker and Barge 

Movement Report, and EIA-812, Monthly Product Pipeline Report. Net receipts is the difference between total 

movements into and total movements out of each PAD 

District by pipeline, tanker, and barge. For survey descriptions and other detail, see Explanatory Note 1.1. 

Note 8: Notes on Tables 

Note 8.1 Crude OH and Petroleum Products Overview 

statistics on the referenced line appear in Table 3 of the 

"Detailed Statistics," except where noted. 

• Crude Oil and Petroleum Products Stock Withdrawal ( + ) or Addition (-), Petroleum Products Supplied, 

Total Imports, Crude Oil Imports, Total Exports, and 

Crude Oil Exports appear as labeled in Table 3. Total 

Production and Crude Oil Production appear under 

Field Production in Table 3. 

• Natural Gas Plant Production is the sum of Natural 

Gas Liquids and Finished Petroleum Products Field 

Production in Table 3. 

• Petroleum Products Imports is the sum of Natural 

Gas Liquids and LRGs, Other Liquids, and Finished 

Petroleum Products Imports in Table 3. 

• Total Crude Oil and Petroleum Products Ending 

Stocks appear in thousand barrels in Table 2. 

Note 8.2 Crude Oil Supply and Disposition statistics on 

referenced line appear in Table 1 of the "Detailed Statistics," except where noted. 

• Total Domestic Field Production, Alaskan Field Production, SPR Imports, Other Imports (synonymous 

with Gross Imports Excl. SPR) SPR and Other Primary 

Stocks Withdrawal (+) or Addition (-), Unaccounted 

For Crude Oil, Refinery Inputs, and Exports appear as 

labeled in Table 1. 

• Crude Losses and Product Supplied appear as labeled in Table 3. 

• SPR Ending Stocks and Other Primary Ending 

Stocks (synonymous with stocks excluding SPR) appear in thousand barrels in Table 1. 

• Total Crude Oil Ending Stocks appear in thousand 

barrels in Table 2. 

• Total Imports appear in Table 3. 

Note 8.3 Finished Motor Gasoline Supply and Disposition statistics on the referened line appear in Table 3 of 

the "Detailed Statistics," except where noted. 

• Total Production is the sum of Field Production and 

Refinery Production in Table 3. 

• Imports, Stock Withdrawal ( + ) or Addition (-), Exports and Product Supplied appear as labeled in 

Table 3. 

• Unleaded Percent of Total Product Supplied represents the ratio of finished unleaded motor gasoline 

product supplied to total finished motor gasoline 

44 

Petroleum 9upply Annuel 1984, Volume I I Enorgy Informetlon Admlnlotrotlon 
product supplied, multiplied by 100 and rounded to 

the nearest tenth. 

• Ending stocks are aggregated from ending stocks 

in thousand barrels In Table 2. 

Note 8.4 Distillate and Residual Fuel Oil Supply and 

Disposition statistics on the referenced lines appear in 

Table 4 of the Detailed Statistics, except where noted. 

• Total Production Is the sum of Field Production and 

Refinery Production In Table 3. 

• Imports, Stock Withdrawal ( + ) or Addition (-), Exports, and Product Supplied appear as labeled in 

Table 3. 

• Ending stocks appear In thousand barrels in Table 

2. 

Note 8.5 Liquefied Petroleum Gases Supply and Disposition statistics represent the aggregation of statistics 

on ethane, ethylene, propane, propylene, butane, butylene, and Isobutane. The statistics on the reference line 

appear In Table 3 of the Detailed Statistics, except 

where noted. 

• Total Production is the sum of Field Production and 

Refinery Production In Table 3. 

• Imports, Stocks Withdrawal (+) or Addition (-), Refinery Inputs, Exports, and Product Supplied appear 

as labeled in Table 3. 

• Ending stocks appear In thousand barrels in Table 

2. 

Note 8.6 Other Petroleum Products Supply and Disposition statistics represent the aggregation of statistics 

on pentanes plus, other liquids, and all finished petroleum products except finished motor gasoline, distillate fuel oil, residual fuel oil, and liquefied petroleum 

gases. The statistics on the referenced line are aggregated from Table 3 of the Detailed Statistics, except 

where noted. 

• Total production Is the aggregation sum of Field 

Production and Refinery Production in Table 3. 

• Imports, Stock Withdrawal ( + ) or Addition (-), Refinery Inputs, Exports, and Product Supplied are aggregated from Table 3. 

• Ending stocks are aggregated from ending stocks 

in thousand barrels in Table 2. 

Note 8.7 Table 1. U.S. Petroleum Balance 

• Lines (1) through (3): Crude oil (including lease condensate) production tor Alaska, and Total U.S. appear 

as labeled in Table 9. Lower 48 states is calculated by 

subtracting Alaska crude oil production from Total 

U.S. crude oil production. 

• Line (5): SPR Imports are reported on survey Form 

EIA-814. 

• Line (12): Total Other Sources equals crude oil 

stock withdrawal (+) or addition (-) plus unaccounted for crude oil minus crude oil losses minus crude 

oil product supplied in Table 2. 

• Line (14): Natural Gas Plant Liquids (NGPL) Field 

Production equals Field production of natural gas liquids (NGL) plus field production of finished petroleum products in Table 2. 

• Line (15): NGPL Net Imports equals the sum of the 

imports of pentanes plus minus the exports of pentanes plus in Table 2. 

• Line (16): NGPL Stock Withdrawal (+)or Addition 

(-) is equal to the stock withdrawal ( + ) or addition 

(-) of pentanes plus in Table 2. 

• Line (17) equals the sum of lines (14), (15), and (16). 

• Line (18): Other liquids Stock Withdrawal (+) or 

Addition (-) equals the aggregate stock withdrawal 

(+) or addition (-) for other hydrocarbons and alcohol, unfinished oils, motor gasoline blending components, and aviation gasoline blending components in 

Table 2. 

• Line (20): Other Hydrocarbons and Alcohol New 

Supply equals the field production of same in Table 2. 

• Line (21): Refinery Processing Gain is a balancing 

item equal to total refinery production minus total refinery input in Table 2. 

• Line (23): Total Other Liquids equals the sum of 

lines (18) through (22). 

• Line (24): Total Production of Products equals 

crude oil input to refineries plus field production of 

natural gas liquids and LRG and finished petroleum 

products; plus imports of pentanes plus; plus stock 

withdrawal (+) or addition (-) of pentanes plus; plus 

stock withdrawal (+) or addition (-) of other liquids; 

plus imports of other liquids; plus field production of 

other liquids; plus total refinery production; minus total refinery input; plus crude oil product supplied in 

Table 2. 

• Line (25): Gross Imports of Refined Products 

equals imports of LPG plus imports of finished petroleum products In Table 2. 

• Line (26): Exports of Refined Products equals exports of LPG plus exports of finished petroleum products in Table 2. 

• Line (27): Net Imports of Refined Products equals 

the difference between lines (25) and (26). 

• Line (28) Total New Supply of Products equals 

crude oil input to refineries plus field production of 

natural gas liquids and LRG and finished petroleum 

products; plus imports of pentanes plus; plus stock 

withdrawal (+) or addition (-) of pentanes plus; plus 

stock withdrawal (+) or addition (-) of other liquids; 

plus imports of other liquids; plus total field production of other liquids; plus total refinery production; 

minus total refinery input; minus crude oil product 

45 

Petroleum Supply Annuel 1994, Volume I I Enorgy Informetlon AdmlnletreUon 
P.53 

supplied plus imports of LPG and finished petroleum 

products; minus exports of LPG and finished petroleum products in Table 2. 

• Line (29): Refined Products Stock Withdraw! (+) or 

addition (-) equals the sum of stock withdrawal (-*•) 

or addition (-) for LPG and finished petroleum products In Table 2. 

• Line (30): Total Petroleum Supplied for Domestic 

Use equals total products supplied In Table 2. 

• Line (31): through (35) equal the respective products supplied in Table 2. 

• Line (36): Other Products Supplied equals the sum 

of pentanes plus, aviation gasoline, naphtha-type jet 

fuel; kerosene-type jet fuel; naphtha < 400 Deg. F. for 

petrochemical feedstock use, other oils > 400 Deg. F. 

for petrochemical feedstock use, special naphthas, 

lubricants, waxes, petroleum coke, asphalt, and road 

oil, still gas, unfinished oils, motor gasoline blending 

components, aviation gasoline blending components, and miscellaneous products supplied in Table 

2. 

• Line (37): Total Product Supplied Is equal to total 

products supplied in Table 2. 

• The sum of lines (38) and (39), stocks of Crude Oil 

and Lease Condensate (Excluding SPR) and stocks 

held by the Strategic Petroleum Reserve, equals ending stocks of crude oil in Table 2. 

• Line (43): Stocks of Refined Products equals the 

sum of liquefied petroleum gases and finished petroleum product stocks in Table 2. 

• Other Petroleum Products: 

and 1982—259. 

1974—220; 1980-249; 

• Stock withdrawal calculations beginning in 1975, 

1981,1983 were made using new basis stock levels. 

In January 1984, changes were made in the reporting of 

natural gas liquids. As a result, unfractlonated stream, 

which was formerly included in "Other Petroleum Products Supply and Disposition" table in the Summary Statistics, is now reported on a component basis (ethane, 

propane, normal butane, isobutane, and pentanes plus). 

Most of these stocks will now appear in the "Liquefied 

Petroleum Gases Supply and Disposition" table of the 

Summary Statistics. This change will affect stocks reported and stock withdrawals in each table. Under the 

new basis, end-of-year 1983 stocks, in million barrels, 

would have been: 

• Liquefied Petroleum Gases: 1983—108 

• Other Petroleum Products: 1983—2-48 

Note 10: Stocks of Alaskan Crude Oil 

Stocks of Alaskan crude oil in transit were included for 

the first time in January 1981. The major impact of this 

change is on the reporting of stock withdrawal calculations. Using the expanded coverage (new basis), 1980 

end-of-year stocks, in million barrels, would have been 

488 (Total) and 380 (Other Primary). 

Note 11: Changes in Petroleum Industry 

Reporting 

Note 9: New Stock Basis 

In January 1975,1981, and 1983, numerous respondents 

were added to bulk terminal and pipeline surveys affecting subsequent stocks reported and stock withdrawal calculations. Using the expanded coverage (new 

basis), the end-of-year stocks, in million barrels, would 

have been: 

• Crude OH: 1982—645 (Total) and 351 (Other Primary). 

• Crude Oil and Petroleum Products: 1974—1,121; 

1980—1,420; and 1982—1,462. 

• Motor Gasoline: 1974—225; 1980—263; 1982—244 

(Total) and 203 (Finished). 

• Distillate Fuel Oil: 1974—224; 1980—205; and 

1982—186. 

• Residual Fuel Oil: 1974—75; 1980—91; and 1982— 

68. 

• Liquefied Petroleum Gases: 1974—113; 1980—128; 

and 1982—103. . 

Petroleum statistics contained in this report for all 

years through 1980 were developed using definitions, 

concepts, reporting procedures, and aggregation methods that are consistent with those developed by the 

U.S. Bureau of Mines. Research conducted by the Energy Information Administration in 1979 and 1980 indicated that changes had occurred in the petroleum industry 

that were not being adequately reflected in El A's reporting system. 

EIA reporting forms, definitions, and procedures were 

modified beginning in January 1981 to describe industry operations more accurately. Unfortunately, empirical information is not available to precisely measure 

the data shortcomings throughout 1980. However, estimates of the magnitudes of differences in the major 

data series are described below to form a basis for comparing 1979,1980, and 1981 data. 

Motor Gasoline 

Prior to 1979, the EIA product-supplied series for motor 

gasoline was consistently about 2 percent lower than 

the Federal Highway Administration (FHWA) gasolinesales data series, which is derived from State tax receipts. The difference increased to about 3 percent in 

1979 and 1980. There were two primary causes for this 

46 

Petroleum Eupply Annuel 1994, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.54 

growing difference. First, refinery operations, particularly the flows of unfinished oils and the redesignation 

of some finished products, were not being accurately 

described on the EIA survey forms. Second, a large 

amount of gasoline was being produced away from refineries at "downstream blending stations" to take advantage of provisions in regulations governing the 

amount of lead that could be added. These blending 

stations were not reporting gasoline production to the 

EIA until the data system was changed in January 1981. 

Quantitative estimates of the magnitude of the difference In ElA's gasoline product supplied data in 1979 

and 1980 have been made by the EIA and the American 

Petroleum Institute (API). The following table provides 

1979 and 1980 data as published In the Petroleum Statement Annual, as well as EIA and API estimates of "recast" motor gasoline product supplied. 

Finished Motor Gasoline Product Supplied 

(Thousand Barrels per Day) 

EIA 

Reported 

API 

Recast 

EIA 

Recast FHWA* 

1979. 

1980. 

7,034 

6,579 

7,302 

6,882 

7,183-7,347 

6,806-6,889 

7,258 

6,792 

'FHWA gasoline statistics based on data from Federal Highway Administration. Estimate of Total Gasoline Use. Table 

MF-21A Published October 1980 and September 1981. Aviation 

gasoline (Table MF-24) has been subtracted from FHWA product supplied quantities to make data comparable. 

EIA recast estimates were based upon preliminary 

monthly information in the Monthly Petroleum Statement. The ranges displayed in the EIA column reflect 

uncertainty In the estimates. Also shown are the FHWA 

motor gasoline sales statistics for those years. 

Distillate and Residual Fuel Oil 

Distillate and residual fuel oil refinery production statistics through 1980 were adjusted to account for an imbalance between unfinished oil supply and disposition. 

The reported quantities of refinery inputs of unfinished 

oils typically exceed the available supply of unfinished 

oils. It has been assumed that this occurs when distillate and residual fuel oils produced by a refinery is 

shipped to another refinery, where it is treated as unfinished oil. This oil Is then reprocessed rather than used 

or sold as distillate or residual fuel oil. 

For many years (Including 1980), the difference between unfinished oil disposition and supply was subtracted from distillate and residual fuel oil production 

to adjust for this discrepancy. Two-thirds of the difference was applied to distillate, and one-third to residual 

fuel oil. 

Beginning in January 1981 this adjustment was discontinued because there was not sufficient empirical evidence to support it. The following table presents distillate and residual fuel oil refinery production in 1979 and 

1980 as published (adjusted) and on the same basis as 

1981 statistics (unadjusted) to permit comparison. 

Distillate and Residual • Fuel 

Product Supplied 

(Thousand Barrels per Day) 

Oils Production and 

Adjusted Unadjusted 

Refinery Refinery 

Production Production 

Distillate Fuel Oil 

1979 3,152 3,169 

1980 2,661 2,764 

Residual Fuel Oil 

1979 1,687 1,695 

1980 1,580 1,634 

Unadjusted 

Product 

Difference Supplied 

16 

103 

8 

54 

3,327 

2,969 

2,834 

2,562 

Adjusted distillate and residual fuel oil product supplied volumes differ from the unadjusted volumes by 

the same amounts as the adjusted and unadjusted production volumes. 

Total Petroleum Products 

The imbalance between the supply and disposition of 

unfinished oils and gasoline blending components is 

included with other products (line 35) line in the U.S. Petroleum Balance (Table 1). These imbalances are reported as negative product supplied in the Other Liquids 

section, Supply and Disposition Statistics (Table 2). 

Since these changes only involve redistribution of the 

volumes of gasoline, distillate and residual fuel oil, 

gasoline blending components, and unfinished oils, 

the total volume of petroleum products supplied remains unaffected by them. 

Note 12: NGL Import/Export Algorithms 

Beginning in January 1984, the Energy Information Administration (EIA) implemented changes in the reporting of natural gas liquids (NGL) supply data, moving 

from a nine-product slate basis to a five-product slate 

basis that corresponds to industry record-keeping practices. Changes could not be made to the import and export systems. Therefore, in order to allocate imports 

and exports of mixed NGL streams to individual component parts, the EIA developed a statistical algorithm. 

Imports 

The imports algorithm is based on information 

gathered from the larger importers of NGL, who were 

asked to provide component analysis of the products 

they imported during the first six months of 1983. The 

percentages shown in the table below are derived from 

the weighted averages of the data provided by the importers. 

Exports 

The export algorithm is based on information gathered 

from the larger exporters of NGL, who were asked to 

provide component analyses of the products they exported during 1983. The percentages shown below are 

derived from the weighted averages of the data provided by the exporters. It was necessary to derive percentages by Petroleum Administration for Defense (PAD) 

Districts of exportation, due to the wide variation of 

components included in the mixed streams. 

47 

Petroleum 9upply Annuel 1994, Volume I I Enorgy Informetlon Admlnlotrotlon 
P.55 

Algorithm for Allocating NGL Imports/Exports 

Import Product Ethane 

Natural Gasoline 

and Isopentane 

(EIA-814) 

Plant Condensate 

(EIA-814) 

Ethane (IM-145).... 100% 

Butane (IM-145).... 

Butane-Propane 

Mixtures (IM-145). 

Ethane-Propane 

Mixtures (IM-145)... 80% 

Export Product 

Ethane (All PAD).... 100% 

Propane (ALL PAD) . 

- Butane (All PAD).... 

Mixed Streams 

PAD 1, IV, V 

PAD II 30% PAD III 

EIA Component State 

NorPropane 

40% 

20% 

100% 

40% 

25% 

80% 

rnal 

Bu- Isobutane tane 

60% -40% 

35% 20% 

100% 

60% 

15% 15% 20% 

JAN FEB 

Refinery Gross Input to Crude Distillation Units 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

Refinery Crude Oil input 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

270 267 

206 205 

1,771 1,737 

2,287 2,204 

270 267 

205 205 

1,752 1,720 

2,256 2,166 

Pentanes 

Plus 

100% 

100% 

5% 

15% 

MAR 

265 

210 

1,782 

2,223 

265 

210 

1,761 

2,187 

APR 

266 

206 

1,759 

2,257 

266 

206 

1,732 

2,211 

Refinery Finished Leaded Motor Gasoline Gross Production 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

270 267 

181 180 

431 425 

444 436 

265 

181 

451 

460 

266 

180 

458 

469 

Refinery Finished Unleaded Motor Gssoline Gross Production 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

270 267 

158 161 

694 666 

790 770 

Refinery Distillate Fuel Oil Gross Production 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

270 267 

194 196 

427 436 

567 572 

Refinery Residual Fuel Oil Gross Production 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

270 267 

172 169 

179 177 

265 273 

265 

160 

723 

831 

265 

199 

402 

475 

265 

169 

170 

264 

Refinery finished Leaded Motor Gasoline Stocks 

Respondents 

Nonzero Respondents 

Average 

Standard Deviation 

48 

270 267 

187 187 

108 112 

115 129 

265 

185 

116 

123 

266 

163 

697 

827 

266 

199 

370 

448 

266 

168 

156 

259 

266 

186 

117 

117 

Him 9uppiy Annuel 1994, Volumo 1 1 

Note 13: Statistical Notes 

The universe of each of the Petroleum Supply Surveys (refinery, bulk terminal, pipeline, crude oil stock, 

import, etc) is relatively small and everchanging due to 

company births, deaths, mergers and splits. The frequency distributions of the petroleum supply variables 

are non-normal, highly variable, | positive skewed and 

leptokurtic; that is, there are many small units and few 

large ones. Zeros often dominate the responses; that is, 

not all of the sampling units produce and/or store all 

products. 

The statistics described below * -were calculated from 

the monthly census surveys over a 12 month period. 

1. The number of active sampling units (respondents). 

2. The number of sampling units reporting nonzero 

values (nonzero respondents). 

3. The average of nonzero values reported in thousand barrels (average). 

4. The standard deviation of nonzero values reported 

in thousand barrels (standard deviation). 

MAY 

262 

209 

1,845 

2,332 

262 

212 

1,791 

2,280 

262 

178 

475 

496 

262 

161 

758 

857 

262 

201 

421 

494 

262 

172 

155 

250 

262 

187 

124 

127 

JUN 

262 

213 

1,749 

2,234 

262 

211 

1,742 

2,198 

262 

182 

441 

443 

262 

160 

743 

864 

262 

203 

440 

534 

262 

170 

156 

264 

262 

186 

111 

113 

JUL 

262 

204 

1,850 

2,273 

262 

203 

1,837 

2,235 

262 

177 

449 

453 

262 

158 

764 

862 

262 

194 

450 

520 

262 

157 

160 

231 

262 

183 

105 

108 

AUG 

259 

205 

1,896 

2,416 

254 

204 

1,876 

2,366 

259 

172 

454 

448 

259 

154 

787 

887 

259 

193 

443 

541 

259 

160 

164 

276 

259 

184 

96 

103 

SEP 

257 

202 

1,853 

2,317 

257 

201 

1,832 

2,276 

257 

175 

433 

448 

257 

155 

774 

872 

257 

190 

444 

536 

257 

161 

165 

290 

257 

181 

108 

116 

Enorgy Informetlon AdmlnletreUon 

OCT 

257 

199 

1,893 

2,423 

257 

197 

1,885 

2,373 

257 

168 

446 

458 

257 

156 

792 

883 

257 

192 

451 

563 

257 

163 

178 

288 

257 

179 

100 

108 

NOV 

254 

196 

1,876 

2,302 

254 

194 

1,872 

2,262 

254 

167 

465 

465 

254 

151 

822 

899 

254 

184 

473 

555 

254 

156 

186 

286 

254 

174 

109 

111 

DEC 

250 

195 

1,903 

2,267 

250 

191 

1,908 

2,220 

250 

166 

450 

435 

250 

153 

829 

911 

250 

175 

514 

574 

250 

155 

217 

356 

250 

173 

115 

120 
P.56 

JAN FEB MAR 

Bulk Terminal Finished Leaded Motor Gasoline Stocks 

Respondents 317 

Nonzero Respondents 146 

Average 313 

Standard Deviation 637 

317 

147 

326 

665 

318 

148 

349 

722 

Pipeline Finished Leaded Motor Gasoline Stocks 

Respondents 90 

Nonzero Respondents 59 

Average 449 

91 

59 

469 

Standard Deviation 1,085 1,105 

91 

58 

427 

775 

Refinery Finished Unleaded Motor Gasoline Stocks 

Respondents 270 

Nonzero Respondents 174 

Average 126 

Standard Deviation 139 

267 

176 

137 

157 

265 

175 

146 

171 

APR 

317 

145 

367 

734 

90 

59 

438 

852, 

266 

175 

146 

165 

Bulk Terminal Finished Unleaded Motor Gasoline Stocks 

Respondents 317 

Nonzero Respondents 145 

Average 321 

Standard Deviation 704 

317 

147 

335 

750 

318 

147 

334 

747 

Pipeline Finished Unleaded Motor Gasoline Stocks 

Respondents 90 

Nonzero Respondents 61 

Average 406 

Standard Deviation 878 

Refinery Distillate Fuel Oil Stocks 

Respondents 270 

Nonzero Respondents 218 

Average 158 

Standard Deviation 221 

Bulk Terminal Distillate Fuel Oil Stocks 

Respondents 317 

Nonzero Respondents 249 

Average 237 

Standard Deviation 650 

Pipeline Distillate Fuel Oil Stocks 

Respondents 90 

Nonzero Respondents 62 

Average 419 

Standard Deviation 1,150 

Refinery Residual Fuel Oil Stocks 

Respondents 270 

Nonzero Respondents • 191 

Average 101 

Standard Deviation 179 

Bulk Terminal Residual Fuel Oil Stocks 

Respondents 317 

Nonzero Respondents 94 

Average 273 

Standard Deviation 640 

Refinery Crude Oil Stocks 

Respondents 270 

Nonzero Respondents 216 

Average 493 

Standard Deviation 738 

91 

60 

444 

899 

267 

217 

176 

276 

317 

244 

283 

770 

91 

59 

422 

1,132 

267 

188 

118 

209 

317 

93 

374 

982 

267 

214 

459 

652 

91 

60 

495 

1,173 

265 

213 

157 

198 

318 

243 

217 

619 

91 

60 

389 

1,070 

265 

188 

102 

177 

318 

93 

306 

775 

265 

215 

468 

662 

317 

145 

350 

783 

90 

61 

494 

1,264 

266 

214 

139 

184 

• 

317 

238 

193 

554 

90 

62 

353 

947 

266 

188 

106 

184 

317 

93 

295 

780 

266 

216 

469 

673 

MAY 

317 

144 

365 

739 

90 

61 

413 

806 

262 

177 

148 

178 

317 

141 

371 

812 

90 

61 

507 

1,259 

262 

215 

144 

195 

317 

231 

195 

542 

90 

59 

374 

918 

262 

190 

100 

165 

317 

92 

296 

851 

262 

211 

512 

729 

JUN 

318 

147 

347 

714 

90 

59 

423 

901 

262 

174 

143 

179 

318 

144 

354 

774 

90 

60 

527 

1,463 

262 

214 

165 

229 

318 

234 

231 

662 

90 

58 

404 

886 

262 

193 

99 

172 

318 

86 

322 

865 

262 

212 

511 

711 

JUL 

319 

142 

343 

693 

90 

60 

399 

789 

262 

173 

143 

176 

319 

146 

361 

802 

90 

62 

491 

1,399 

262 

212 

182 

239 

319 

234 

265 

776 

90 

59 

403 

976 

262 

190 

103 

172 

319 

85 

346 

861 

262 

212 

515 

735 

AUG 

318 

144 

305 

646 

90 

57 

419 

795 

259 

173 

135 

155 

318 

146 

326 

754 

90 

60 

491 

1,277 

259 

209 

193 

266 

318 

238 

283 

850 

90 

57 

450 

1,103 

259 

186 

101 

167 

318 

82 

314 

748 

259 

209 

463 

629 

SEP 

319 

144 

316 

656 

90 

55 

409 

720 

257 

168 

143 

165 

319 

146 

350 

802 

90 

57 

553 

1,384 

257 

206 

197 

279 

319 

239 

309 

910 

90 

59 

485 

1,358 

257 

184 

96 

173 

319 

81 

358 

893 

257 

207 

458 

627 

OCT 

319 

145 

308 

641 

90 

58 

370 

668 

257 

166 

149 

160 

319 

146 

361 

823 

90 

59 

535 

1,346 

257 

206 

197 

281 

319 

238 

350 

1,016 

90 

61 

463 

1,183 

257 

184 

109 

193 

319 

80 

382 

1,041 

257 

207 

472 

651 

NOV 

319 

141 

325 

665 

89 

59 

401 

707 

254 

166 

148 

162 

319 

144 

361 

800 

89 

59 

570 

1,404 

254 

200 

218 

316 

319 

236 

375 

1,097 

89 

62 

466 

1,295 

254 

179 

102 

175 

319 

79 

362 

1,070 

254 

202 

486 

672 

DEC 

318 

143 

342 

704 

89 

55 

427 

767 

250 

166 

152 

164 

318 

144 

379 

806 

89 

60 

551 

1,347 

250 

202 

199 

293 

318 

236 

384 

1,084 

89 

60 

504 

1,362 

250 

180 

108 

192 

318 

77 

433 

1,211 

250 

203 

479 

665 

n 

49 

Petroleum 9upply Annuel 1994, Volume I I Energy InformeUon AdmlnletreUon 
P.57 

JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV DEC 

Pipeline/Tank Farm Crude Oil Stocks 

Respondents 180 

Nonzero Respondents 147 

Average 1,338 

Standard Deviation 2,827 

179 

145 

1,331 

2,810 

179 

145 

1,295 

2,684 

179 

144 

1,366 

2,893 

179 

143 

1,403 

2,964 

180 

143 

1,369 

2,886 

180 

144 

1,362 

2,917 

179 

143 

1,347 

2,959 

179 

142 

1,277 

2,704 

179 181 

145 143 

1,358 1,394 

2,894 3,073 

182 

143 

1,407 

3,095 

Note 14: EIA-820: Annual Refinery 

Report 

Background 

The Form EIA-820, Annual Refinery Report, Is used to 

collect data measuring current and next year projections for refinery Input of crude oil and other feedstocks, and resultant product yields; working and shell 

storage capacity for crude oil and petroleum products 

at the refinery; current year and next year projections 

for operable capacity of refining facilities; refinery receipts of crude oil by method of transportation; and 

fuels consumed for all purposes at the refinery. 

Refinery capacity data collection was begun In 1918, by 

the Bureau of Mines (BOM), then In the Department of 

Commerce and was operated on a voluntary basis until 

1980. 

In 1980, the mandatory Energy Information Administration (EIA) Form EIA-177, Capacity of Petroleum Refineries, was implemented. Information on refining capacity was expanded to include not only current year 

operations but two year projections, and refinery input/production data where requested. 

In 1983, the form was revised to Improve the consistency and quality of the data collected by the EIA and redesignated as Form EIA-820, Annual Refinery Report. 

Two sections for data previously reported monthly were 

added to the annual: (1) refinery receipts of crude oil by 

method of transportation, and (2) fuels consumed for all 

purposes. Also, the second year projections were eliminated. As a result of a study conducted by the EIA evaluating motor gasoline data collected by the Federal 

Highway Administration (FHWA) and by the EIA, motor 

gasoline blending plants were included for the first 

time In the universe of respondents In order to produce 

more accurate statistics on the production of motor 

gasoline. 

the petroleum industry such as refinery sales, mergers 

and new operations. 

Information Collected 

The main items of information collected annually are 

current year and next year projections for refinery input 

of crude oil and other feedstocks, and resultant product 

yields; working and shell storage capacity for crude oil 

and petroleum products at the refinery; current year 

and next year projections for operable capacity of refining facilities; refinery receipts of crude oil by method of 

transportation during the preceding year; and fuels 

consumed for all purposes at the refinery during the 

preceding year. 

Collection Methods 

The Form EIA-820 is sent to respondents during the 

first week of the current report year and completed 

forms are required to be postmarked by the 15th day of 

February of that year. 

Receipt of the reports are monitored using an automated respondent mailing list. Telephone follow-up calls 

are made to secure responses from those companies 

failing to report by February 15th. Data are estimated 

and non-compliance procedures are implemented for 

those companies still not reporting data by close-out 

for the report year. 

Resubmissions are required whenever an error greater 

than five percent of the true value is discovered. In the 

event of a reporting error, company reports are updated 

after contact with the company and are followed-up by 

corrected reports resubmissions. Company reports or 

resubmissions received after the data close-out for the 

report year are not processed, but are filed with other 

respondent reports. 

Imputing Missing Data 

Description of Survey Universe 

The reporting universe consists of all operating and 

idle petroleum refineries and blending plants (including 

new refineries under construction) located In the 50 

States, the District of Columbia, Puerto Rico, the Virgin 

Islands, the Hawaiian Foreign Trade Zone, and Guam. 

As of January 1,1985 there were 223 refineries and 29 

motor gasoline blending plants located in the 50 states. 

The list of respondents is maintained by monitoring the 

monthly Form EIA-810, Monthly Refinery Report, and 

industry publications for changes and developments in 

The response rate for the Form EIA-820 is normally 

very high. For the January 1,1985 survey, only three refineries failed to report, thereby requiring imputation. 

For nonrespondents, the following imputation methodology is applied: 

Sections 14 2: Projected Refinery Input/Production Data 

The estimates for these sections are based on data reported on the previous year's report and the monthly 

Form EIA-810, Monthly Refinery Report. The monthly 

data are summed and divided by 365 days to arrive at a 

barrels per calendar day figure. 

50 

Petroleum tupply Annuel 1994, Volume I I Enorgy Informetlon AdmlnletreUon 
P.58 

Section 3: Working and Shell Storage Capacity 

The estimates for this section are based on previous 

year's data. The shell capacity is taken directly from the 

previous year's report. The working capacity is estimated as 92 percent of the shell capacity reported. 

Section 4: Operable Capacity of Crude Oil 

Distillation and Downstream Facilities 

Estimates for this section are based on data reported 

on the previous year's annual report and the monthly 

Form EIA-810, Monthly Refinery Report. The crude oil 

distillation capacity, In barrels per calendar day, is 

taken from the January 1985 monthly report. A barrels 

per stream day capacity Is derived by dividing the reported capacity by .95. Downstream facilities and all 

projected capacities are taken from the previous year's 

annual report. 

Section 5: Refinery Receipts of Crude Oil by 

Method ot Transportation during 1984 

The estimates for this section are based on data reported on the monthly Form EIA-810, Monthly Refinery Report. The monthly data for 1984 are summed to arrive at 

a total for domestic and foreign receipts of crude oil. 

The method of transportation is taken from the previous year's annual report. The difference between the 

total receipts reported in 1984 and the total receipts reported on the annual report are distributed proportionately to the method of transportation categories. 

Section 6: Fuels Consumed for All Purposes at 

Refineries during 1984 

The estimates for this section are based on data reported on the monthly Form EIA-810, Monthly Refinery Report. To arrive at 1984 fuels consumed data, a ratio of 

fuel use to fuel use and losses is determined for each 

product category from the aggregated monthly data for 

1983 and applied to the 1984 monthly aggregated data 

for similar product categories. 

Note 15: Annual Refinery ReportAccuracy of the Data 

There are two types of errors usually associated with 

data produced from a survey—sampling errors and nonsampling errors. Sampling errors are those errors that 

occur when survey estimates are based on a sample 

rather than being derived from a complete census of 

the frame. Nonsampling errors, sometimes referred to 

as biases, are those which can arise from a number of 

sources: (1) the inability to obtain data from all companies in the frame or sample (nonresponse) and the 

method used to account for nonresponses, (2) definitional difficulties and or improperly worded questions 

which lead to different interpretations, (3) mistakes in 

recording or coding the data obtained from respondents, and (4) other errors of collection, response, coverage, and estimation. Because estimates from the Form 

EIA-820 survey are based on a complete census of the 

frame of petroleum refineries and motor gasoline 

blending plants, there is no sampling error in the data 

presented in this report. The data, however, are subject 

to nonsampling errors. Quality control procedures are 

employed in the collection and editing operations in an 

attempt to minimize misinterpretation and misreporting. Nonresponse follow-up procedures are employed 

to reduce the number of nonrespondents, and procedures employed to impute missing data, introduce a 

minimal amount of bias, given the relatively small volume of imputed data. 

Note 16: Annual Refinery ReportMotor Gasoline Blending Plants 

Most finished motor gasoline production occurs at petroleum refineries. However, some production takes 

place at blending facilities which mechanically blend 

gasoline components into finished motor gasoline. The 

following is a list of motor gasoline blending plants and 

their locations that operated during 1984 or reported on 

the Form EIA-820 for 1985. 

Apex Oil Co. 

Wilmington, North Carolina 

Apex Oil Co. 

Albany, New York 

B-T Energy Corp. 

New Albany, Indiana 

Citgo Petroleum Corp. 

Linden, New Jersey 

Edgington Oil Co. Inc. 

Signal Hill, California 

Florida Hydrocarbons Co. 

Brooker, Florida 

GATX Terminal Corp. 

Pasadena, Texas 

GATX Terminal Corp. 

Carteret, New Jersey 

IDA Gasoline Co. Inc. 

Belcher, Louisiana 

Intercontinental 

Terminal Co. 

Deer Park, Texas 

IOT Energy Co. 

St. Louis, Missouri 

LandseaOHCo. 

Martinez, California 

Landsea Oil Co. 

Pasadena,Texas 

Long Beach Terminal Co. 

Long Beach, California 

Marion Petroleum 

Distributing 

Ocala, Florida 

Morgan Production Inc. 

Karnack, Texas 

Northville Industries Corp. 

Linden, New Jersey 

Northville Industries Corp. 

Riverhead, New York 

Northville Industries Corp. 

Setauket, New York 

Oil Tanking of Texas Inc. 

Houston, Texas 

Phillips Petroleum Co. 

Jefferson City, Missouri 

Phillips Petroleum Co. 

East St. Louis, Indiana 

Phillips Petroleum Co. 

Decatur, Illinois 

Phillips Petroleum Co. 

Kansas City, Kansas 

Primary Oil & Energy Corp. 

Chester, Virginia 

Sergeant Oil & Gas Co. 

Houston, Texas 

Southland Oil Co. 

Vicksburg, Mississippi 

Western Refining Corp. 

Grand Junction, Colorado 

Wickland Oil Terminal Co. 

Crockett, California 

51 

Petroleum 9upply Annuel 1994, Volume I I Enorgy Informetlon AdmlnletreUon 
P.59 

Definitions of Petroleum Products and 

Other Terms 

Alcohol. The family name of a group of organic chemical compounds composed of carbon, hydrogen, and 

oxygen. The series of molecules vary in chain length 

and are composed of a hydrocarbon plus a hydroxyl 

group; CH-(CH)n-OH. Alcohol includes methanol and 

ethanol. 

Alkyiation. A refinery process for chemically combining 

isoparaffin with olefin hydrocarbons. The product, alkylate, has high octane value and is blended with motor 

and aviation gasoline to improve the antiknock value of 

the fuel. 

API Gravity. An arbitrary scale expressing the gravity or 

density of liquid petroleum products. The measuring 

scale is calibrated in terms of degrees API; it may be 

calculated in terms of the following formula: 

Deg API = 

141.5 

spgr60F/60F 

-131. 5 

Aromatics. Hydrocarbons characterized by unsaturated 

ring structures of carbon atoms. Commercial petroleum aromatics are benzene, toluene, and xylene. 

Asphalt. A dark-brown-to-black cement-like material 

containing bitumens as the predominant constituents, 

obtained by petroleum processing. The definition includes crude asphalt as well as the following finished 

products: cements, fluxes, the asphalt content of 

emulsions (exclusive of water), and petroleum distillates blended with asphalt to make cutback asphalts. 

The conversion factor for asphalt is 5.5 barrels of 42 

U.S. gallons per short ton. 

ASTM. The acronym for the American Society for Testing and Materials. 

Aviation Gasoline Blending Components. Finished 

components in the gasoline range which will be used 

for blending or compounding into finished aviation 

gasoline. 

Aviation Gasoline (Finished). All special grades of 

gasoline for use in aviation reciprocating engines, as 

given in ASTM Specification D910 and Military Specification MIL-G5572. Excludes, blending components 

which will be used in blending or compounding into finished aviation gasoline. 

Barrel. A volumetric unit of measure for crude oil and 

petroleum products equivalent to 42 U.S. gallons. This 

measure is used in most statistical reports. Factors for 

converting petroleum coke, asphalt and wax to barrels 

aro given in the definitions for these products. 

Barrels Per Calendar Day. See Operable Capacity. 

Barrels Per Stream Day. See Operable Capacity. 

Bi-Metallic. A term used to describe a type of catalyst. 

A catalytic process utilizing a catalyst comprised of 

two metals (e.g. platinum, rhenium). 

Butane. A normally gaseous straight-chain or branchchain hydrocarbon. (C4H10). It is extracted from natural 

gas or refinery gas streams. It includes isobutane and 

normal butane and is covered by ASTM Specification 

D1835 and Gas Processors Association Specifications 

for commercial butane. 

Isobutane. A normally gaseous branch-chain hydrocarbon, (C4H10). It is a colorless paraffinic gas that 

boils at a temperature of 10.9 degrees F. It is extracted from natural gas or refinery gas streams. 

Normal Butane. A normally gaseous straight-chain 

hydrocarbon, (C4H10). It is a colorless paraffinic gas 

that boils at a temperature of 31.1 degrees F. It is extracted from natural gas or refinery gas streams. 

Butylene. An olefinic hydrocarbon, (C4H8), recovered 

from refinery processes. 

Catalytic Cracking. The refining process of breaking 

down the larger, heavier, and more complex hydrocarbon molecules into simpler and lighter molecules. 

Catalytic cracking is accomplished by the use of a catalytic agent and is an effective process for increasing 

the yield of gasoline from crude oil. 

Catalytic Hydrocracking. A refining process for converting middle boiling or residual material to high-octane gasoline, reformer charge stock, jet fuel and/or 

high grade fuel oil. Hydrocracking is an efficient, relatively low temperature process using hydrogen and a 

catalyst. 

Catalytic Hydrotreatlng. A process for treating petroleum fractions (e.g. distillate fuel oil and residual oil) and 

unfinished oils (e.g. naphthas, reformer feeds and 

heavy gas oils) in the presence of catalysts and substantial quantities of hydrogen to upgrade their quality. 

Catalytic Reforming. .The use of controlled heat and 

pressure with catalysts to effect the rearrangement of 

certain hydrocarbon molecules without altering their 

composition appreciably; the conversion of low-octane 

gasoline fractions into higher octane stocks suitable 

for blending into finished gasoline; also the conversion 

of naphthas to obtain a more volatile product of higher 

octane number. 

Conventional. A term used to describe a type of catalyst. A catalytic process utilizing a catalyst comprised 

of a metal and a non-metal (e.g. platinum, alumina). 

Coaf. A generic term applied to carbonaceous rocks 

that were formed by the partial or complete decomposition of vegetation. These stratifed carbonaceous rocks 

are either solid or brittle and are highly combustible. In52 

Petroleum Eupply Annuel 1994, Volumo I I Enorgy Informetlon Admlnlotrotlon 
P.60 

eludes lignite, bituminous coal, and anthracite which 

conform to ASTM Specification D388. 

Crude Distillation. The refining process of separating 

crude oil components by heating and subsequent condensing of the fractions by cooling. 

Crude Oil (including Lease Condensate). A mixture of 

hydrocarbons that existed in liquid phase in underground reservoirs and remains liquid at atmospheric 

pressure after passing through surface separating facilities. Included are lease condensate and liquid hydrocarbons produced from tar sands, gilsonite and oil 

shale. Drip gases are also included, but topped crude 

oil (residual) oil and other unfinished oils are excluded. 

Liquids produced at natural gas processing plants and 

mixed with crude oil are likewise excluded where identifiable. Crude oil is considered as either domestic or 

foreign according to the following: 

Domestic. Crude oil produced in the United States or 

from its "outer continental shelf" as defined in 43 

U.S.C. 1331. 

Foreign. Crude oil produced outside the United 

States. Imported Athabasca hydrocarbons are included. 

Delayed Coking. A process to produce low Conradson 

carbon gas oil for catalytic cracking feedstock and for 

gasoline. 

Distillate Fuel Oil. A general classification for one of 

the petroleum fractions produced in conventional distillation operations. It is used primarily for space heating, on-and-off-highway diesel engine fuel (including 

railroad engine fuel and fuel for agricultural machinery), 

and electric power generation. Included are products 

known as No. 1, No. 2, and No. 4 fuel oils; No. 1, No. 2, 

and No. 4 diesel fuels. 

No. 1 Fuel Oil. A light distillate fuel oil intended for 

use in vaporizing pot-type burners. ASTM Specification D396 specifies for this grade maximum distillation temperatures of 400 degrees F. at the 10-percent 

point and 550 degrees F. at the 90-percent point, and 

kinematic viscosities between 1.4 and 2.2 centistokes at 100 degrees F. 

No. 2 Fuel Oil. A distillate fuel oil for use in atomizingtype burners for domestic heating or for moderate capacity commercial-industrial burner units. ASTM 

Specification D396 specifies for this grade distillation temperatures at the 90-percent point between 

540 degrees and 640 degrees F., and kinematic viscosities between 2.0 and 3.6 centistokes at 100 degrees F. 

No. 1 and No. 2 Diesel Fuel Oils. Distillate fuel oils 

used in compression-ignition engines, as given by 

ASTM Specification D975: 

No. 1-D. A volatile distillate fuel oil with a boiling 

range between 300-575 degrees F. and used in highspeed diesel engines generally operated under 

variations in speed and load. Includes type C-B diesel fuel used for city buses and similar operations. 

Properties are defined in ASTM Specification D975. 

No. 2D. A gas oil type distillate of lower volatility 

with distillation temperatures at the 90-percent 

point between 540-640 degrees F. for use in highspeed diesel engines generally operated under uniform speed and load conditions. Includes Type 

R-R diesel fuel used for railroad locomotive engines, and Type T-T fordiesel-engine trucks. Properties are defined in ASTM Specification D975. 

No. 4 Fuel Oil. A fuel oil for commercial burner installations not equipped with preheating facilities. It 

is used extensively in industrial plants. This grade is 

a blend of distillate fuel oil and residual fuel oil 

stocks that conforms to ASTM Specification D396 or 

Federal Specification VV-F-815C; its kinematic viscosity is between 5.8 and 26.4 centistokes at 100 degrees F. Also included is No. 4-D, a fuel oil for lowand medium-speed diesel engines that conforms to 

ASTM Specification D975. 

Eastern Hemisphere. That half of the earth east of the 

Atlantic Ocean which includes Europe, Asia, Africa and 

Australia. The Hawaiian Foreign Trade Zone is in this 

hemisphere. 

Electric Energy (Purchased). Electricity purchased for 

refinery operations that is not produced within the refinery complex. 

Ethane. A normally gaseous straight-chain hydrocarbon, (C2H6). It is a colorless paraffinic gas that boils at 

a temperature of -127.48 degrees F. It is extracted 

from natural gas and refinery gas streams. 

Ethylene. An olefinic hydrocarbon, (C2H4), recovered 

from refinery processes or petrochemical processes. 

Field Production. Represents crude oil production on 

leases, natural gas liquids production at natural gas 

processing plants, and new supply of other hydrocarbons and alcohol. 

Fluid Coking. A thermal process utilizing the fluidizedsolids technique for continuous conversion of heavy, 

low-grade oils into lighter products. 

Gasohol. See Motor Gasoline (Finished). 

Gas Oil. A liquid petroleum distillate having a viscosity 

intermediate between that of kerosene and lubricating 

oil. Derives its name from having originally been used 

in the manufacture of illuminating gas. Now supplies 

distillate-type fuel oils and diesel fuel, also cracked to 

produce gasoline. 

Gasoline Blending Components. Finished components 

in the gasoline range which will be used for blending or 

compounding into finished aviation or motor gasoline. 

Idle Capacity. The component of operable capacity that 

is not in operation and not under active repairs, but 

capable of being placed in operation within 30 days; 

and capacity not in operation but under active repairs 

that can be completed within 90 days. 

Imported Crude Oil Burned As Fuel. The amount of foreign crude oil burned as a fuel oil, usually as residual 

fuel oil, without being processed as such. Imported 

53 

Petroleum Supply Annuel 1994, Volume I I Energy Informetlon AdmlnletreUon 
P.61 

crude oil burned as fuel includes lease condensate and 

liquid hydrocarbons produced from tar sand oil, gilsonite, and shale oil. 

Isobutane. See Butane. 

Isomerlzatlon. A refining process which alters the 

fundamental arrangement of atoms in the molecule. 

Used to convert normal butane into isobutane, an 

alyklation process feedstock, and normal pentane and 

hexane into isopentane and isohexane, high-octane 

gasoline components. 

Kerosene. A petroleum distillate that boils at a temperature between 300-550 degrees F., that has a flash point 

higher than 100 degrees F. by ASTM Method D56, that 

has a gravity range from 40-46 degrees API, and that has 

a burning point in the range of 150-175 degrees F. Included are the two classifications recognized by ASTM 

D3699: No. 1-K and No. 2-K, and all grades of kerosene 

called range or stove oil which have properties similar 

to No. 1 fuel oil, but with a gravity of about 43 degrees 

API and a maximum end-point of 625 degrees F. Kerosene is used in space heaters, cook stoves, and water 

heaters and is suitable for use as an illuminant when 

burned in wick lamps. 

Kerosene-Type Jet Fuel. A quality kerosene product 

with an average gravity of 40.7 degrees API, and a 10 

percent distillation temperature of 400 degrees F. It is 

covered by ASTM Specification D1655 and Military 

Specification MIL-T-5624L (Grades JP-5 and JP-8). A 

relatively low-freezing point distillate of the kerosene 

type; it is used primarily for commercial turbojet and 

turboprop aircraft engines. 

Lease Condensate. A natural gas liquid recovered from 

gas well gas (associated and nonassociated) in lease 

separators or natural gas field facilities. Lease condensate consists primarily of pentanes and heavier hydrocarbons. 

Liquefied Petroleum Gases (LPG). Ethane, Ethylene, 

propane, propylene, normal butane, butylene, and isobutane produced at refineries or natural gas processing 

plants, including plants that fractionate raw natural gas 

plant liquids. 

Liquefied Refinery Gases (LRG). Liquefied petroleum 

gases fractionated from refinery or stiU gases. Through 

compression and/ or refrigeration they are retafned in 

the liquid state. The reported categories are ethane/ethylene, propane/propylene, normal butane/butylene, and isobutane. Excludes still gas used for chemical or rubber manufacture which is reported as a petrochemical feedstock and also excludes liquefied petroleum gases intended for blending into gasoline which 

are reported as gasoline blending components. Liquefied refinery gases are reported for use as petrochemical feedstock or other uses. 

Lubricating Oils. A substance used to reduce friction 

between bearing surfaces. Petroleum lubricants may 

be produced either from distillates or residues. Other 

substances may be added to impart or improve certain 

required properties. "Lubricants" includes all grades of 

lubricating oils from spindle oil to cylinder oil and 

those used in greases. The three categories include: 

Bright Stock. A refined, high viscosity lubricating oil 

base stock that is usually made from a residuum by a 

treatment such as deasphalting, acid treatment, or 

solvent extraction. 

Neutral. A distillate lubricating oil base stock with a 

viscosity that is usually not above 550 Saybolt Universal Seconds (SUS) at 100 degrees F. It is prepared by 

a treatment such as hydrofining, acid treatment, or 

solvent extraction. 

Other. A lubricating oil base stock used in finished 

lubricating oils and greases, including black, coastal, 

and red oils. 

Middle Distillates. A general classification that includes distillate fuel oil and kerosene. 

Miscellaneous Products. Includes all finished products 

not classified elsewhere, e.g., petrolatum, absorption 

oils, ram-jet fuel, petroleum rocket fuels, synthetic natural gas feedstocks, speciality oils and medicinal oils. 

Motor Gasoline Blending Components. Finished components in the gasoline range which will be used for 

blending or compounding into finished motor gasoline. 

Pool gasoline is included in this category. 

Motor Gasoline (Finished). A complex mixture of 

relatively volatile hydrocarbons, with or without small 

quantities of additives, that have been blended to form 

a fuel suitable for use in spark-ignition engines. Specifications for motor gasoline, as given in ASTM Specification D439 or Federal Specification VV-G-1690B, include a boiling range of 122-158 degrees F. at the 10-

percent point to 365-374 degrees F. at the 90-percent 

point and a Reid vapor pressure range from 9 to 15 psi. 

"Motor gasoline" includes finished leaded gasoline, 

finished unleaded gasoline, and gasohol. Blendstock is 

excluded until blending has been completed. Alcohol 

that is to be used in the blending of gasohol is also excluded. 

Finished Leaded Gasoline. Contains more than 0.05 

gram of lead per gallon or more than 0.005 gram of 

phosphorus per gallon. The actual lead content of 

any given gallon, however, may vary as a function of 

the size of the producer and company according to 

specific Environmental Protection Agency waiver 

provisions. Premium and regular grades are included, 

depending on the octane rating. Includes leaded 

gasohol. Blendstock'is excluded until blending has 

been completed. Alcohol that is to be used in the 

blending of gasohol is also excluded. 

Finished Unleaded Gasoline. Contains not more than 

0.05 gram of lead per gallon and not more than 0.005 

gram of phosphorus per gallon. Premium and regular 

grades are included, depending on the octane rating. 

Includes unleaded gasohol. Blend stock is excluded 

until blending has been completed. Alcohol that is to 

be used in the blending of gasohol is also excluded. 

Gasohol. A blend of finished motor gasoline (leaded 

or unleaded) and alcohol (generally ethanol but sometimes methanol) in which 10 percent or more of the 

product is alcohol. 

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Naphtha-Type Jet Fuel. A fuel in the heavy naphtha boiling range with an average gravity of 52.8 degrees API 

and 20 to 90 percent distillation temperatures of 290 degrees to 470 degrees F, meeting Military Specification 

MIL-T-5624L (Grade JP-4). JP-4 is used for turbojet 

and turboprop aircraft engines, primarily by the military. Excludes ram-jet and petroleum rocket fuels. 

Natural Gas. A mixture of hydrocarbons and small 

quantities of various nonhydrocarbons existing in the 

gaseous phase or in solution with crude oil in underground reservoirs. 

Natural Gas Field Facility. A field facility designed to 

process natural gas produced from more than one 

lease for the purpose of recovering condensate from a 

stream of natural gas; however, some field facilities are 

designed to recover propane, normal butane, pentanes 

plus, etc., and to control the quality of natural gas to be 

marketed. 

Natural Gas Plant Liquids. Natural gas liquids recovered from natural gas in gas processing plants, and in 

some situations, from natural gas field facilities. Natural gas liquids extracted by fractionators are also included. These liquids are defined according to the- published specification of the Gas Processors Association 

and the American Society for Testing and Materials and 

are classified as follows: Ethane, propane, normal butane, isobutane, pentanes plus, and other products 

from natural gas processing plants (i.e. products meeting the standards for finished petroleum products produced at natural gas processing plants, such as finished motor gasoline, finished aviation gasoline, special naphthas, kerosene, distillate fuel oil, and miscellaneous products). 

Natural Gasoline and Isopentane. A mixture of hydrocarbons, mostly pentanes and heavier, extracted from 

natural gas, that meets vapor pressure, end-point, and 

other specifications for natural gasoline set by the Gas 

Processors Association. Includes isopentane which is 

a saturated branch-chain hydrocarbon, (C5H12), obtained by fractionation of natural gasoline or isomerization of normal pentane. 

Normal Butane. See Butane. 

OPEC. The acronym for the Organization of Petroleum 

Exporting Countries, oil-producing and exporting countries that have organized for the purpose of negotiating 

with oil companies on matters of oil production, prices 

and future concession rights. Current members are Algeria, Ecuador, Gabon, Indonesia, Iran, Iraq, Kuwait, 

Libya, Nigeria, Qatar, Saudi Arabia, United Arab Emirates, and Venezuela. 

Operable Capacity. The amount of capacity that, at the 

beginning of the period, is in operation; not in operation, and not under active repairs but capable of being 

placed in operation within 30 days; or not in operation 

but under active repairs that can be completed within 

90 days. Operable capacity is the sum of the operating 

and idle capacity and is measured in barrels per calendar day or barrels per stream day. 

Barrels Per Calendar Day. The maximum number of 

barrels of input that can be processed in an atmospheric distillation facility during a twenty-four hour 

period after making allowances for the following limitations: 

The capability of downstream facilities to absorb 

the output of crude oil processing facilities of a given refinery. No reduction is made when a planned 

distribution of intermediate streams through other 

than downstream facilities is part of a refinery's 

normal operation. 

The types and grades of inputs to be processed. 

The types and grades of products expected to be 

manufactured. 

The environmental constraints associated with refinery operations. 

The reduction of capacity for scheduled downtime 

such as routine inspection, mechanical problems, 

maintenance, repairs and turnaround. 

The reduction of capacity for unscheduled downtime such as mechanical problems, repairs, and 

slowdowns. 

Barrels Per Stream Day. The amount a unit can process running at full capacity under optimal crude and 

product slate conditions. 

Operating Capacity. The component of operable capacity that is in operation at the beginning of the period. 

Other Hydrocarbons. Materials received by a refinery 

and consumed as raw materials. Includes hydrogen, 

coal tar derivatives, giisonite, and natural gas received 

by the refinery for reforming into hydrogen. Natural gas 

to be used as fuel is excluded. 

Pentanes Plus. A mixture of hydrocarbons, mostly pentanes and heavier, extracted from natural gas. Includes 

isopentane, natural gasoline and plant condensate. 

Petrochemical Feedstock Use. Chemical feedstocks 

derived from petroleum, principally for the manufacture 

of chemicals, synthetic rubber and a variety of plastics. 

The categories reported are "Naphtha-Less than 400 

degrees F. end-point" and "Other oils over 400 degrees 

F. end point." 

Naphtha-Less Than 400 Degrees F. End-Point. A 

naphtha with an end point of less than 400 degrees F. 

that is intended for use as a petrochemical feedstock. 

Other Oils-Over 400 Degrees F. End-Point Oils with 

an end point over 400 degrees F. that is intended for 

use as a petrochemical feedstock. 

Petroleum Coke. A residue, the final product of the condensation process in cracking. This product is reported 

as marketable coke or catalyst coke. The conversion 

factor is 5 barrels of 42 U.S. gallons per short ton. 

Marketable Coke. Those grades of coke produced in 

delayed or fluid cokers which may be recovered as 

relatively pure carbon. This "green" coke may be sold 

as is or further purified by calcining. 

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Catalyst Coke. In many catalytic operations (i.e., catalytic cracking) carbon is deposited on the catalyst 

thus, deactivating the catalyst. The catalyst is reactivated by burning off the carbon, which is used as a 

fuel in the refinery process. This carbon or coke is 

not recoverable in a concentrated form. 

Petroleum Products. Petroleum products are obtained 

from the processing of crude oil (including lease condensate), natural gas and other hydrocarbon compounds. Petroleum products include unfinished oils, 

liquefied petroleum gases, pentanes plus, aviation 

gasoline, motor gasoline, naphtha-type jet fuel, kerosene-type jet fuel, kerosene, distillate fuel oil, residual 

fuel oil, naphtha less than 400 F. end-point, other oilsover 400 F. end-point, special naphthas, lubricants, 

waxes, petroleum coke, asphalt, road oil, still gas, and 

miscellaneous products. 

Petroleum Refinery. An installation that manufacturers 

finished petroleum products from crude oil, unfinished 

oils, natural gas liquids, other hydrocarbons, and alcohol. 

Plant Condensate. One of the natural gas liquids, mostly pentanes and heavier hydrocarbons, recovered and 

separated as liquids at gas inlet separators or scrubbers in processing plants. 

Primary Stocks. Stocks of crude oil or petroleum products held in storage at (or in) leases, refineries, natural 

gas processing plants, pipelines, tankfarms, and bulk 

terminals that can store at least 50,000 barrels of petroleum products or that can receive petroleum products 

by tanker, barge, or pipeline. Crude oil that is in transit 

from Alaska, or that is stored on Federal leases or in the 

Strategic Petroleum Reserve is included. Primary 

Stocks excludes stocks of foreign origin that are held 

in bonded warehouse storage. 

Propane. A normally gaseous straight-chain hydrocarbon, (C3H8). It is a colorless paraffinic gas that boils at 

a temperature of -43.67 degrees F. It is extracted from 

natural gas or refinery gas streams. It includes all products covered by Gas Processors Association Specifications for commercial propane and HD-5 propane and 

ASTM Specification D1835. 

Propylene. An olefinic hydrocarbon, (C3H6), recovered 

from refinery processes or petrochemical processes. 

Residual Fuel Oil. The topped crude of refinery operations which includes No. 5 and No. 6 fuel oils as defined in ASTM Specification D396 and Federal Specification VV-F-815C, Navy Special fuel oil as defined in 

Military Specification MIL-F-859E including Amendment 2 (NATO Symbol F-77), and Bunker C fuel oil. Residual fuel oil is used for the production of electric power, space heating, vessel bunkering, and various industrial purposes. Imports of residual fuel oil include "Imported Crude Oil Burned as Fuel." 

Road Oil. Any heavy petroleum oil, including residual 

asphaltic oil used as a dust pallative and surface treatment on roads and highways. It is generally produced in 

six grades from 0, the most liquid, to 5, the most viscous. 

Special Naphthas. All finished products within the 

gasoline range that are used as paint thinners, cleaners, or solvents. These products are refined to a specified flash point and have a boiling range of 90 degrees 

to 220 degrees F. "Special naphthas" includes all commercial hexane and cleaning solvents conforming to 

ASTM Specification D1836 and D484, respectively. 

Naphthas to be blended or marketed as motor gasoline 

or aviation gasoline or that are to be used as petrochemical and synthetic natural gas (SNG) feedstocks 

are excluded. 

Steam (Purchased). Steam, purchased for use by a refinery, that was not generated from within the refinery 

complex. 

Still Gas (Refinery Gas). Any form or mixture of gas produced in refineries by distillation, cracking, reforming, 

and other processes. The principal constituents are 

methane, ethane, ethylene, normal butane, butylene, 

propane, propylene, etc. Still gas is reported for petrochemical feedstock use and/or refinery fuel use. 

Petrochemical Feedstock Use. Includes all refinery 

streams which are used by chemical or rubber manufacturing operations for further processing, less the 

amount of such streams returned to the source refinery. Finished petrochemical products are not included. For example, polyethylene, butadiene, etc. are 

considered petrochemical products; therefore, only 

their feedstock equivalents are included. 

Fuel Use. All other still gas. 

Strategic Petroleum Reserve (SPR). Petroleum stocks 

maintained by the Federal Government for use during 

periods of major supply interruption. 

Thermal Cracking. A refining process in which heat and 

pressure are used to break down, rearrange, or combine 

hydrocarbon molecules. Thermal cracking is used to increase the yield of gasoline obtainable from crude oil. 

Unfinished Oils. Includes ali oils requiring further processing, except those requiring only mechanical blending. 

Unfractionated Streams. Mixtures of unsegregated natural gas liquid components excluding those in plant 

condensate. This product is extracted from natural gas. 

Vacuum Distillation. Distillation under reduced pressure (less the atmospheric) which lowers the boiling 

temperature of the liquid-being distilled. This technique with its relatively low temperatures prevents 

cracking or decomposition of the charge stock. 

Visbreaking. A thermal cracking process in which 

heavy vacuum-still bottoms produced on the primary 

distillation unit are cracked to increase production of 

distillate products. 

Wax. A solid or semi-solid material derived from petroleum distillates or residues by such treatments as chilling, precipitating with a solvent, or de-oiling. It is lightcolored, more-or-less translucent crystalline mass, 

slightly greasy to the touch, consisting of a mixture of 

solid hydrocarbons in which the paraffin series pre56 

Potroloum Eupply Annuel 1994, Volumo I I Energy Informetlon Admlnlotrotlon 
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dominates. Includes all marketable wax whether crude 

scale or fully refined. The three grades included are microcrystalline, crystalline-fully refined, and crystallineother. The conversion factor is 280 pounds per 42-U.S. 

gallon barrel. 

Microcrystalline Wax. Wax extracted from certain petroleum residues having a finer and less apparent 

crystalline structure than paraffin wax and having the 

following physical characteristics: 

Penetration at 77 degrees F. (D1321)-60 maximum. 

Viscosity at 210 degrees F. in Saybolt Universal 

Seconds (SUS). (D88)-60 SUS (10.22 centistokes) 

minimum to 150 SUS (31.8 centistokes) maximum. 

Oil content (D721)-5 percent minimum. 

Crystalllne-Fully Refined Wax. A light-colored paraffin wax having the following characteristics: 

Viscosity at 210 degrees F. (D88)-59.9 SUS (10.18 

centistokes) maximum. Oil Content (D721)-0.5 percent maximum. Other +20 color, Saybolt minimum. 

Crystalline-Other Wax. A paraffin wax having the following characteristics: 

Viscosity at 210 degrees F. (D88)-59.9 SUS (10.18 

centistokes) maximum. Oil Content (D721)-0.51 

percent minimum to 15 percent maximum. 

Western Hemisphere. That half of the earth that includes North and South America and adjacent islands. 

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