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Refining & Marketing - Operational Changes
Table 18.� U.S. Refinery Configurations of FRS
Companies, Selected Years,
��������������� 1974-2006
������ ����������(Percent) |
FRS Companies |
Downstream Capacity as a Percent of
Crude Distillation Capacity |
1974 |
1981 |
1993 |
1996 |
1997 |
1999 |
2000 |
2001 |
2002 |
2003 |
2004 |
2005 |
2006 |
|
Integrated Refiners |
� Coking |
n.c. |
n.c. |
n.c. |
13.0 |
12.6 |
12.9 |
13.9 |
14.1 |
15.8 |
15.4 |
15.7 |
15.4 |
15.4 |
� Catalytic cracking |
27.7 |
30.4 |
36.5 |
33.8 |
35.9 |
35.8 |
35.6 |
35.2 |
33.0 |
33.4 |
33.7 |
33.7 |
33.9 |
� Catalytic reforming |
17.6 |
22.4 |
25.8 |
24.9 |
23.4 |
22.3 |
22.4 |
22.2 |
21.8 |
21.8 |
21.8 |
21.4 |
21.7 |
� Hydro cracking |
5.6 |
5.7 |
9.6 |
9.6 |
9.6 |
10.9 |
11.0 |
10.9 |
10.7 |
10.4 |
10.7 |
10.5 |
11.0 |
� Catalytic hydrotreating |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
79.5 |
82.3 |
85.8 |
� Alkylation |
4.8 |
5.3 |
7.7 |
6.8 |
7.5 |
7.4 |
7.4 |
7.2 |
7.1 |
7.2 |
7.3 |
7.3 |
7.5 |
|
Non-Integrated Refiners
(includes CITGO and Motiva) |
� Coking |
n.c. |
n.c. |
n.c. |
11.0 |
12.7 |
12.0 |
12.1 |
12.4 |
12.0 |
13.5 |
14.7 |
14.3 |
14.4 |
� Catalytic cracking |
n.c. |
n.c. |
n.c. |
29.8 |
34.1 |
34.0 |
35.5 |
35.5 |
36.3 |
36.7 |
38.4 |
37.2 |
37.2 |
� Catalytic reforming |
n.c. |
n.c. |
n.c. |
18.9 |
21.5 |
22.5 |
21.9 |
21.7 |
21.4 |
21.1 |
21.8 |
20.4 |
20.1 |
� Hydro cracking |
n.c. |
n.c. |
n.c. |
6.3 |
7.8 |
8.6 |
8.6 |
8.4 |
7.8 |
8.5 |
8.7 |
8.1 |
8.3 |
� Catalytic hydrotreating |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
n.c. |
71.4 |
72.7 |
73.7 |
� Alkylation |
n.c. |
n.c. |
n.c. |
6.0 |
6.8 |
6.0 |
6.3 |
6.3 |
6.4 |
6.4 |
6.9 |
6.6 |
6.6 |
� n.c.:� Information not collected.
� Sources:� Oil and Gas Journal, "Worldwide
Refinery Report," 1974, 1981, 1993, 1996, 1997, 1999, 2000, 2001, 2002,
2003, 2004, 2005, and 2006. |
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