Coll 30/146 'Oil: Bahrain Petroleum Company: Annual Reports.' [‎62r] (123/767)

12 -
(q) Alterations and additions to the shipping facilities at Sltra.
With the completion of the foregoing facilities, the major items of refining
equipment and their respective nominal capacities may be summarized as follows:-
Number
of Units
3
1
2
2
1
1
1
1
1
1
1
2
4
2
1
2
Description
Crude Distillation Units
Power Kerosene Rerun Unit
Gasoline Reforming Units
Thermal Cracking Units
Kerosene S0 2 Treating Plant
Nominal Capacity
65,000 BPCD
2,500 BPCD
13,000 BPCD
13,500 BPCD
8,100 BPCD
Fluid Catalytic Cracking Unit{Finished 100
)Octane Aviation
Butane Isomerization Plant {Gasoline
)production
Alkylation Unit )capacity.
Cracked Gasoline Acid Treating Plant
Kerosene Acid Treating Plant
Aviation Gasoline Acid Treating Plant
Kerosene Sweetening Plants )
Gasoline Sweetening Plants
Sulfuric Acid Manufacturing Plants
6 ,000 BPCD
6 ,000 BPCD
3,100 BPCD
8,350 BPCD
)Combined capacity com-
jmensurate with output.
Sulfuric Acid Recovery Plant
Power Plants - Total Nominal Steam
35 Tons
CAL/Day.
123 Tons
Stream Day
Generation - 5 30,000#/Hr. 550# Steam
- Total Nominal Power
Output
- 11,000 Kilowatts
At the end of the year 1945, the following construction was still in progress,
NEW REFINERY STOREHOUSE
To accommodate increased storehouse supplies necessary for satisfact y p
tion of the enlarged refining facilities installed during the past two years,
98’ X 204' storehouse was started during the latter part of 1945 and will be co p
early in 1946 .