2737. POWER, H. H. Petroleum
Substitutes: Past and Present Research, Development, and Economics.
Petrol. Eng., vol. 18, No. 5, 1947, pp. 70, 72, 75, 78, 80, 82, 84.
Review of the literature on the production of liquid
fuels from the hydrogenation of coal, from coal carbonization, from oil shale,
from tar sands, and from the Fischer-Tropsch synthesis, with 25 refs.
Special emphasis is placed on the economics of the various processes and
the discussion on costs is summarized in the table given below.
Process
|
Est.
reserves in U. S.
|
Size
of plant, bbl. gaso-
line
per day
|
Total
invest-
ment,
million dollars
|
Invest-
ment
cost per bbl. gasoline per day, dollars
|
Operating
costs, including depreciation
|
Bbl.
oil,
billion
|
Bbl.
gasoline, billion
|
Per
bbl.
oil,
dollars
|
Per
gal. gasoline, cents
|
Coal
hydrogenation
|
-----------
|
3,100
|
1,750
|
50
|
28,500
|
----------
|
1
15.5-22.6
|
Coal
carbonization
|
-----------
|
322
|
1,000
|
4
|
4,000
|
0.94
|
2
10
|
Oil shale
|
100
|
-----------
|
500-540
|
5.8-5.9
|
11,600-16,700
|
1.75-2.00
|
9.7-10.7
|
Tar sands
|
3
275
|
-----------
|
3,000
|
8
|
2,670
|
.75
|
(Compete
with gasoline from crude oil.)
|
Fischer-Tropsch:
|
|
|
|
|
|
|
|
European
process using coal
|
-----------
|
4,000
|
6,000
|
45.6
|
7,600
|
-----------
|
1
19.2
|
European
process using natural gas
|
-----------
|
15
|
6,000
|
28.5
|
4,750
|
-----------
|
4
8.8
|
Future
American process using coal
|
-----------
|
4,000
|
--------
|
----------
|
-----------
|
-----------
|
5
6.0
|
Future
American process using natural gas
|
-----------
|
15
|
6,000
|
20
|
3,330
|
-----------
|
4
5.25
|
1
Coal at $2.75 per ton.
2 Coal
at $1.55 per ton.
3 Total
in Western Hemisphere.
4
Natural gas at $0.05 per M cu. ft.
5 Coal
at $2.00 per ton.
PRANSCHKE, A.
See abs. 2623.
PRATJE, W. See
abs. 3052, 3053.
|