742. DOWNS,
C. R., AND RUSHTON, J. H. Tonnage
Oxygen. Chem. Eng. Progress, vol. 1, 1947, pp. 12-20; Chem. Abs.,
vol. 41, 1947, p. 2213.
Potential examples for the use
of tonnage oxygen are discussed at some length:
Gasification of coal, synthetic gas production, synthetic liquid fuels,
chemical products (Synthine process), H2SO4 and SO2,
and metallurgical uses. Costs are
calculated as follows:
Estimated total
plant and operating costs, October 946, for producing 95% O2
|
|
|
|
|
|
Plant capacity……….…..tons per day.
|
120
|
240
|
360
|
480
|
1,000
|
Plant capacity…….…...….tons per hr..
|
5
|
10
|
15
|
20
|
42
|
95% O2 ……..…million cu. ft. per day.
|
2.88
|
5.76
|
8.64
|
10.52
|
24.00
|
Approx. plant cost …......million dollars.
|
.9
|
1.3
|
1.7
|
2.0
|
3.4
|
Total utility cost…....….dollars1 per
ton
|
1.29
|
1.27
|
1.25
|
1.22
|
1.20
|
Operating labor per ton, $80 per
day....
|
.68
|
.34
|
.23
|
.17
|
.08
|
Maintenance per ton, 2.5%………..….
|
.54
|
.39
|
.34
|
.30
|
.25
|
Fixed charges per ton, 12.5%……..….
|
2.70
|
1.95
|
1.70
|
1.50
|
1.22
|
Total
operating cost per ton….……...
|
5.21
|
3.95
|
3.52
|
3.19
|
2.75
|
Total
operating cost per 1,000 cu. ft...
……….cents………………………
|
21.7
|
16.5
|
14.7
|
13.3
|
11.5
|
Kw.-hr. per 1,000 cu. ft. for
compression…………………………
|
13.4
|
13.1
|
12.8
|
12.7
|
12.5
|
Kw.-hr. per 1,000 cu. ft. for auxiliaries
|
2.2
|
2.2
|
2.2
|
2.2
|
2.2
|
Total kw.-hr. per 1,000 cu. ft.
|
15.6
|
15.3
|
15.0
|
14.9
|
14.7
|
1Includes water, 1 cent per 1,000 gal.;
incidental electric power, 0.4 cent per kw.-hr.; steam, 30 cents per 1,000 lb.
|