Page 112 - Pressure Vessel Design Manual
P. 112
General Design 93
100,000
80,000
60.000
50,000
40,000
30,000
20,000
10,000
8,000
6,000
5,000
4,000
3,000
2,000
1.000
800
600
500
400
300
200
100
80
60
50
40
30
20
10
1 1.5 2 3 4 5 6 7 8 910 15 20
Vessel Diameter, ft
(From K. Abakians, Hydrocarbon Processing and Petroleum Refiner, June 1963.)
Figure 2-58. Method 1: Chart for determining optimum diameter.
