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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

4 to 8
6 to 12
2 to 3
3 to 5

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

Operating pressure and welding/joint efficiency
Ultimate tensile strength (or yield point) of the material and operating temperature
All of these
Diameter of the vessel

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/5 or minimum 2" to D
D/2 or minimum 2" to 5D
D/5 or minimum 2" to 5D
None of these

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

Hemispherical
Torispherical
None of these
Elliptical

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Process Equipment and Plant Design
Reflux ratio variation in a distillation column is between

Minimum and infinity
None of these
Zero and infinity
Zero and one

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Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/4t
pD/2t
pD/6t
pD/3t

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