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Process Equipment and Plant Design

Process Equipment and Plant Design
In a cylinderical vessel subjected to internal pressure, the longitudinal stress σL and the circumferential stress, σh are related by

No relation exists
σh = σL/2
σh = 2 σL
σh = σL

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.95
0.55
0.8
0.99

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Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Inner
None of these
Outer
Approximate

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Process Equipment and Plant Design
Diameter of bubble caps used in high pressure columns is __________ as compared to that used in identical vacuum columns.

Same
Either A or B; no generalisation can be made
More
Less

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Neither A nor B
Leads to high tray efficiency
Results in higher pressure drop per tray
Both A & B

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Process Equipment and Plant Design
__________ is the determining factor for the number of bubble caps to be used per tray.

Permissible slot velocity
Vapor load
Tray diameter
Liquid load

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