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Process Equipment and Plant Design

Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

30.5
12.5
45.5
5.5

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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
σh = 2 σL
σh = σL/2

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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
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

None of these
Increase by 21.6
Decrease by 22
Increase by 1.8

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thick walled vertical
Horizontal
None of these
Thin shperical (e.g. Horton sphere)

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Process Equipment and Plant Design
Needle valves are generally not used for

Very large diameter pipes
Smaller sizes of pipe
High pressure throttling service
Very accurate flow control

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