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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = 1/G0.6
Δp = G0.5
Δp = G
Δp = G2

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Process Equipment and Plant Design
Typical static submergence for bubble cap plate column operating at atmospheric pressure may be around

0.5"
50% of the plate spacing
2.5"
5"

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

L to 3
12.5 to 18.5
3 to 12.5
4 to 8

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Process Equipment and Plant Design
Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

I.D. of the shell
25 cms
5 cms
40% of the I.D. of the shell

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Large diameter tanks
All of these
Small diameter tall tanks
Small diameter tanks

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

High film co-efficient
High latent heat
Non-corrosive condensate
Low cost

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