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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 = G0.5
Δp = 1/G0.6
Δp = G2
Δp = G

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

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

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

None of these
Approximate
Inner
Outer

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

< 4 : 1 for gas-gas exchangers
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
4 : 1 to 8 : 1 for liquid-liquid exchanger
Both B & C

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Process Equipment and Plant Design
Rivets are generally specified by the

Head diameter
Overall length
Shank diameter
None of these

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Process Equipment and Plant Design
Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?

Smaller dia vessel
Strength of the vessel is same irrespective of the diameter
Larger dia long vessel
Larger dia vessel

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