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Process Equipment and Plant Design

Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₂/S₁
S₁/S₂
S₁.S₂
1/S₁.S₂

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

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

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

2
8
1/2
4

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Plain carbon steel and cast iron parts are used
Both B & C
Material of construction is high alloy steel
Wall thickness is > 30 mm

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

1.2-1.5
0.4-0.9
0.2-0.5
0.1-0.2

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Process Equipment and Plant Design
Correct use of 'factor of safety' is very important in equipment design. It is defined as the ratio of the

Ultimate stress to breaking stress
Ultimate stress to working stress
Working stress to ultimate stress
None of these

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