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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum baffle height should be

3/4 of the tank height
Twice the tank diameter
Equal to the impeller diameter
Twice the impeller diameter

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Process Equipment and Plant Design
A claming section before the liquid flows into the downcomer is privided to

Reduce the discharge fluctuation
Cool the liquid before it flows down
Ensure better vapour-liquid contact
Permit release of entrained vapour in the liquid

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Process Equipment and Plant Design
In a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, D₁ and D₂ are I.D. of inner and outer pipes)

None of these
D₂ - D₁
(D₂² - D₁²)/D₂²
(D₂² - D₁²)/D₁²

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Process Equipment and Plant Design
For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

Bubble cap
Sieve
Counterflow
Valve

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Process Equipment and Plant Design
The wall thickness of thin cylindrical shell with hemispherical ends is __________ that of the spherical ends.

Less than
Either B or C; depends on maximum permissible internal pressure
More than
Equal to

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Double pipe heat exchanger
Fouling fluids
Counter flow of hot and cold fluids
Multipass shell and tube heat exchanger

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