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Process Equipment and Plant Design

Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

10-12.5
5-7.5
15-20
2.5-3.0

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B
U-bend
Floating head tube sheet
Either A or B

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Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Remains same
Decreases
Increases
Remains same, only if the number of tube passes does not change

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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)

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

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Process Equipment and Plant Design
__________ liquor is best handled in a long tube vertical evaporator.

Viscous
Scaling
Salting
Foamy

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Both B and C
Much less (say 2% than that for fully open globe valves)
Much more than that for fully open globe valves

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