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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

10000
1000
5000
3000

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D²
D
D⁵
D⁹

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

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

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Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

34
6
24
18

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Process Equipment and Plant Design
Hold up of material in a operating rotary drier is in the range of

0.5 to 0.8
0.05 to 0.15
0.8 to 0.9
0.25 to 0.50

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

2 d
0.75 d
0.5 d
D

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