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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 7 < 15
< 7
> 20 < 50
< 30

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Process Equipment and Plant Design
The value of fouling factor depends upon the

All of these
Characteristic of process fluid
Suspended solids in the fluid
Velocity of process fluid containing suspended solids

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Process Equipment and Plant Design
Liquid/petroleum fuel storage tanks are built underground (as in case of petrol pumps), when the storage capacity is less than __________ kilolitres.

85
45
20
30

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

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Process Equipment and Plant Design
A minimum clearance of about __________ mm is maintained between the distillation column wall and the bubble cap.

95
38
19
76

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Reverse
Split
Cross
Cascade

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