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Process Equipment and Plant Design

Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Columns
Skirts
Saddles

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.2
G1.5
G0.5
G0.8

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Tall but empty
Small
Large horizontal cylindrical
Thick walled tall

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Segmental
Orifice
Disk and ring
Independent of the type of

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D²
D²
1/D⁵
1/D

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Process Equipment and Plant Design
Reflux ratio variation in a distillation column is between

Zero and infinity
Zero and one
Minimum and infinity
None of these

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