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Process Equipment and Plant Design

Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Pitch
Both A & B
Neither A nor B
Layout

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Process Equipment and Plant Design
Width and depth of grooves in the tube sheet holes normally are __________ inch respectively.

1/2 and 5
1/8 and 1/64
1/64 and 1/8
1/2 and 8

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Process Equipment and Plant Design
In case of plain carbon steel, butt welded joints are used for shell plate thickness ≤ __________ cms. .

3.8
0.5
6.8
1.2

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

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

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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/D
1/D⁵

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Gas blowing beneath cap skit
Maldistribution of gas
Back trapping
All of these

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