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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

Both A & B
Layout
Pitch
Neither A nor B

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Tall vertical
Small horizontal
Large horizontal
Thick walled

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

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

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant
Decreases very rapidly
Increases linearly
Increases very rapidly

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Process Equipment and Plant Design
In case of 1.5" heat exchanger tubes, the inside flow area __________ with decrease in BWG.

None of these
Decreases
Remains same
Increases

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Process Equipment and Plant Design
In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds.

12.5
17.5
5
2.5

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