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Process Equipment and Plant Design

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.

20
45
85
30

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

Less than
One-fourth of
2.5 times
1.25-1.50 times

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Process Equipment and Plant Design
In case of a continuous distillation column, increase in reflux ratio may result in the

All of these
Greater cost for the reboiler heat supply
Lower fixed charges for the column
Greater cost for the condenser coolant

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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

Increases linearly
Remains constant
Decreases very rapidly
Increases very rapidly

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

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

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

Large horizontal
Thick walled
Small horizontal
Tall vertical

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