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Process Equipment and Plant Design

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

Tall vertical
Large horizontal
Thick walled
Small horizontal

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

2
8
1/2
4

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Process Equipment and Plant Design
A pipe is generally made of circular cross-section, because a circular cross-section has the

None of these
Higher structural strength
Both A & B
Lowest surface area requirement for a given volume

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

10000
3000
5000
1000

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Neither A nor B
Both A & B
Results in higher pressure drop per tray
Leads to high tray efficiency

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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
Remains same
Decreases
Increases

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