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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

25
5
1
15

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Process Equipment and Plant Design
__________ tray arrangement is recommended for distillation column having diameter upto 4 ft.

Cascade
Radial flow
Split flow
Cross flow

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Process Equipment and Plant Design
Which of the following is the most common type of baffle used in industrial shell and tube heat exchanger?

Orifice baffle
25% cut segmental baffle
Disk and doughnut baffle
75% cut segmental baffle

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

None of these
Increase by 1.8
Increase by 21.6
Decrease by 22

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Lower limit of vapour velocity
Hole diameter of the seive tray
Height of the plate spacing
Upper limit of the vapour velocity

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

1
3.5
5.5
2

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