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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Bubble cap plate
None of these
Sieve plate
Packed

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Process Equipment and Plant Design
The force due to wind load acting on a tall vessel depends upon its

Shape
Outside diameter
Height
All of these

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

43961
> 3
< 12.5
> 5

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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
15
1

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Hemispherical
Torispherical
Conical or flat plate
Elliptical

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B
Either A or B
Floating head tube sheet
U-bend

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