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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.

Packed
Sieve plate
None of these
Bubble cap plate

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Process Equipment and Plant Design
Most of the storage vessels/tanks are made cylindrical, because of the fact that a cylinder

Neither A nor B
Both A & B
Has greater structural strength
Is easy to fabricate

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Back trapping
Maldistribution of gas
Gas blowing beneath cap skit
All of these

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Process Equipment and Plant Design
The operating pressure drop range in a bag filter is about __________ mm water gauge.

43961
50-150
1500-2500
500-1500

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Process Equipment and Plant Design
The minimum shell thickness for tank ≤ 15 metres diameter is limited to __________ mm, for reasons of elastic stability.

15
10
2
5

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.4-0.9
0.2-0.5
1.2-1.5
0.1-0.2

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