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Process Equipment and Plant Design

Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

2.5 to 5
1.5 to 2
10 to 15
5 to 10

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large plate spacing
Resistance offered to flow of liquids by caps & risers and the flow of gas
Low gas velocity
Large reflux ratio

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Columns
Saddles
Skirts

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

None of these
Packed
Bubble cap plate
Sieve 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
Is easy to fabricate
Has greater structural strength

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Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

3 to 5
6 to 12
2 to 3
4 to 8

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