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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

None of these
Torispherical
Elliptical
Hemispherical

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

1
2
3.5
5.5

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Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

1 to 12
0.25 to 8
0.25 to 4
1 to 5

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

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

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Process Equipment and Plant Design
A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

95
80
45
60

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