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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

43833
0.5 - 1.0
0.01 - 0.5
0.07 - 0.12

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

3.5
2.5
1.25
1.75

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Process Equipment and Plant Design
Joint efficiency (J) for a seamless pipe is

1.2
0.85
1
< 0.5

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Process Equipment and Plant Design
Diameter of bubble caps used in high pressure columns is __________ as compared to that used in identical vacuum columns.

Same
More
Either A or B; no generalisation can be made
Less

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Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Hemispherical
Dished
Ellipsoidal
Conical

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Process Equipment and Plant Design
An adequate clearance between the tray and the shell wall of a distillation column is provided to

None of these
Drain the liquid from the tray when the unit is not in operation
Allow for thermal expansion and facilitate installation
Avoid back-trapping

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