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Process Equipment and Plant Design

Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

One-fourth of
Less than
2.5 times
1.25-1.50 times

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity
Is highly viscous
Is of high specific gravity

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Lower limit of vapour velocity
Hole diameter of the seive tray
Upper limit of the vapour velocity
Height of the plate spacing

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Process Equipment and Plant Design
What is the slope of the operating line in the stripping section of a distillation column?

< 1
> 1
?

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Process Equipment and Plant Design
In inclined long tube vertical evaporators, the tubes are inclined at an angle of

90°
60°
15°
45°

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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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