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Process Equipment and Plant Design

Process Equipment and Plant Design
What is the slope of the feed line, if the feed to a distillation column is a saturated liquid?

∞
< 1
> 1

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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.

1.75
1.25
2.5
3.5

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Remains same
Decreases
May increase or decrease depending upon the plate spacing
Increases

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Fouling fluids
Double pipe heat exchanger
Multipass shell and tube heat exchanger
Counter flow of hot and cold fluids

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

8
4
2
1/2

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Less than
Same as
More than
Either more or less (depending upon relative volatility)

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