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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
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

Decreases
Remains same
May increase or decrease depending upon the solubility of the gas in the liquid
Increases

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

3 to 12.5
12.5 to 18.5
4 to 8
L to 3

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Process Equipment and Plant Design
Back-trapping in a distillation column results due to

Excessive liquid gradient over the tray
Low reflux ratio
Low gas velocity
High gas velocity

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

0.5 metre
2.5 metres
6 metres
10 metres

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Both B & C
More than arithmetic mean value
Less than arithmetic mean value
More than geometric mean value

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