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Process Equipment and Plant Design

Process Equipment and Plant Design
The normal range of velocity of steam in pipes is __________ m/sec.

10-20
0.1-0.5
1-5
80-100

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Process Equipment and Plant Design
What is the value of 'q' for saturated vapor feed to a distillation column ?(where q = fraction of the feed stream that is 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

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

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Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

1
2
3
3.5

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Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

< 30
> 7 < 15
> 20 < 50
< 7

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

0.5 - 1.0
0.01 - 0.5
0.07 - 0.12
43833

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