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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.

0 to 1.5
0 to 0.08
0 to 0.8
0 to 2.2

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Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

18
34
6
12

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
High film co-efficient
Non-corrosive condensate
High latent heat

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

> 3
> 5
43961
< 12.5

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Orifice
Independent of the type of
Segmental
Disk and ring

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