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Process Equipment and Plant Design

Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

40 to 50
55 to 75
5 to 10
15 to 30

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

< 4 : 1 for gas-gas exchangers
Both B & C
4 : 1 to 8 : 1 for liquid-liquid exchanger
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers

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

10-50
15-30
0.1-0.5
1-2

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

∞
> 1

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase reactor
Pot type reactor
A vapor phase reactor
A liquid phase catalytic reactor

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Process Equipment and Plant Design
for couplings and unions would be

60
200
Negligible
350

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