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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

6
24
34
18

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Process Equipment and Plant Design
In a continuous distillation column, the optimum reflux ratio ranges from __________ times the minimum reflux ratio.

2.7 to 3
1.6 to 2
2.2 to 2.6
1.1 to 1.5

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Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Hemispherical
Conical
Dished
Ellipsoidal

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

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Process Equipment and Plant Design
A 'rupture disc' is provided in chemical equipments as an accessory meant for

Enhancing mixing rate
Relieving excess pressure
Creating turbulence
Avoiding vortex formation

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Process Equipment and Plant Design
With increase in pressure drop (for a given particle size), the dust collection efficiency of a cyclone separator will

Decrease
Increase
Increase or decrease depending on the nature of the dust
Remain unaffected

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