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Process Equipment and Plant Design

Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

1.2-1.5
0.1-0.2
0.2-0.5
0.4-0.9

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Process Equipment and Plant Design
What is the value of 'q' for saturated liquid feed to a distillation column?

>1
1

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

None of these
D/2 or minimum 2" to 5D
D/5 or minimum 2" to D
D/5 or minimum 2" to 5D

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Process Equipment and Plant Design
The dust collection efficiency of electrostatic precipitator increases with increase in the

Electrode area
Both A & B
Gas flow rate
Neither A nor B

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

None of these
Density of the fluid
Viscosity of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)

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Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Ultimate stress
Elastic limit
Breaking stress
Yield stress

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