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Process Equipment and Plant Design

Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Inside diameter
Wall thickness
None of these
Outside diameter

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

1.75
3.5
2.5
1.25

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

Less than
2.5 times
1.25-1.50 times
One-fourth of

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Process Equipment and Plant Design
The value of fouling factor depends upon the

Characteristic of process fluid
All of these
Suspended solids in the fluid
Velocity of process fluid containing suspended solids

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Process Equipment and Plant Design
Overall mass transfer co-efficient in case of absorption of __________ in water is based on the gas film co-efficient only, as the mass transfer process is gas film (phase) controlling.

CO₂
NH₃
None of these
SO₂

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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

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

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