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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of 1.5" heat exchanger tubes, the inside flow area __________ with decrease in BWG.

Decreases
Remains same
None of these
Increases

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Lug
Saddle
Skirt
Bracket

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Process Equipment and Plant Design
The dust collection efficiency of a cyclone separator

None of these
Decreases with increase in gas flow rate
Is inversely proportional to the mass of the dust particle
Is directly proportional to the radius of the dust particle path

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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.

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

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

6 metres
2.5 metres
10 metres
0.5 metre

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Process Equipment and Plant Design
Baffles may be eliminated for

None of these
Low viscosity liquids (< 200 poise)
Large diameter tanks
High viscosity liquids (> 600 poise)

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