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Process Equipment and Plant Design

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.55
0.75
0.95
0.85

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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
10 metres
2.5 metres
0.5 metre

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Double pipe heat exchanger
Fouling fluids
Counter flow of hot and cold fluids
Multipass shell and tube heat exchanger

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

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

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

Skirt clearance
Static submergence
Downcomer liquid seal
None of these

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Process Equipment and Plant Design
A claming section before the liquid flows into the downcomer is privided to

Ensure better vapour-liquid contact
Permit release of entrained vapour in the liquid
Reduce the discharge fluctuation
Cool the liquid before it flows down

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