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Process Equipment and Plant Design

Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

45.5
5.5
12.5
30.5

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Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Inner
Outer
Approximate
None of these

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Process Equipment and Plant Design
for couplings and unions would be

350
200
60
Negligible

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.99
0.8
0.95
0.55

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Process Equipment and Plant Design
A single pass air heater is connected to a two pass unit. For the air flow rate and other conditions remaining the same, the film heat transfer co-efficient for air will vary in the ratio of

20.8
2
None of these
20.2

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

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