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Process Equipment and Plant Design

Process Equipment and Plant Design
With increase in gas flow rate to fabric surface area ratio (Nm³/hr/m² fabric surface area), the size & the cost of a bag filter

None of these
Increases
Decreases
Remain unaffected

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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

0.8
0.95
0.55
0.99

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Process Equipment and Plant Design
Diameter of bubble caps used in high pressure columns is __________ as compared to that used in identical vacuum columns.

Same
More
Either A or B; no generalisation can be made
Less

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Inadequate equipment design
Failure of equipments
Improper layout of the equipments
Faulty operating procedures

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Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

15-20
2.5-3.0
10-12.5
5-7.5

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B
Either A or B
Floating head tube sheet
U-bend

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