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Process Equipment and Plant Design

Process Equipment and Plant Design
Shell side heat transfer co-efficient in case of square pitch as compared to the triangular pitch under similar condition of fluid flow and tube size is

Twice
Same
Less
More

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

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

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.5 to 0.6 d
0.2 to 0.5 d
0.02 to 0.05 d
0.08 to 0.12 d

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Low gas velocity
Large reflux ratio
Resistance offered to flow of liquids by caps & risers and the flow of gas
Large plate spacing

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Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.5 - 1.0
43833
0.01 - 0.5
0.07 - 0.12

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

43895
44183
43962
44058

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