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Process Equipment and Plant Design

Process Equipment and Plant Design
The thickness of segmental baffles (25 -35% cut truncated plates usually) is generally __________ the tube wall thickness.

Equal to
Half
Four times
Twice

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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

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

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

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

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

30.5
45.5
5.5
12.5

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Decreases
Remains same
May increase or decrease depending upon the plate spacing
Increases

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Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√(2πd)
√(2d)
D
√d

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