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Process Equipment and Plant Design

Process Equipment and Plant Design
Commercial packed scrubbers are normally designed for a pressure drop range of __________ mm water coloumn per metre of packed height.

17-34
88-105
43929
52-68

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

D²
1/D²
1/D⁵
1/D

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Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Complete back mixing
Plug flow
Eddy diffusivity = 0
Laminar flow

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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

√d
√(2πd)
√(2d)
D

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Process Equipment and Plant Design
An underdesigned steam trap will

Destroy itself of acceleration wear due to rapid recycling
Back up condensate and cause water hammer in steam line
Waste steam
None of these

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Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

All of these
An increase in relatived volatility for rectification columns
An increase in liquid viscosity
Decrease in gas solubility for absorbers

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