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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

None of these
High viscosity liquids (> 600 poise)
Large diameter tanks
Low viscosity liquids (< 200 poise)

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Heat transfer co-efficient is proportional to 0.8th power
Pressure drop is proportional to the square
Both A & B
Neither A nor B

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Process Equipment and Plant Design
__________ liquor is best handled in a long tube vertical evaporator.

Scaling
Salting
Foamy
Viscous

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

Eddy diffusivity = 0
Plug flow
Laminar flow
Complete back mixing

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

5.5
12.5
30.5
45.5

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Process Equipment and Plant Design
Power required for agitation depends upon the

All of these
Size of agitator & the tank
Agitator type & speed of agitation
Height & properties of the liquid

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