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Process Equipment and Plant Design

Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₁/S₂
S₁.S₂
S₂/S₁
1/S₁.S₂

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Process Equipment and Plant Design
In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the

Liquid gradient on the tray
Lower skirt clearance
Lower static submergence
Small downcomer liquid seal

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Process Equipment and Plant Design
The value of fouling factor depends upon the

Suspended solids in the fluid
All of these
Characteristic of process fluid
Velocity of process fluid containing suspended solids

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Results in higher pressure drop per tray
Leads to high tray efficiency
Both A & B
Neither A nor B

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Process Equipment and Plant Design
In which of the following evaporators, steam is fed inside the tube while the liquor is outside the tube?

None of these
Long tube vertical evaporator
Horizontal tube evaporator
Short tube vertical evaporator

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Process Equipment and Plant Design
Heat transfer co-efficient, hG(Kcal/hr.m² .°C) and mass velocity of air, G (kg/hr.m² ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to

1.004G0.8
HG = 1.004G0.37
HG = 0.0176G0.37
0.0176G1.37

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