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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

< 7
> 20 < 50
< 30
> 7 < 15

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Process Equipment and Plant Design
In a multiple effect evaporator system having 'n' effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

1.5 nth
0.5 nth
nth
(1/n)th

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

More than
Same as
Less than
Either more or less (depending upon relative volatility)

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Process Equipment and Plant Design
The ratio of lateral strain to linear strain is termed as the

Poisson's ratio
Modulus of elasticity
Shear modulus
Bulk modulus

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

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

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Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

7500
2500
15000
1250

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