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Process Equipment and Plant Design

Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D⁵
D⁹
D²
D

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Process Equipment and Plant Design
Longitundinal stress induced in a thin walled cylindrical storage vessel is

PD/2t
PD/3t
PD/6t
PD/4t

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

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

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

Minimum
0
1
∞

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

None of these
Density of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)
Viscosity of the fluid

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Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Increases
Remains same
Remains same, only if the number of tube passes does not change
Decreases

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