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Process Equipment and Plant Design

Process Equipment and Plant Design
Most of the storage vessels/tanks are made cylindrical, because of the fact that a cylinder

Both A & B
Neither A nor B
Has greater structural strength
Is easy to fabricate

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Process Equipment and Plant Design
In condenser, the cooling water is passed in the tube side in a pass arrangement, because

It reduces heat transfer area
Pressure drop is reduced
More thinner tubes can be used
It makes condenser compact

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Process Equipment and Plant Design
Which of the following is not a graphical method (but is an analytical method) for the calculation of theoretical number of stages in case of continuous binary distillation?

McCabe-Thiele's method
Ponchon-Savarit method
None of these
Sorel-Lewis method

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase catalytic reactor
A liquid phase reactor
A vapor phase reactor
Pot type reactor

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Process Equipment and Plant Design
__________ is the determining factor for the number of bubble caps to be used per tray.

Permissible slot velocity
Tray diameter
Vapor load
Liquid load

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Increases very rapidly
Decreases very rapidly
Remains constant
Increases linearly

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