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Process Equipment and Plant Design

Process Equipment and Plant Design
Vertical vessels are not supported by

Columns
Brackets
Skirts
Saddles

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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
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

4(0.86p² - πd²/4)/πd
(4p² - πd²/4)/πd
(p² - πd²/4)/πd
4(0.86p² - πd²)/πd

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Small diameter tall tanks
Large diameter tanks
Small diameter tanks
All of these

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

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Process Equipment and Plant Design
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of

(1.2)3/2
(1.2)5/3
(1.2)2/3
(1.2)3/5

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