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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

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

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Packed
Bubble cap plate
None of these
Sieve plate

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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

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

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Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Layout
Both A & B
Pitch
Neither A nor B

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Back trapping
Gas blowing beneath cap skit
Maldistribution of gas
All of these

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be supported very easily
Withstand higher pressure for a given metallic shell thickness
Be fabricated very easily
Be designed without wind load considerations

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