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

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.5
G0.2
G1.5
G0.8

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

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the shell side cross flow area does not depend upon

Baffle spacing
Pitch
Clearance
None of these

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Process Equipment and Plant Design
Baffles may be eliminated for

Large diameter tanks
None of these
High viscosity liquids (> 600 poise)
Low viscosity liquids (< 200 poise)

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

Sieve plate
None of these
Bubble cap plate
Packed

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