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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

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

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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

Remains constant
Increases linearly
Increases very rapidly
Decreases very rapidly

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Process Equipment and Plant Design
Diameter of rivet hole (d, mm) and the plate thickness (t, mm) are related by Unwin's formula as

D = 3√t
D = 1.6 √t
D = 1.1 t
D = 1.5 t

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering branch) would be

Around 90
Both B and C
Less than that for Tee (used as elbow, entering run)
More than that for Tee (used as elbow, entering run)

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Counter flow of hot and cold fluids
Multipass shell and tube heat exchanger
Fouling fluids
Double pipe heat exchanger

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Process Equipment and Plant Design
A claming section before the liquid flows into the downcomer is privided to

Ensure better vapour-liquid contact
Cool the liquid before it flows down
Reduce the discharge fluctuation
Permit release of entrained vapour in the liquid

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