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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

More
Same
Less
More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Square pitch
Heat transfer rate is independent of tube arrangement
Diagonal square pitch
Triangular pitch

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Process Equipment and Plant Design
Where does the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure?

At the inner surface
At the outer surface
None of these
At the mid thickness of the cylindrical wall

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

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

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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

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

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