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Process Equipment and Plant Design

Process Equipment and Plant Design
The thickness of segmental baffles (25 -35% cut truncated plates usually) is generally __________ the tube wall thickness.

Equal to
Four times
Twice
Half

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Increases
Decreases
Remains same
May increase or decrease depending upon the plate spacing

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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
G1.5
G0.8
G0.2

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Process Equipment and Plant Design
Which of the following packing materials provides for maximum mass transfer?

Raschig rings
Cross-partition rings
All of these
Lessig rings

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

45°
60°
75°
30°

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