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Process Equipment and Plant Design

Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₁/S₂
S₁.S₂
1/S₁.S₂
S₂/S₁

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Process Equipment and Plant Design
Baffles are provided in a shell and tube heat exchanger to increase the turbulence and velocity of the shell side fluid. Which of the following shaped baffles does not fall in the category of transverse baffle?

Disk type baffle
Segmental baffle
Flat plate extending across the wall
Helical type baffle

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.55
0.95
0.75
0.85

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

10
75
300
25

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Process Equipment and Plant Design
In packed towers provided with pall rings liquid redistributors are positioned at heights of every 6 metres or 5-10 times the column diameter, whichever is less. Maximum size of the pall rings should not exceed __________ of the column diameter.

1/10-1/15th
1/2 to 1/4th
1/20-1/30th
1/5-1/10th

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Process Equipment and Plant Design
Which of the following factors affect the pressure drop in a co-current gas-liquid absorption packed tower?

Fluid flow rates
All of these
Density and viscosity of fluids
Size, shape, orientation and surface of the packing particles

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