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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)

S₂/S₁
1/S₁.S₂
S₁.S₂
S₁/S₂

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/5 or minimum 2" to 5D
None of these
D/2 or minimum 2" to 5D
D/5 or minimum 2" to D

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

None of these
Thick walled vertical
Thin shperical (e.g. Horton sphere)
Horizontal

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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
Packed
Bubble cap plate

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Nozzle or rim
Fluid in
Flared out
Ring plate

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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