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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
S₁.S₂
S₁/S₂
1/S₁.S₂

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Process Equipment and Plant Design
Filtration rate is affected by the

Area of filtering surface & the viscosity of filtrate
All of these
Pressure drop across the cake & filter medium
Cake & filter medium resistance

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Both B and C
Much less (say 2% than that for fully open globe valves)
Much more than that for fully open globe valves

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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

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

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

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Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Laminar flow
Plug flow
Eddy diffusivity = 0
Complete back mixing

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