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Process Equipment and Plant Design

Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Sa = 1.5 Aa
Aa = Sa
1.2 Aa = 1.2 Sa
Aa = 1.5 Sa

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Process Equipment and Plant Design
For given number of passes, pitch & tube diameter, the maximum number of tubes that can be accommodated in a shell of tripled inside diameter will be __________ times.

About 9
About 3
Considerably more than 9
Considerably less than 9

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Tall but empty
Tall (say 30 metres), but is full of liquid
None of these
Short (< 2 m) and housed indoor

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

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

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

Fluid rates and fluid properties
Operating pressure and column diameter
Type & size of packing
All of these

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Preventing the local overstressing of the shell around the opening
None of these
Reduction of discontinuity in shape at the junction
Making the joint leak proof

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