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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)

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

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Is highly viscous
Is of high specific gravity
Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Thick walled
Small horizontal
Tall vertical

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Process Equipment and Plant Design
What is the minimum recommended ligament for square pitch arrangement in case of heat exchangers?

6.5 mm
6.5 cms
Equal to tube I.D
Equal to tube O.D

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Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Bending
Elongation
Deformation
Shear

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Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

1 to 5
0.25 to 4
0.25 to 8
1 to 12

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