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Process Equipment and Plant Design

Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

12.5 to 18.5
4 to 8
3 to 12.5
L to 3

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Process Equipment and Plant Design
Maximum allowable vapour velocity in a bubble cap tower is determined by the

Vapour density
Entrainment considerations
None of these
Diameter of the column

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Both A & B
Results in higher pressure drop per tray
Leads to high tray efficiency
Neither A nor B

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Neither A nor B
Cap pitch of 1.3-2 times the cap diameter
Clearance of 25-75 mm
Either A or B

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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
S₂/S₁
1/S₁.S₂
S₁/S₂

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Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

5
25
15
1

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