- (A) Diameter of the bubble cap column
- (B) Diameter of the sieve plate column
- (C) Tray pressure drop
- (D) Residence time in the downcomer for the disengagement of entrained vapour
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- (A) 50 to 100
- (B) 100 to 150
- (C) 250 to 500
- (D) 600 to 700
- (A) Equal to
- (B) More than
- (C) Less than
- (D) Either
- (A) ∞
- (B) 1
- (C) 20.8
- (D) 2
- (A) Only if the opening is on spherical vessel
- (B) Only if the opening is on a vertical cylindrical vessel
- (C) Only if the opening is on a horizontal cylindrical vessel
- (D) Irrespective of the shape of the vessel
- (A) 60
- (B) 200
- (C) 350
- (D) Negligible
- (A) 8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
- (B) 4 : 1 to 8 : 1 for liquid-liquid exchanger
- (C) < 4 : 1 for gas-gas exchangers
- (D) Both
- (A) Providing a higher skirt clearance or a higher weir
- (B) Decreasing the number of rows of caps through which the liquid flows or by decreasing the velocity of liquid flow past the caps or by reducing the distance along the tray through which the liquid must flow
- (C) Using split flow, radial flow or cascade flow for column diameter large than 4 ft
- (D) All
- (A) 0 to 0.08
- (B) 0 to 0.8
- (C) 0 to 1.5
- (D) 0 to 2.2
- (A) nth
- (B) (1/n)th
- (C) 0.5 nth
- (D) 1.5 nth

