- (A) Flow rates of each fluid
- (B) Type and size of packing
- (C) Concentration of each fluid
- (D) All A,
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- (A) hG = 1.004G0.37
- (B) 1.004G0.8
- (C) hG = 0.0176G0.37
- (D) 0.0176G1.37
- (A) 1″ dia cap with 0.5″ dia riser
- (B) 6″ dia cap with 4″ dia riser
- (C) 8″ dia cap with 1″ dia riser
- (D) 4″ dia cap with 8″ dia riser
- (A) 5 cms
- (B) 40% of the I.D. of the shell
- (C) 25 cms
- (D) I.
- (A) Half
- (B) Twice
- (C) Thrice
- (D) Five times
- (A) 1 to 2
- (B) 4 to 10
- (C) 10 to 20
- (D) 20 to 30
- (A) 30°
- (B) 45°
- (C) 60°
- (D) 75°
- (A) Increase
- (B) Decrease
- (C) Remain unaffected
- (D) Increase or decrease depending on the nature of the dust
- (A) Permit release of entrained vapour in the liquid
- (B) Reduce the discharge fluctuation
- (C) Ensure better vapour-liquid contact
- (D) Cool the liquid before it flows down
- (A) 0.5 to 1.5
- (B) 2.5 to 4.0
- (C) 5 to 10
- (D) 10 to 15

