- (A) Reflux ratio
- (B) Plate efficiency to be achieved
- (C) Thermal condition of the feed
- (D) Relative volatility
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- (A) Use steam distillation
- (B) Use molecular distillation
- (C) Use high pressure distillation
- (D) An azeotrope may be formed during distillation
- (A) 500
- (B) 1200
- (C) 900
- (D) 800
- (A) Entrainment
- (B) Foaming
- (C) Weeping & dumping
- (D) All
- (A) Decreases
- (B) Increases
- (C) Remains unchanged
- (D) None of these
- (A) 25
- (B) > 25
- (C) < 25
- (D) – 25
- (A) Molal
- (B) Relative
- (C) Percentage
- (D) None of these
- (A) Providing irregular grain size
- (B) Providing minimum percentage of voids
- (C) Having maximum possible points of contact
- (D) None of these
- (A) Centrifugal extractor
- (B) Pachuca tanks
- (C) Bollman extractor
- (D) None of these
- (A) Binary mixture is represented by the apex
- (B) Binary mixture is represented by any point inside
- (C) Ternary mixture is represented by the sides
- (D) Pure component is represented by the apex

