- (A) Impeller diameter or speed
- (B) Number of pumps and joining them in series
- (C) Number of pumps and joining them in parallel
- (D) All
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- (A) Dilatent fluid
- (B) Pseudo plastic fluid
- (C) Ideal plastic
- (D) None of these
- (A) Drag on particles
- (B) Drag on column walls
- (C) Bed height
- (D) Bed voidage
- (A) M2/sec
- (B) N/m2. sec
- (C) Kg. sec/m
- (D) None of these
- (A) 39.6y
- (B) 48y
- (C) 49.2y
- (D) 58y
- (A) 0.5
- (B) 2
- (C) 4
- (D) 1
- (A) Drag stress to inertial stress
- (B) Inertial stress to drag stress
- (C) Inertial stress to gravitational stress
- (D) Gravitational stress to drag stress
- (A) 10
- (B) 100
- (C) 1000
- (D) 10000
- (A) < 0.3
- (B) > 3
- (C) 50
- (D) 1
- (A) High capacity at high heads
- (B) High capacity at low heads
- (C) Low capacity at high heads
- (D) Low capacity at low heads

