A. Classification
B. Clarification
D. Decantation
A. Compression and tearing
B. Compression
D. Cutting action
A. Powdered food & granular materials
C. Dry chemicals
D. Light metal powder down upto 4 mesh size
A. cm/gm-1
C. gm-1
D. gm/cm-1
A. 5-Jan
B. 200-300
C. > 500
A. Sand bed filter
B. Plate and frame filter press
D. Batch basket centrifuge
A. Unpredictable
B. Same
C. More
A. Complicates handling of the product
B. Gives less wear on chamber walls
D. Requires more energy
A. T3
B. ?T
D. T1.5
A. 10 to 25
B. < 5
D. > 1000
A. ? 1/ ?P
B. ? ??P
D. ? ?P
A. Volatile matter content
B. Differential wettability
D. Size
A. Banbury mixer
B. Muller-mixer
D. None of these
A. a1 = 0.5 a2
B. a1 = a2
C. a1 = 2a2
A. Compression
B. None of these
D. Cutting
A. Feed rate
C. Clearance between hammer & grinding plates
D. Rotor speed
A. 1
B. ?
D. > 1
B. Blake jaw crusher
C. Gyratory crusher
D. Dodge jaw crusher
A. Intermediate
C. Wet
D. Ultrafine
B. Rod mills
C. Gyratory crushers
D. Crushing rolls
C. Fact that screening is more effective
D. Assumption that all particles in a single fraction are equal in size
A. Its speed
B. Its ball load
D. The density of the material being ground
A. Hydrocyclones
B. Dorr Oliver rake classifier
C. Sharpies super-centrifuge
A. Bucket elevator
B. Screw conveyor
C. None of these
A. Extraction
C. Absorption
D. Leaching
A. 2
B. 2.5
D. 1
B. Viscosity of the liquid
C. Square of rotational speed
D. Cube of impeller diameters
A. d
B. 1/d
D. ?d
B. Flocculation
A. Sherwood
C. Peclet
D. Stanton
A. Tube mill
B. Pebble mill
D. Compartment mill
B. Vapour is in equilibrium with the liquid at the room temperature
D. Partial pressure of vapour equals the vapour pressure of the liquid at room temperature
B. Ultrafine
C. Primary
A. Fluid energy mill
B. Rod mill
C. Ball mill
A. Under-sizes are retained in oversize fraction
B. Screen capacity is abruptly increased
D. Over-sizes are present in undersize fraction
B. Cake
C. ium
D. Filter medium
E. Channel carrying the slurry to the upstream side of the cake and filtrate away from the filter
B. Impact
C. Cutting
D. Compression
A. Asbestos
C. Purified wood cellulose
D. Diatomaceous earth
B. 0.5 D
C. 1.5 D
D. 2 D
A. Hexane
B. Lime water
C. Dilute H2SO4
A. Crushing
B. Cutting
D. Grinding
A. 85
B. 3
D. 25
A. No reflux
B. Minimum reflux ratio
C. Zero reflux ratio
A. Batch basket centrifuge
B. Tank filter (Nutsche filter)
D. Filter press
B. 5 mm screen and retained on 10 mm screen
C. Both 5 mm and 10 mm screens
D. Neither 5 mm nor 10 mm screen
A. Froude number is independent for the curves between power number and Reynolds number in
B. fled system
D. Power number becomes independent of impellers Reynolds number at high Reynolds number,
E. er number
F. Froude number is used to account for the effect of surface (e.g., the centre vortex) on the
A. Po ? Re0.5
B. Po ? Re1.0
D. Po ? Re-1.0
A. Roll
B. Vibratory
A. Size of feed (at constant reduction ratio)
B. Size of the product (at constant feed size)
D. Capacity of the crushing machine
A. Pulverisation
B. Comminution
D. Dispersion
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