A. Sand
B. Wheat
D. None of these
A. None of these
B. Wettability
C. Particle shape
A. Specific humidity
B. Partial pressure of vapour
D. Neither A. nor B.
A. 1.5-2.5
B. 0.5-2
D. 1.33-1.45
A. Dewaxing of lubricating oil
C. Separation of cream from milk
D. Concentration of rubber latex
C. Bonds crushing law
D. Kicks law
A. Different fluids
B. Same fluid
C. Same field of force
A. Provides more effective washing
B. Facilitates filtration under higher pressure
D. Entails less labor cost
A. Raschig rings
C. Cylinder (L/D = 1)
D. Cube
A. Coagulation
B. Clarification
D. Flocculation
A. Rate of filtration increases with time
C. Rate of filtration is constant
D. Resistance decreases with time
A. Filters
B. Thickness
D. Cyclones
A. Propeller agitator
C. Sharpies centrifuge
A. Product size
B. Feed size
D. Diameter of the rolls
A. Dp/Df
C. None of these
D. Df Dp
A. Temperature
B. Pressure
C. Nature of the components
A. > 100
B. < 100
D. > 10
A. 1
B. > 1
C. 1.5
B. Shaking screen
C. Trommel
D. Grizzly
A. 5
B. 10
D. 0.5
A. Nc = (1/4?). ?(g/R1 R2)
B. Nc = (1/2?). ?(R1 R2/g)
D. Nc = (1/?). ?(g/R1 R2)
B. 75-80
C. 40-50
D. 90-95
A. Single spiral
B. Cross-partition
C. Lessing
A. Grinder
C. Cutter
D. Crusher
A. 0.0074 mm
B. 0.0047 cm
D. 74 milli-microns
A. Collector
B. Modifier
D. Activator
A. Cresylic acid
C. Sodium carbonate
D. Calcium carbonate
A. Primary
B. Ultrafine
D. Secondary
A. Size of the grinding media
B. Operating speed
D. Final product size
A. Attrition
B. Cutting
C. Compression
A. Jaw crusher
C. Cone crusher
D. Gyratory crusher
C. Overall
D. Over medium
A. kg/sec
B. kWh/sec. kg
C. kWh/kg
A. Calcite
C. Gypsum
D. Quartz
A. Compressible cake and turbulent
B. Compressible cakes and laminar
D. Incompressible cake and turbulent
A. Muller
C. Tumbler
D. Ribbon blender
A. Should be of high volatility
B. All A., B. and C.
D. Should form azeotropes with the original components
A. Operating speed should be more than the critical speed
B. Fine feed requires a larger ball
B. 1
C. 0
D. 0.2
B. Employs smaller balls
C. Has larger length/diameter ratio (>2 as compared to 1 for ball mill)
D. Gives finer size reduction but consumes more power
A. Pitman
C. Check plates
D. Toggles
A. Clarification
B. Thickening
C. Froth floatation
B. High power consumption in grinding
C. Poor grindability
B. 1000C and 500 atm
C. 200C and 5 atm
D. 500C and 50 atm
A. Crushing
C. Cutting
D. Grinding
A. Curved
C. Either A. or B.
D. Plane
A. Pre-coated on the filter medium prior to filtration
C. Separated from the cake by dissolving solids or by burning it off
D. Added to the feed slurry
A. 70
B. 35
D. 85
A. Stamp mill
B. Bradfords breaker
D. Blake jaw crusher
B. 1/R
C. 1/?
D. S
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