A. Decreasing machine capacity

B. None of these

D. Decreasing size of product at constant size of feed

B. Flocculation

C. Sedimentation

D. Clarification

B. Grizzlies

C. Shaking screen

D. Trommels

A. Intermediate

B. Fine

C. Coarse

A. Pressure and temperature only

B. Temperature and composition only

C. Pressure and composition only

A. Bag filter

B. Gravity settler

C. Tubular centrifuge

A. Chromite

B. Rutile

D. Siderite

A. Rotary drum vacuum filter

B. Plate and frame filter press

D. Cartridge filter

B. Fluid energy mill

C. Ball mill

D. Rod mill

A. 0.1

B. 0.4

C. None of these

A. Ball mill

C. Tube mill

D. Jet pulveriser

A. Classifier

B. Cyclone separator between mill & classifier

D. Neither A. nor B.

B. More

C. Less

D. Either A. or B., depends on other factors

A. Venturi atomiser

B. Gravity settling chamber

D. Cyclone separator

A. Gas film

B. None of these

D. Chemical reaction

A. None of these

B. Densities

C. Particle sizes

B. [(DP2/18). (?s ?/?)] ?2r

C. [(DP/18). (?s ?/?)] ?2r2

D. [(DP/18). (?s ?/?)] ?2r

A. Drag conveyor

B. Ribbon conveyor

D. Flight conveyor

A. Recovery

B. Recovery/rejection

D. Rejection

A. Solids from solids

B. Solids

D. Liquids

B. Belt

C. Drag

D. Screw

B. Wheat

C. Talc

D. Iron core

A. Apron conveyor

B. Pneumatic conveyor

C. Bucket elevator

A. Clarifier

B. Sparkler filter

D. Vacuum leaf filter

A. Decreases

B. Is same as for coarser grinding

C. Is 1.5 times that for coarser grinding

A. Time for half change is independent of the initial concentration

B. Reaction rate is trebled when the initial concentration is trebled

C. Time for completion of the reaction is independent of the initial concentration

A. None of these

C. Coke breeze

D. Sand

A. Clarification

B. Sedimentation

D. Elutriation

A. 0.5

B. ?3

D. ?2

B. Ball mill

C. Tube mill

D. Jaw crusher

A. Cake becomes very dense

B. Liquor stops flowing out to the discharge

C. Filtration pressure rises suddenly

A. Attrition

B. Cutting

C. Impact

A. Viscosity

B. Thermal conductivity

D. Surface tension

A. Reduction ratio can be varied by adjusting the distance from cage to hammers

C. Maximum acceptable feed size is 30 cms

D. Crushing takes place by impact breaking

A. 16

C. 64

D. 52

B. Ratio of volume to surface as the particle

C. None of these

D. Volume as the particle

A. Silica gel

B. Calcium silicate

C. Sodium carbonate

A. Jaw crusher

B. Rod mill

C. Ball mill

A. Sulphur dioxide oxidation

B. Benzene oxidation

D. Ammonia synthesis

B. 5 to 10

C. 20 to 25

D. 50 to 70

A. Quartz

B. Fluorspar

C. Calcite

A. Grinding element & the housing

B. Feed particles

D. Neither A. nor B.

A. Separated by particle density

C. Separated by particle shape

D. Mixed

B. Roll crusher

C. Hammer crusher

D. Gyratory crusher

A. Less than

B. Data insufficient; cant be predicted

D. More than

A. Cant be used for separation of fine suspended solids from a liquid

C. Employ bowl of larger diameter

D. Cant be operated under pressure/vacuum

A. Nylon

B. Glass cloth

D. Metal cloth of monel or stainless steel

A. Catalyst

B. Filter medium

D. Explosive

A. Bulk density of materials

C. Pressure of the conveying air

D. Diameter of the conveying line

A. 1/D2.5

C. D

D. 1/D