A. Increases
C. Decreases exponentially
D. Remains unchanged
A. Increases with increase in
B. Is one at unity value of
D. Neither A. nor B.
B. Cake resistance decreases
C. Filter medium resistance decreases
D. Filter medium resistance increases
B. Ball mill
C. Toothed roll crusher
D. Tube mill
A. Pr = Sc; percentage change in heat and mass transfer flux will be the same for a given change
B. the degree of turbulence
C. Pr = Sc = 1; total mass, momentum and thermal diffusivity will be the same
E. Pr = Sc; there wont be any change in heat and mass transfer flux with changes in degree of
F. bulence
A. Gravity settler
B. Coagulant
D. Clarifier
A. tons/hr
B. tons/ft2
C. Both A. & B.
B. Disk-bowl
A. 1.5
B. ?3
C. 2
A. Exponentially increases
B. Does not affect
C. Increases
A. Produces finer products
B. Uses smaller balls
C. Is long in comparison with its diameter
A. None of these
C. Induced
D. Forced
A. P/m = K/ ?Dp
B. P/m = K . ln D? sa/D? sb
D. None of these
A. N1
C. N
D. N3
B. Humid heat
C. Sensible heat
D. Latent heat
A. G/L
B. Always < 1
C. None of these
B. Sedimentation
C. Flocculation
D. Dispersion
B. None of these
C. Levas equation
D. Blake-Plummer equation
A. Tabling
C. Jigging
D. Classification
B. Continuously increases
C. Remain constant throughout
D. May increase or decrease; depends on the pressure
A. 1/?
B. ??
D. 1/?2
A. Disc-bowl
B. Suspended batch basket
D. Tubular bowl
A. Viscosity with concentration
B. Degree of ideality of the solution
B. At a speed more than the critical speed
C. With minimum possible small balls
D. At a speed equal to the critical speed
A. Removal of fines from liquid
B. Liquids of very high viscosity
C. Liquids having high vapour pressure
A. Volume
C. Weight
A. Sorting
B. Elutriation
D. Flocculation
B. The ratio of number of actual plates to ideal plates
C. Same as the Murphree efficiency
D. Always more than the point efficiency
A. Apron conveyor
B. Bucket elevator
C. Belt conveyor
A. Hot cupric oxide
B. Alumina
C. Cold Ca(OH)2
B. Decreases
C. Remains constant
D. Increases linearly
D. Screw conveyor
B. N ? D
C. N ? ?D
D. N ? 1/D
A. Plate & frame
C. Rotary
D. Vacuum
A. Screening becomes progressively easier
D. Capacity and effectiveness of the screen is increased
A. Ultrafine
B. Fine
C. Secondary
B. Coarse grinding
C. Attrition
D. Crushing
A. 3.34 Wi
C. Wi
D. 0.5 Wi
A. Filtration time only
C. Square of the viscosity
D. Washing time only
A. Always greater than
C. Not related to
A. Tearing (shear) and compression
B. Impact and attrition
A. 4 to 5
B. 0.01 to 0.1
C. 2 to 3.5
A. ?(LS)
B. LS
C. 250 LS
A. Lime
C. Sodium silicate
D. Alumina
A. Sand
D. Press
A. Runs at very slow speed (2 rpm)
B. All A., B. and C.
C. Is used for mixing high viscosity pastes
A. Enhancing the cake porosity in case of a dense impermeable cake
B. Accelerating the rate of filtration
D. Reducing the filtration pressure
A. P. gc. ?/?2
B. P. gc/n2. D2. ?
D. n3. D3. ?/P. gc
A. Fluid energy mill
B. Hammer crusher
D. Impact mill
A. Parallel
B. Straight
D. Neither parallel nor straight
Showing 2301 to 2350 of 8709 mcqs