B. Either A. or B.; depends on the gas
C. Decreases
D. Remain same
A. Momentum flux
B. Kinematic viscosity
C. Thermal diffusivity
A. Rotary vacuum
B. Freeze
C. Tray
A. Caustic solution
C. Dilute HCl
D. Ethanolamine
A. Liquid side
C. Interfacial
D. Both liquid and gas side
B. Partial pressure
C. Mole fraction
D. None of these
A. Galileo number
C. Dean number
D. Weber number
A. Absorption of NH3 from air by water
B. All liquid-solid diffusion systems
D. All liquid-liquid diffusion systems
A. Humidity
C. Velocity
D. Temperature
A. Lowering the barometric pressure
B. Reducing the humidity of entering air
D. Increasing the air velocity over the wet surfaces
B. None of these
C. Increases
D. Remains unchanged
A. Cost
C. Durability
D. Size
A. Remains unchanged
C. Decreases exponentially
D. Decreases
A. Height < 6
B. Diameter < 0.6
D. Neither A. nor B.
A. Rotary dryer
B. Drum dryer
C. Dielectric dryer
A. Sieve plate
B. Bollman
C. Mixer-settler
A. 12
B. 18
C. 8
A. Gas phase
B. All A , B. & C.
C. Liquid phase
A. Hydrochloric acid
B. Nitric acid
C. Sulphuric acid
A. Rotary
C. Fluidised bed
D. Spray
A. Either A. or B.; depends on the packing height
B. Less
C. Equal
A. 1
B. 0
B. Sh Pr
C. Pr St
D. St Sh
A. Reboiler itself contains one plate
C. Vapour is recycled to the column
B. 25
C. 25
D. < 25
B. Thermal conductivity of solute increases
C. Viscosity of solvent decreases
B. Enthalpy concentration method
C. Ponchon-Savarit method
D. McCabe-Thiele method
A. Polymerisation industry
B. Ammonia synthesis plant
C. Soap manufacturing
A. 2 metres above the ground
C. 5 metres above ground
D. 10 metres above ground
A. Dialysis
C. Diffusion
D. Electrodialysis
B. Particle size
C. Temperature
D. Agitation
A. Schmidt number
B. Lewis relationship
C. Sherwood number
A. Providing minimum percentage of voids
B. Having maximum possible points of contact
D. Providing irregular grain size
A. Diffusion co-efficient
C. NTU
A. 5
B. 100
C. 1
A. Continuous
B. Azeotropic
C. None of these
A. D ? 1/P1.5
C. D ? P0.5
D. D ? 1/P0.5
A. Dew point
C. Dry-bulb
D. Adiabatic saturation
D. Bollman
A. Fluidised bed
D. Vacuum rotary
A. Increasing the vapour flow rate
B. Increasing the liquid flow rate
C. Using higher reflux ratio
A. Blow down
B. Vapor load
A. Dissolution
C. Agitation and settling
D. Decoction
C. Flux = Co-efficient/concentration difference
D. Flux=concentration difference/coefficient
A. 6.89
C. 8.25
D. 10
A. Percentage
C. Relative
A. Minimise the overall pressure drop
C. Avoid flooding
D. Reduce liquid hold up
A. 2
B. ?
D. 0.5
B. Evaporation
C. Continuous distillation
D. Absorption
B. Percentage
D. Relative
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