A. 51 min
B. 15 min
C. 94 min
A. 1.5
B. 0.6
C. -0.6
A. Same as simple distillation
C. Most useful for handling binary systems
D. Same as differential distillation
B. Liquid phase obeys Daltons law and vapor phase obeys Raoults law
C. Only vapor phase follows Raoults law
D. Only liquid phase obeys Daltons law
A. Extractive
B. Molecular
D. Steam
A. Liquid stream should be distributed uniformly
B. Gas stream should be distributed uniformly
D. By passing should be completely avoided
E. wer: Option C
A. Better flow characteristics
B. Rapid absorption rates
D. Low pumping pressure drop
B. Concentrated solutions
C. Gaseous solutions at high pressure
D. None of these
A. Molecular
C. Flash
D. Equilibrium
A. K ?D2
C. K ?D
D. K ?D1.5
B. Use high pressure distillation
C. Use molecular distillation
D. Use steam distillation
A. Dew point < wet bulb temperature
B. Wet bulb temperature < dry bulb temperature
D. Neither A. not B.
A. Relative humidity decreases
B. Relative humidity increases
C. Wet bulb temperature decreases
A. Humidification only
B. Heating only
D. Evaporative cooling
A. Wet bulb temperature
B. Partial pressure of vapour
D. Relative humidity
B. Equal to the heat of formation of surface compound
C. Called integral heat of adsorption
D. Zero
B. KG = 1/KG + m/KL
C. KG = 1/KL + m/KG
D. 1/KG = 1/KL + m/KG
A. Plate efficiency to be achieved
B. Reflux ratio
D. Relative volatility
A. Equal to
B. Either A., or B.; depends on the type of packing
C. Greater than
A. Low pressure drop and high hold up
B. High pressure drop and high hold up
D. High pressure drop and low hold up
A. Use molecular distillation
B. Use steam distillation
C. Use high pressure distillation
B. None of these
C. Concentrated solutions
D. Gaseous solutions at high pressure
A. ?
C. 0
D. #NAME?
C. Penetration
D. Surface renewal
A. Reducing the total pressure
B. Increasing the total pressure
C. Reducing the temperature
B. Composition of the residue remains unchanged
C. More number of trays are required and the residue composition is more dilute in methanol
D. More number of trays are required but the residue composition remains unchanged
A. 100
D. < 100
A. Perforated tray tower
B. Wetted wall tower
C. Grid tray tower
A. 0.048
B. 0.079
C. 0.122
A. Vapour laden gas at 1 atm. and room temperature
C. Gas plus its accompanying vapour at 1 atm. and room temperature
D. Vapour laden gas at 1 atm. and gas temperature
B. < 1
C. 1
D. 0.5
A. Steam
B. Extractive
C. Molecular
A. Increase in rate of drying
C. Decreasing temperatures
A. D2
C. D0.5
D. 1/D
A. Room
C. Wet bulb
A. Re0.53
C. Re
D. Re0.33
A. Equipment size required is smaller
B. Drying cost per unit weight of dried product is less
D. Product with more uniform moisture content is produced
B. Fick
C. Toor and Marcello
D. Stefan
B. Decreases
C. Remain unaffected
D. Passes through a maximum
A. Absorption
B. Extractive distillation
B. Solvent extraction
C. Reverse osmosis
D. Leaching
A. The overall M.T.C. of the system
B. M.T.C. of individual components in a liquid-liquid system
D. M.T.C. of liquid in liquid-gas system
A. Less than
B. Equal to
A. 1
D. 2
B. Increase in Murphree plate efficiency
C. Decrease in liquid hold up in the column
D. Decrease in pressure drop
B. Dependent on the water lost by evaporation
C. Desirable
D. All A., B. & C.
B. Gas-solid
C. Solid-solid
D. Liquid-solid
A. Increases pressure drop, decreases surface area
B. Decreases pressure drop, decreases surface area
D. Increases pressure drop, increases surface area
A. Drift
B. Evaporation
C. Blowdown and leakage
B. Between 100 and 210
C. None of these
D. At > 210.6
Showing 251 to 300 of 697 mcqs