Free Mass Transfer Operations MCQs with Answers

669 Mass Transfer Operations MCQs from Chemical Engineering, each with the correct answer and a written explanation of why it is correct. Free and unlimited, with no account needed.

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669 questions · page 22 of 34

  • A. Concentrated solution and non-isothermal operation
  • B. Dilute solution and non-isothermal operation
  • C. Dilute solution and isothermal operation
  • D. Concentrated solution and isothermal operation

Explanation: For dilute mixtures under isothermal conditions, the equilibrium relation is approximately linear and the operating-line material balance…

Correct answer: Dilute solution and isothermal operation
  • A. Drying cost per unit weight of dried product is less
  • B. Product with more uniform moisture content is produced
  • C. Equipment size required is smaller
  • D. All A , B. & C.

Explanation: Continuous dryers generally reduce drying cost through steadier operation, provide more uniform product moisture, and require less…

Correct answer: All A , B. & C.
  • A. Nature of the vapor
  • B. None of these
  • C. Composition of the mixture
  • D. Temperature of the mixture

Explanation: Relative saturation is the ratio of actual vapour partial pressure to saturation vapour pressure at the same temperature.

Correct answer: None of these
  • A. T2
  • B. √T
  • C. T
  • D. 1/T

Explanation: For liquids, the simplified temperature dependence of diffusivity is D proportional to T, although the complete relation also includes the…

Correct answer: T
  • A. Fixed bed absorption
  • B. Moving bed absorption
  • C. Fixed bed adsorption
  • D. Moving bed adsorption

Explanation: Hypersorption is an adsorption process carried out with a moving bed of adsorbent, allowing near-continuous solids circulation and…

Correct answer: Moving bed adsorption
  • A. Unbound
  • B. Bound
  • C. Critical
  • D. Free

Explanation: Equilibrium moisture is the amount retained when the solid is in equilibrium with the surrounding gas; moisture above this value can be…

Correct answer: Free
  • A. Extractive
  • B. Azeotropic
  • C. Molecular
  • D. Flash

Explanation: Extractive distillation adds a relatively nonvolatile solvent that changes component relative volatilities without necessarily forming a…

Correct answer: Extractive
  • A. 0.31
  • B. 0.107
  • C. 0.017
  • D. 0.215

Explanation: Humid heat is the heat capacity of dry gas plus the vapour contribution: c_H = c_g + Hc_v = 0.2 + (0.01)(1.5) = 0.215 kJ/(kg dry gas·K).

Correct answer: 0.215
  • A. 100
  • B. None of these
  • C. < 100
  • D. > 100

Explanation: With a long liquid flow path, the liquid composition changes substantially across the tray, so the reference equilibrium vapour…

Correct answer: > 100
  • A. Uses molal units for material and energy balance
  • B. Uses weight fractions to express liquid and vapour composition
  • C. Can use any type of units
  • D. Is more accurate than Ponchon-Savarit method

Explanation: The McCabe-Thiele construction is based on mole balances and the constant-molal-overflow assumption, so liquid and vapour compositions are…

Correct answer: Uses molal units for material and energy balance
  • A. 1
  • B. 0.24
  • C. 3.97
  • D. 600

Explanation: For air-water vapour, thermal and mass diffusivities are of similar magnitude, so Sc and Pr are both close to unity.

Correct answer: 1
  • A. And humidified
  • B. And dehumidified with increase in wet bulb temperature
  • C. And dehumidified with decrease in wet bulb temperature
  • D. At the same relative humidity

Explanation: Because the entering dew point is 18°C and the spray water is at 15°C, the air is cooled below its dew point and water condenses from it.

Correct answer: And dehumidified with decrease in wet bulb temperature
  • A. Azeotropic mixture is
  • B. More
  • C. Same
  • D. Less
  • E. Either more or less; depends on the system

Explanation: At an azeotrope, the equilibrium liquid and vapour compositions are identical, so the mixture distils without composition change.

Correct answer: Same
  • A. None of these
  • B. Moles transferred/ [(time) (area) (mass A/mass B)]
  • C. Moles transferred/ [(time) (area) (pressure)]
  • D. Moles transferred/ [(time) (area) (mole fraction)]

Explanation: A mass-transfer coefficient has units of molar flux divided by a concentration, mole-fraction, mass-ratio, or pressure driving force.

Correct answer: None of these
  • A. 1
  • B. ∞
  • C. 0.5
  • D. 2

Explanation: In equimolal counterdiffusion, the molar fluxes satisfy N_A = -N_B, so the total molar flux N_A + N_B is zero.

Correct answer: ∞
  • A. High pressure
  • B. Low pressure
  • C. Extractive
  • D. Steam

Explanation: Rose oil is volatile and heat-sensitive, so it is recovered by steam distillation at a temperature lower than its normal boiling point.

Correct answer: Steam
  • A. Decreases tray efficiency
  • B. Increases tray efficiency
  • C. Reduces pressure drop
  • D. Is desirable, as it provides improved vapour-liquid contact

Explanation: Back-trapping causes liquid or vapour to move undesirably back to a preceding tray, increasing mixing and reducing the effective driving…

Correct answer: Decreases tray efficiency
  • A. Cracks develop on the surface of the solid
  • B. Surface evaporation of unbound moisture occurs
  • C. Rate of drying decreases abruptly
  • D. None of these

Explanation: During the constant-rate period, the exposed surface remains saturated with unbound moisture, so evaporation occurs at an essentially…

Correct answer: Surface evaporation of unbound moisture occurs
  • A. 0 to 0.5
  • B. 0 to 3
  • C. 1.25 to 2
  • D. 5 to 15

Explanation: An absorption factor of about 1.25 to 2 gives a practical balance between solvent circulation and absorber size.

Correct answer: 1.25 to 2
  • A. Isothermal operation
  • B. Dilute solutions
  • C. None of these
  • D. Dilute solutions and isothermal operation

Explanation: For dilute solutions at constant temperature, the equilibrium relation is approximately linear, such as y* = mx, and constant physical…

Correct answer: Dilute solutions and isothermal operation