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This set of Mass Transfer Multiple Choice Questions & Answers (MCQs) focuses on Mass Transfer Set 23
Q1 | Gaseous diffusion co-efficient increases with increase in the
- Pressure
- Temperature
- Both (A) & (B)
- Neither (A) nor (B)
Q2 | Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted)represent
- A pure component
- A binary mixture
- A ternary mixture
- Partially miscible ternary system
Q3 | The rate of mass transfer is not dependent upon the
- Degree of dispersion of one fluid in the other
- Interfacial surface exposed between the phases
- Both (A) & (B)
- None of these
Q4 | Air at a particular humidity is heated in a furnace. The new dew point
- Decreases
- Increases
- Depends on the extent of heating
- Remain unchanged
Q5 | The rate of solid-liquid extraction is limited by the
- Phase change of the solute as it dissolves in the solvent
- Diffusion of the solute through the solvent in the pores to the outside of the particle
- Diffusion of the solute from the solution in contact with the particle to the main bulk of the solution
- All 'a', 'b' & 'c'
Q6 | In case of gases, the binary diffusivity is proportional to (where, P = pressure).
- P
- 1/P
- 1/?P
- ?P
Q7 | One mole feed of a binary mixture of a given composition is flash vaporised at a fixed P and T. If Raoult's law is obeyed, then changing the feed composition would effect
- The product composition but not the fraction vaporised
- The product composition as well as the fraction vaporised
- The fraction vaporised but not the product composition
- Neither the product composition nor the fraction vaporised
Q8 | What is the reflux ratio at total reflux?
- Zero
- Infinity
- Unity
- Data insufficient
Q9 | The operating line for an absorber is curved, when plotted in terms of
- Mole fractions
- Mole ratios
- Partial pressure
- Mass fractions
Q10 | Which of the following is the most suitable for extraction in a system having very lowdensity difference?
- Mixer-settler extractor
- Centrifugal extractor
- Pulsed extractor
- Packed extraction tower
Q11 | (NSh/NRe.NSc) is termed in mass transfer operation as the
- Stanton number
- Peclet number
- Thermal diffusivity
- Momentum diffusivity
Q12 | In the desorption of highly soluble gas from the liquid, the main resistance will be in the __________ phase.
- Gas
- Liquid
- Both (A) & (B)
- Neither (A) nor (B)
Q13 | Positive deviation from Raoult's law means a mixture whose total pressure is
- Greater than that computed for ideality
- Less than that computed for ideality
- Less than the sum of the vapour pressure of the components
- None of these
Q14 | Flooding results in
- High tray efficiency
- Low tray efficiency
- High gas velocity
- Good contact between the fluids
Q15 | At minimum reflux ratio for a given separation
- Number of plates is zero
- Number of plates is infinity
- Minimum number of the theoretical plates is required
- Separation is most efficient
Q16 | An ideal tower packing should not
- Have low weight per unit volume
- Have large surface area per unit volume
- Have large free cross-section
- Hold up large amount of liquid in the packing
Q17 | Diffusion in concentrated solutions differs from that in dilute solutions, because of the change in the __________ with the concentration of the solution.
- Degree of ideality
- Viscosity
- Both 'a '& 'b'
- Neither 'a' nor 'b'
Q18 | Make up water is supplied during cooling tower operation to compensate for water losses due to
- Evaporation
- Blowdown
- Entrainment
- All (A), (B) & (C)
Q19 | The dimension of diffusivity is same as that of the
- Density
- Molal concentration
- Kinematic viscosity
- Velocity head
Q20 | As the reflux ratio in a distillation column is increased from the minimum, the
- Slope of the operating line in stripping section decreases
- Number of plates decreases very slowly first and then more and more rapidly
- Total cost first decreases and then increases
- Liquid flow increases while the vapor flow decreases for a system
Q21 | Fenske-Underwood equation used for calculating the minimum number of theoreticalplates in distillation column is valid for
- Constant molal overflow
- Total reflux
- Constant relative volatility
- All (A), (B) and (C)
Q22 | Solvent used in extractive distillation
- Is of low volatility
- Forms a low boiling azeotrope
- Forms a high boiling azeotrope
- Does not alter the relative volatility of the original components
Q23 | When the feed to a distillation column is a saturated liquid, slope of the feed line is
- Zero
- Unity
- Infinity
- None of these
Q24 | The absorption factor is defined as (where, L = liquid flow rate, G = gas flow rate and, m = slope of the equilibrium line).
- L/mG
- G/mL
- mL/G
- LG/m
Q25 | Chemisorption (chemical adsorption) is
- Same as "Van der Waals" adsorption
- Characterised by adsorption of heat
- An irreversible phenomenon
- A reversible phenomenon