Mass Transfer Flashcards

1
Q

Mass transfer rate between two fluid phases does not necessarily depend on the __________ of the two phases. A. chemical properties B. physical properties C. degree of turbulence D. interfacial area

A

A. chemical properties

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2
Q

In a solution containing 0.30 Kg mole of solute and 600 kg of solvent, the molality is A. 0.5 B. 0.6 C. 2 D. 1

A

A. 0.5

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3
Q

Fenske equation determines the A. maximum number of ideal plates. B. height of the distillation column. C. minimum number of theoretical plates. D. optimum reflux ratio.

A

C. minimum number of theoretical plates.

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4
Q

The term “cooling range” in a cooling tower refers to the difference in the temperature of A. cold water leaving the tower and the wet bulb temperature of the surrounding air. B. hot water entering the tower and the wet bulb temperature of the surrounding air. C. hot water entering the tower and the cooled water leaving the tower. D. none of these

A

C. hot water entering the tower and the cooled water leaving the tower.

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5
Q

Which of the following is the most suitable for extraction in a system having very low density difference? A. Mixer-settler extractor B. Centrifugal extractor C. Pulsed extractor D. Packed extraction tower

A

B. Centrifugal extractor

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6
Q

Total reflux in a distillation operation requires minimum A. reboiler load B. number of plates C. condenser load D. all (a), (b) and (c)

A

B. number of plates

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7
Q

The amount of steam required per unit quantity of distillate in case of steam distillation will be reduced by A. raising the temperature. B. lowering the total pressure. C. both (a) and (b). D. neither (a) nor (b).

A

C. both (a) and (b).

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8
Q

The difference of wet bulb temperature and adiabatic saturation temperature of unsaturated mixture of any system is A. (+)ve B. (-)ve C. zero D. none of these

A

A. (+)ve

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9
Q

Fenske’s equation for determining the minimum number of theoretical stages in distillation column holds good, when the A. relative volatility is reasonably constant. B. mixture (to be separated) shows negative deviation from ideality. C. mixture (to be separated) shows positive deviation from ideality. D. multicomponent distillation is involved.

A

A. relative volatility is reasonably constant.

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10
Q

When the temperature and humidity of air is low, we usually use __________ draft cooling tower. A. natural B. forced C. induced D. none of these

A

A. natural

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11
Q

Pick out the correct statement. A. In case of liquid-liquid extraction, no separation is possible, if the selectivity of the solvent used is unity. B. With increase in temperature, the selectivity of the solvent used in solvent extraction decreases. C. The selectivity of solvent used in solvent extraction is unity at the plait point. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

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12
Q

__________ columns are used for liquid dispersion in a continuous gas phase. A. Packed B. Pulse C. Bubble cap D. Sieve plate

A

A. Packed

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13
Q

Overall efficiency of the distillation column is A. the ratio of number of ideal plates to actual plates. 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

A. the ratio of number of ideal plates to actual plates.

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14
Q

On addition of solute in the solvent, the __________ of the solution decreases. A. boiling point B. freezing point C. vapour pressure D. both (b) and (c)

A

D. both (b) and (c)

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15
Q

Which is the controlling factor for a drum drier? A. Diffusion B. Heat transfer C. Both (a) and (b) D. Neither (a) nor (b)

A

B. Heat transfer

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16
Q

Drying operation under vacuum is carried out to A. dry those materials which have very high unbound mositure content. B. reduce drying temperature. C. increasing drying temperature. D. dry materials having high bound moisture content.

A

B. reduce drying temperature.

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17
Q

Air initially at 101. 3 kPa and 40°C and with a relative humidity of 50%, is cooled at constant pressure to 30°C. The cooled air has a A. higher dew point. B. higher absolute (specific) humidity. C. higher relative humidity D. higher wet bulb temperature.

A

C. higher relative humidity

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18
Q

Separation of two or more components of a liquid solution can not be achieved by A. fractional crystallisation B. liquid extraction C. absorption D. evaporation

A

C. absorption

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19
Q

Stefan’s law describes the mass transfer by A. diffusion B. bulk flow C. both ‘a’ & ‘b’ D. neither ‘a’ nor ‘b’

A

C. both ‘a’ & ‘b’

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20
Q

At minimum reflux ratio for a given separation A. number of plates is zero. B. number of plates is infinity. C. minimum number of the theoretical plates is required. D. separation is most efficient.

A

B. number of plates is infinity.

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21
Q

Relative humidity is the ratio of the A. partial pressure of the vapour to the vapour pressure of the liquid at room temperature. B. partial pressure of the vapour to the vapour pressure of the liquid at gas temperature. C. actual humidity to saturation humidity. D. none of these

A

B. partial pressure of the vapour to the vapour pressure of the liquid at gas temperature.

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22
Q

In batch distillation with constant reflux, overhead product composition __________ with time. A. increases B. decreases C. does not vary D. may increase on decrease, depends on the system.

A

B. decreases

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23
Q

Psychrometry deals with the properties of gas-vapor mixture. Humidity can be determined by the measurement of the __________ of a fibre. A. electrical resistance B. thermal conductivity C. strength D. none of these

A

A. electrical resistance

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24
Q

Heat in BTU necessary to increase the temperature of 1 lb of gas and its accompanying vapour by 1°F is called the A. latent heat B. humid heat C. specific heat D. sensible heat

A

C. specific heat

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25
Q

To increase the absorption factor, (where, G = gas flow rate, S = solvent flow rate) A. increase both ‘G’ and ‘S’. B. decrease both ‘G’ and ‘S’. C. increase ‘S’ and decrease ‘G’. D. increase ‘G’ and decrease ‘S’

A

C. increase ‘S’ and decrease ‘G’.

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26
Q

The mass diffusivity, the thermal diffusivity and the eddy momentum diffusivity are same for, NPr = NSc = __________ A. 1 B. 0.5 C. 10 D. 0

A

A. 1

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27
Q

Dew point of a gas-vapour mixture A. increases with temperature rise. B. decreases with temperature rise. C. decreases with decrease in pressure. D. increases with increase in pressure.

A

C. decreases with decrease in pressure.

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28
Q

In a packed absorption tower, if the equilibrium and operating lines are both straight lines, then the ratio, HETP/HTUOG __________ the absorption factor. A. increases with increase in B. is one at unity value of C. both (a) and (b) D. neither (a) nor (b)

A

C. both (a) and (b)

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29
Q

Which of the following plays an important role in problems of simultaneous heat and mass transfer? A. Lewis number B. Schmidt number C. Prandtl number D. Sherwood number

A

A. Lewis number

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30
Q

In case of an absorber, the operating A. line always lies above the equilibrium curve. B. line always lies below the equilibrium curve. C. line can be either above or below the equilibrium curve. D. velocity is more than the loading velocity.

A

A. line always lies above the equilibrium curve.

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31
Q

As the reflux ratio in a distillation coloumn is increased from the minimum, the A. slope of the operating line in stripping section decreases. B. number of plates decreases very slowly first and then more and more rapidly. C. total cost first decreases and then increases. D. liquid flow increases while the vapor flow decreases for a system.

A

C. total cost first decreases and then increases.

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32
Q

Absorption factor is defined as (where, S1 = slope of the operating line S2 = slope of the equilibrium curve) A. S2/S1 B. S1/S2 C. S1 - S2 D. S1 x S2

A

B. S1/S2

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33
Q

A plait point is the point on the solubility curve, where the tie line reduces to a point. What is the number of plait point for a ternery system containing twopairs of partially miscible liquids? A. 0 B. 1 C. 2 D. 3

A

A. 0

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34
Q

Which of the following remains constant during sensible cooling process? A. Specific humidity B. Partial pressure of vapour C. Both (a) and (b) D. Neither (a) nor (b)

A

C. Both (a) and (b)

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35
Q

Physical absorption is A. an irreversible phenomenon. B. a reversible phenomenon. C. accompanied by evolution of heat. D. both (b) and (c)

A

D. both (b) and (c)

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36
Q

Make up water is required in a cooling tower to replace the water lost by A. evaporation B. drift C. blowdown and leakage D. all (a), (b) and (c)

A

D. all (a), (b) and (c)

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37
Q

Which of the following quantities need not be fixed before starting the design of a co-current absorber? A. Heat gain or loss B. Flow rate of entering liquid C. Flow rate of gas D. None of these

A

B. Flow rate of entering liquid

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38
Q

Mass transfer co-efficient of liquid is A. affected more by temperature than that for gases. B. affected much less by temperature than that for gases. C. not affected by the temperature. D. none of these.

A

A. affected more by temperature than that for gases.

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39
Q

Absorption accompanied with chemical reaction is exemplified by the absorption of A. ammonia in water. B. benzol present in coke oven gas by wash oil. C. SO2 in alkaline solution. D. all (a), (b) and (c).

A

C. SO2 in alkaline solution.

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40
Q

Which of the following unit operations makes use of Thiele-Geddes equation? A. Liquid-liquid extraction B. Solid-liquid extraction C. Multicomponent absorption with chemical reaction D. Multicomponent distillation.

A

D. Multicomponent distillation.

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41
Q

Which of the following liquid-vapor contacting devices provides maximum contact surface area for a particular duty? A. Sieve plate column B. Bubble cap column C. Randomly packed column D. Wetted wall column

A

D. Wetted wall column

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42
Q

The equipment frequently used for adiabatic humidification-cooling operation with recirculating liquid is A. natural draft cooling tower B. induced draft cooling tower C. spray chamber D. none of these

A

C. spray chamber

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43
Q

Chemisorption (chemical adsorption) is A. same as “Van der Waals” adsorption. B. characterised by adsorption of heat. C. an irreversible phenomenon. D. a reversible phenomenon.

A

C. an irreversible phenomenon.

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44
Q

The rate of solid-liquid extraction is limited by the A. phase change of the solute as it dissolves in the solvent. B. diffusion of the solute through the solvent in the pores to the outside of the particle. C. diffusion of the solute from the solution in contact with the particle to the main bulk of the solution. D. all ‘a’, ‘b’ & ‘c’.

A

D. all ‘a’, ‘b’ & ‘c’.

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45
Q

Raoult’s law applies to the A. all liquid solutions B. non-ideal solution only. C. non-volatile solute. D. solvents.

A

D. solvents.

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46
Q

In distillation columns, the number of bubble caps per tray primarily depends upon the A. allowable liquid velocity. B. allowable gas velocity. C. allowable gas and liquid velocities. D. feed composition.

A

C. allowable gas and liquid velocities.

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47
Q

In distillation, overhead product contains A. only one component B. two components C. any number of components D. only saturated liquid

A

C. any number of components

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48
Q

With increase in pressure, the relative volatility for a binary system A. increases. B. decreases. C. remains same. D. either (a) or (b), depends on the system.

A

B. decreases.

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49
Q

Low viscosity absorbent is preferred for reasons of A. rapid absorption rates and good heat transfer characteristics. B. improved flooding characteristics. C. low pressure drop on pumping. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

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50
Q

Mass transfer co-efficient (K) and diffusivity (D) are related according to film theory as A. K ∝ D B. K ∝ sqrt(D) C. K ∝ D^1.5 D. K ∝ D^2

A

A. K ∝ D

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51
Q

The McCabe Δ L law states that the A. molar heats of vaporisation of components are nearly equal. B. linear crystal growth rate depends on the degree of supersaturation. C. linear crystal growth rate does not depend on the crystal size. D. linear crystal growth rate depends on the crystal size.

A

C. linear crystal growth rate does not depend on the crystal size.

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52
Q

Bollman extractor A. is a static bed leaching equipment. B. is used for extraction of oil from oilseed. C. is a centrifugal extractor. D. employs only counter-current extraction.

A

B. is used for extraction of oil from oilseed.

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53
Q

The relation, Sc = Pr = 1, is valid, when the mechanism of __________ ansfer is same. A. heat and mass B. mass and momentum C. heat and momentum D. heat, momentum and mass

A

A. heat and mass

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54
Q

A coalescer in a mixer-settler liquid-liquid extraction coloumn A. comprises of thin bed of substances of extended surface having high porosity. B. helps in increasing the bubble size entering the settler. C. helps in increasing the settling rate of the bubbles. D. all ‘a’, ‘b’, & ‘c’.

A

D. all ‘a’, ‘b’, & ‘c’.

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55
Q

For the same feed, feed quality and separation (in a distillation column), with the increase of total pressure, the number of ideal plates will A. increase B. decrease C. remains same D. data insufficient, can’t be predicted

A

A. increase

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56
Q

Pick out the correct statement. A. Ponchan-Savarit method is more accurate than McCabe-Thiele method to determine the number of theoretical stages required for the separation of non-ideal binary system by distillation. B. A sharp decrease in pressure drop is an indication of flooding in a distillation coloumn. C. Solvent used in extractive distillation should be of high volatility. D. Flash distillation is suitable for separating components which have very close boiling temperature.

A

A. Ponchan-Savarit method is more accurate than McCabe-Thiele method to determine the number of theoretical stages required for the separation of non-ideal binary system by distillation.

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57
Q

When the liquid phase and vapour phase of a binary system obeys Raoult’s and Dalton’s law respectively, the relative volatility is the ratio of A. vapour pressure of component A to that of component B. B. vapour pressure of component A to the total pressure. C. vapour pressure of component A to the partial pressure of A. D. partial pressure of component A to the total pressure.

A

A. vapour pressure of component A to that of component B.

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58
Q

The operation involved when the soluble material is largely on the surface of an insoluble solid and is merely washed off by the solvent is called A. decoction B. percolation C. elutriation or elution D. none of these

A

C. elutriation or elution

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59
Q

In the constant rate period of the rate of drying curve for batch drying, A. cracks develop on the surface of the solid. B. rate of drying decreases abruptly. C. surface evaporation of unbound moisture occurs. D. none of these.

A

C. surface evaporation of unbound moisture occurs.

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60
Q

It takes 6 hours to dry a wet solid from 50% moisture content to the critical moisture content of 15%. How much longer it will take to dry the solid to 10% moisture content, under the same drying conditions? (The equilibrium moisture content of the solid is 5%). A. 15 min B. 51 min C. 71 min D. 94 min

A

C. 71 min

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61
Q

Agitator is provided in a crystalliser for A. avoiding deposition on cooler surfaces. B. formation of nuclei. C. crystal growth. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

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62
Q

__________ diffusion is used for separating the isotopes of methane. A. Thermal B. Pressure C. Concentration D. Force

A

A. Thermal

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63
Q

Ordinary diffusion process is also called __________ diffusion. A. pressure B. thermal C. concentration D. forced

A

C. concentration

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64
Q

Pick out the wrong statement. A. Different solids have different equilibrium moisture curves. B. Total condenser or reboiler is considered equivalent to one theoretical plate in McCabe-Thiele method of theoretical plate calculation for distillation column. C. Heat removal load on cooler remains constant, even with increase of the reflux ratio in a distillation column. D. Even a forced draft cooling tower can not cool water below the wet bulb temperature.

A

C. Heat removal load on cooler remains constant, even with increase of the reflux ratio in a distillation column.

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65
Q

Pick out the wrong statement pertaining to the rotary dryer. A. Flights (located in the inside shell of rotary dryer) lift the material being dried and shower it down through the current of hot air/gases. It extends from the wall to a distance which is about 8-12% of the inside diameter of shell. B. Hold up of a rotary drier is defined as the fraction of the dryer volume occupied by the solid at any instant. The best performance for rotary drier is obtained, when the hold up is in the range of 0.05 to 0.15. C. Rotary dryer is suitable for drying sticky material. D. Recommended peripherial speed of a rotary drier is in the range of 10 to 30 metres/minute.

A

C. Rotary dryer is suitable for drying sticky material.

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66
Q

The reason for preferring packed towers over plate towers in distillation practice is that the packed tower operation gives A. low pressure drop and high hold up. B. high pressure drop and low hold up. C. low pressure drop and low hold up. D. high pressure drop and high hold up.

A

C. low pressure drop and low hold up.

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67
Q

If the path of liquid across the plate is very long as in case of large diameter tower, Murphree efficiency can be __________ percent. A. 100 B. > 100 C. < 100 D. none of these

A

B. > 100

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68
Q

Compound A is extracted from a solution of A + B into a pure solvent S. A Co-current unit is used for the liquid-liquid extraction. The inlet rate of the solution containing A is 200 moles of B/hr.m2 and the solvent flow, rate is 400 moles of S/m2. hr. The equilibrium data is represented by Y = 3X2 , where Y is in moles of a A/moles of B and X is in moles A/moles of S. The maximum percentage extraction achieved in the unit is A. 0.25 B. 0.5 C. 0.7 D. 0.9

A

B. 0.5

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69
Q

Raoult’s law is applicable to the A. ideal solutions B. real solutions C. mixture of water and alcohol D. non-ideal gases

A

A. ideal solutions

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70
Q

Weeping in a distillation column A. increase tray efficiency. B. provides large interfacial surface for mass transfer. C. results due to very high gas velocity. D. results due to very low gas velocity.

A

D. results due to very low gas velocity.

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71
Q

In case of binary distillation, increasing the reflux ratio above optimum does not result in the increase of A. area between operating line and 45° diagonal x-y diagram. B. condenser and reboiler surfaces. C. tower cross-section. D. none of these.

A

A. area between operating line and 45° diagonal x-y diagram.

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72
Q

Wetted wall tower experiment determines the A. molal diffusivity. B. volumetric co-efficient. C. mass transfer co-efficient. D. none of these.

A

C. mass transfer co-efficient.

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73
Q

In McCabe-Thiele method, at infinite reflux ratio A. the overhead product is minimum. B. both the operating lines coincide with diagonal. C. both (a) and (b). D. neither (a) nor (b).

A

A. the overhead product is minimum.

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74
Q

With decrease in the throughput (compared with the design capacity) for a bubble cap distillation column, its efficiency A. increases B. decreases C. remains same D. may increase or decrease ; depends on individual design

A

A. increases

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75
Q

Plate towers are preferred to packed towers, when large temperature changes are involved, because of the reason that the A. packing may be crushed due to thermal expansion/contraction of the components of the equipments. B. pressure drop in the equipment will be very high. C. viscosity variation of the fluids may cause channeling/flooding. D. none of these.

A

A. packing may be crushed due to thermal expansion/contraction of the components of the equipments.

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76
Q

The equilibrium liquid composition compared to the vapor composition in case of azeotropic mixture is A. more B. less C. same D. either more or less; depends on the system

A

C. same

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77
Q

Out of the following gas-liquid contacting devices, for a given set of operating conditions, gas pressure drop is the least in __________ tower. A. wetted wall B. bubble cap C. perforated tray D. packed

A

A. wetted wall

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78
Q

Pick out the system with minimum boiling azeotrope at 1 atm. A. benzene-toluene B. ethyl alcohol-water C. hydrochloric acid-water D. all (a), (b) and (c)

A

B. ethyl alcohol-water

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79
Q

Free flowing granular materials can be best dried in a __________ drier. A. rotary B. cylinder C. drun D. freeze

A

A. rotary

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80
Q

In case of an ideal solution, the total vapor pressure varies __________ with the composition expressed as mole fraction, A. inversely B. linearly C. exponentially D. none of these

A

B. linearly

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81
Q

Corresponding to Nusselt number in heat transfer, the dimensionless group in mass transfer is the __________ number. A. Sherwood B. Schmidt C. Peclet D. Stanton

A

A. Sherwood

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82
Q

If the specific heats of a gas and a vapor are 0.2KJ/Kg.°K and 1.5 KJ/Kg.°K respectively, and the humidity is 0.01; the humid heat in KJ/°Kg. is A. 0.31 B. 0.107 C. 0.017 D. 0.215

A

D. 0.215

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83
Q

Liquid diffusivity is of the order of __________ cm2 /second. A. 0.01 B. 0.1 C. 10-5 to 10-6 D. > 1

A

C. 10-5 to 10-6

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84
Q

The solvent used in liquid extraction should not have high latent heat of vaporisation, because A. the pressure drop and hence the pumping cost will be very high. B. it cannot be recovered by distillation. C. its recovery cost by distillation may be prohibitatively high. D. it will decompose while recovering by distillation.

A

C. its recovery cost by distillation may be prohibitatively high.

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85
Q

At the same gas flow rate, the pressure drop in a packed tower being irrigated with liquid __________ that in dry packed tower. A. is greater than B. is lower than C. is same as D. cannot be predicted as data are insufficient

A

A. is greater than

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86
Q

Molarity is defined as the number of gm moles of solute per __________ of solvent. A. liter B. kg C. gm D. c.c

A

A. liter

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87
Q

The value of Lewis number (Le = Sc/Pr) for air-water vapour system is around A. 1 B. 0.24 C. 3.97 D. 600

A

A. 1

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88
Q

Which of the following T-H diagram is valid for dehumidification operation? A. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-501-1.png B. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-501-2.png C. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-501-3.png D. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-501-4.png

A

A. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-501-1.png

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89
Q

An aqueous solution of methanol is to be distilled in a tray column. High pressure steam is available as a source of heat. For a given reflux ratio and overhead composition, two options are being explored; (i) a reboiler is used and (ii) no reboiler is used but steam is fed directly to the bottom of the column. As compared to option (i), in option (ii) A. less number of trays are required. B. composition of the residue remains unchanged. C. more number of trays are required but the residue composition remains unchanged. D. more number of trays are required and the residue composition is more dilute in methanol.

A

A. less number of trays are required.

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90
Q

The partial pressure distribution of an ideal gas diffusing through another stagnant ideal gas at steady state follows a/an __________ law. A. exponential B. parabolic C. linear D. cubic

A

A. exponential

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91
Q

Which of the following binary systems is an example of a maximum boiling azeotrope? A. Water-hydrochloric acid. B. Acetone-carbon disulphide. C. Water-ethyl alcohol. D. n-heptane-n-octane.

A

A. Water-hydrochloric acid.

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92
Q

(NRe . NSc) is termed in mass transfer operation as the __________ number. A. Stanton B. Sherwood C. Peclet D. none of these

A

C. Peclet

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93
Q

The binary diffusivity in gases and liquids vary respectively as A. T^3/2 and T B. T and T^3/2 C. sqrt(T) and T^3/2 D. T^3/2 and sqrt(T)

A

A. T^3/2 and T

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94
Q

Pick out the correct statement. A. The slope of the stripping line is always less than unity. B. For a given separation in a binary distillation column, with increase in reflux ratio (above the minimum reflux ratio), the fixed cost of the distillation column first increases and then decreases. C. In Ponchon-Savarit method of no. of theoretical plate determination, the stripping and rectifying operating lines are vertical at total reflux. D. Kremsor-Brown-Souder’s equation is used to calculate the efficiency of a plate tower.

A

C. In Ponchon-Savarit method of no. of theoretical plate determination, the stripping and rectifying operating lines are vertical at total reflux.

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95
Q

Pick out the correct statement. A. Dialysis process is used for the production of fresh water from brine. B. Electrodylsis is used in the manufacture of NaOH. C. Electrodylsis is used for the refin-ning/purification of petrol. D. both (b) and (c).

A

B. Electrodylsis is used in the manufacture of NaOH.

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96
Q

Pick out the correct statement. A. Bound moisture is removed during constant rate drying period. B. Free moisture is removed during falling rate drying period. C. The sum of free moisture and equilibrium moisture in a solid is called the critical moisture. D. The driving force for mass transfer in a wet solid is its free moisture content.

A

D. The driving force for mass transfer in a wet solid is its free moisture content.

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97
Q

Very tall packed towers are divided into series of beds to A. reduce the overall pressure drop B. avoid channelling C. reduce liquid hold-up D. avoid flooding

A

B. avoid channelling

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98
Q

Moisture contained by a substance in excess of the equilibrium moisture is called the __________ moisture. A. unbound B. free C. critical D. bound

A

B. free

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99
Q

With increase in temperature, the solubility of gases in liquids, at fixed pressure A. increases B. decreases C. remains same D. either (a) or (b), depends on the system

A

B. decreases

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100
Q

In most of the vacuum crystalliser, vacuum is generally produced by means of a A. suction pump B. compressed air jet C. steam jet ejector with a barometric condenser D. none of these

A

C. steam jet ejector with a barometric condenser

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101
Q

On moving the feed line (q-line) from saturated liquid feed (vertical position) to saturated vapor feed (horizontal feed), if the slope of both the operating lines are to be increased, then it will result in A. greater degree of separation with a fixed number of trays B. increased reboiler load C. increased reflux ratio D. None of these.

A

C. increased reflux ratio

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102
Q

__________ column is the most suitable for achieving the best performance for mass transfer operations involving liquid with dispersed solids. A. Watted wall B. Packed C. Plate D. Spray

A

C. Plate

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103
Q

Deairation (removal of O2) of water is done by A. rectification B. absorption C. ion-exchange D. adsorption

A

C. ion-exchange

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104
Q

Make up water is supplied during cooling tower operation to compensate for water losses due to A. evaporation B. blowdown C. entrainment D. all (a), (b)&(c)

A

D. all (a), (b)&(c)

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105
Q

Pick out the wrong statement. A. The mole fraction of solute is directly proportional to the molality of a ‘dilute’ solution. B. For a non-reacting binary mixture of ideal gases, the partial pressure distribution of both components is nonlinear in the case of steady state unimolal unidirectional diffusion. C. Azeotropes obey Raoult’s law at all temperature. D. The relative volatility of a binary mixture at the azeotropic composition is 1.

A

C. Azeotropes obey Raoult’s law at all temperature.

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106
Q

A minimum boiling azeotrope is exemplified by A. toluene-benzene B. acetone-carbon disulphide C. water-isobutyl alcohol D. none of these

A

B. acetone-carbon disulphide

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107
Q

Which of the following solutions will follow Raoult’s law most closely? A. A solution of benzene, toluene and oxylene. B. 35% solution of camphor in water. C. 35% solution of NH3 in water. D. A solution of polar organic compounds (not of homologs of a series).

A

A. A solution of benzene, toluene and oxylene.

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108
Q

Use of raschig rings in place of crushed stones as packing in packed beds (other things being same) A. increases pressure drop, increases surface area. B. increases pressure drop, decreases surface area. C. decreases pressure drop, increases surface area. D. decreases pressure drop, decreases surface area.

A

C. decreases pressure drop, increases surface area.

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109
Q

Critical humidity of a solid salt means the humidity A. above which it will always become damp. B. below which it will always stay dry. C. both (a) and (b). D. above which it will always become dry and below which it will always stay damp.

A

C. both (a) and (b).

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110
Q

The assumption made in Elis method in distillation is that enthalpy concentration lines of vapor and liquid are A. parallel B. straight C. both parallel and straight D. neither parallel nor straight

A

C. both parallel and straight

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111
Q

As complete saturation of an adsorbent is approached, the differential heat of adsrop-tion approaches A. that of normal condensation. B. integral heat of adsorption. C. zero. D. none of these.

A

A. that of normal condensation.

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112
Q

Absorption with chemical reaction’ is involved in the removal of A. carbon dioxide from gaseous stream using alkaline solution. B. benzol from coke oven gas using solar oil/wash oil. C. ammonia from coke oven gas using refrigerated water. D. tar from coke oven gas in primary gas coolers using chilled water.

A

A. carbon dioxide from gaseous stream using alkaline solution.

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113
Q

The-relative volatility for separation of a non-ideal binary mixture by distillation should be A. 0 B. 1 C. > 1 D. < 1

A

C. > 1

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114
Q

Pick out the wrong statement: A. Reboiler is not used in open steam distillation. B. The separation of solutes of different molecular sizes in a liquid solution by use of a suitable membrane is called dialysis. C. Freeze drying is used for the drying of fish. D. Fenske-Underwood equation is used for calculating theoretical number of plates in a distillation column at normal operating reflux condition.

A

D. Fenske-Underwood equation is used for calculating theoretical number of plates in a distillation column at normal operating reflux condition.

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115
Q

In paper industry, paper is dried in a __________ dryer. A. tunnel B. heated cylinder C. conveyor D. festoon

A

B. heated cylinder

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116
Q

Pick out the wrong statement. A. Critical moisture content is not a property of the material itself. B. A sharp increase in pressure drop gives an indication of the flooding in a distillation column. C. Separation of components is not possible in liquid extraction, if selectivity is unity. D. Dehydration of ethyl alcohol is most economically done by molecular distillation at very high vacuum.

A

D. Dehydration of ethyl alcohol is most economically done by molecular distillation at very high vacuum.

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117
Q

Only small amount of evaporation of water produces large cooling effects because of its A. large latent heat B. low viscosity C. small latent heat D. none of these

A

A. large latent heat

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118
Q

The most common packing used in industrial operations is __________ rings. A. raschig B. lessing C. cross-partition D. single spiral

A

A. raschig

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119
Q

When the feed to a distillation column is a saturated liquid, slope of the feed line is A. zero B. unity C. infinity D. none of these

A

C. infinity

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120
Q

Leaching of sugar from sugar beets is done by A. hot water B. hexane C. dilute H2SO4 D. lime water

A

A. hot water

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121
Q

Absorption factor method is used to calculate the number of ideal stages, when A. operating line lies above the equilibrium line. B. operating line lies below the equilibrium line. C. both operating and equilibrium lines are parallel. D. pressure drop in the column is very high.

A

C. both operating and equilibrium lines are parallel.

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122
Q

Flights in a rotary dryer are provided to A. lift and shower the solids thus exposing it thoroughly to the drying action of the gas. B. reduce the residence time of solid. C. increase the residence time of the solid. D. none of these.

A

A. lift and shower the solids thus exposing it thoroughly to the drying action of the gas.

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123
Q

If f = moles of vapour present per mole of feed, then the slope of feed line is (Mcabe-Thiele method) A. (1-f)/f B. -(f-1)/f C. -1/f D. -f/(1-f)

A

C. -1/f

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124
Q

If the solubilities of different components (in a liquid-liquid extraction system) increase with rise in temperature, then the temperature above which they dissolve completely is known as the critical solution temperature (CST or consolute temperature). If solubilities increase with decrease in temperature, then CST is the temperature below which they dissolve completely. If a binary system has no critical solution temperature, it implies that A. the system comprises of partially miscible liquids. B. the system comprises of miscible liquids. C. the system comprises of an azeotrope. D. on heating, a vapor phase will appear ; while on cooling, a solid phase will appear.

A

D. on heating, a vapor phase will appear ; while on cooling, a solid phase will appear.

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125
Q

The rate of mass transfer is not dependent upon the A. degree of dispersion of one fluid in the other. B. interfacial surface exposed between the phases. C. both (a) & (b). D. none of these.

A

D. none of these.

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126
Q

At equilibrium the concentration of water in vapour phase (C)in kg/m3 of air space and the amount of water (m) adsorbed per kg of dry silica gel are related by, C = 0.0667m. To maintain dry conditions in a room of air space 100m3 containing 2.2 kg of water vapour initially, 10 kg of dry silica gel is kept in the room. The fraction of initial water remaining in the air space after a long time (during which the temperature is maintained constant) is A. 0 B. 0.2 C. 0.4 D. 1

A

C. 0.4

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127
Q

Dry bulb temperature of unsaturated air is more than its __________ temperature. A. dew point B. wet bulb C. both ‘a’ & ‘b’ D. neither ‘a’ nor ‘b’

A

C. both ‘a’ & ‘b’

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128
Q

For the case of flow of air past a wet bulb thermometer (air water vapour system), the approximate value of h2/ky.Cz is around A. 0.6 B. 0.24 C. 1 D. 0.72

A

C. 1

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129
Q

The reciprocal of stripping factor is termed as A. selectivity index B. relative volatility C. absorption factor D. Murphree efficiency

A

C. absorption factor

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130
Q

Ponchan-Savarit method analyses the fractional equipment based on A. enthalpy balance only. B. material balance only. C. both enthalpy and material balances. D. the assumption of constant molaloverflow.

A

C. both enthalpy and material balances.

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131
Q

The binary diffusivity in gases at atmospheric conditions is about A. 10^-9 cm/sec B. 10^-1 cm2/sec C. 10^-3 sec/cm D. 10^-4 cm2/sec2

A

B. 10^-1 cm2/sec

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132
Q

Percentage saturation is __________ the relative saturation. A. always smaller than B. always greater than C. not related to D. none of these

A

A. always smaller than

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133
Q

In case of a desorber (stripper), the A. operating line always lies above the equilibrium curve. B. operating line always lies below the equilibrium curve. C. temperature remains unaffected. D. temperature always increases.

A

B. operating line always lies below the equilibrium curve.

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134
Q

What is the reflux ratio at total reflux? A. Zero B. Infinity C. Unity D. Data insufficient

A

B. Infinity

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135
Q

Under conditions of flooding in packed tower, the gas pressure drop A. decreases rapidly B. increases rapidly C. remains constant D. is maximum

A

D. is maximum

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136
Q

For achieving rapid drying rate in a spray dryer, the diameter of the particles in the feed should be in the range of __________ microns (1 mm = 1000 microns). A. 45296 B. 10-60 C. 200-300 D. > 500

A

B. 10-60

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137
Q

For absorbing a sparingly soluble gas in a liquid A. gas side mass transfer co-efficient should be increased. B. liquid side mass transfer co-efficient should be increased. C. liquid side mass transfer co-efficient should be decreased. D. mass transfer co-efficient must be kept constant.

A

B. liquid side mass transfer co-efficient should be increased.

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138
Q

Channelling in a packed tower results from the A. high pressure drop B. maldistribution of liquid C. non-uniformity of packing D. both (b) and (c)

A

D. both (b) and (c)

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139
Q

The change in enthalpy per unit weight of adsorbed gas when adsorbed on gas free or “outgassed” adsorbent to from a definite concentration of adsorbate is called its A. integral heat of adsorption. B. heat of wetting. C. differential heat of adsorption. D. heat of normal condensation.

A

A. integral heat of adsorption.

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140
Q

The minimum number of theoretical plates is required for achieving a given separation in distillation column with A. no reflux B. total reflux C. zero reflux ratio D. minimum reflux ratio

A

B. total reflux

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141
Q

A good solvent used for absorption should not have very high A. viscosity B. vapor pressure C. freezing point D. all (a), (b) & (c)

A

D. all (a), (b) & (c)

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142
Q

In a counter-current liquid extractor A. both liquids flow at fixed rate. B. both liquids can have any desired flow rate. C. only one of the liquids may be pumped at any desired rate. D. liquid’s flow rate depends upon the temperature and pressure.

A

C. only one of the liquids may be pumped at any desired rate.

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143
Q

Which of the following is an undesirable property for an absorbing solvent ? A. Low vapour pressure B. Low velocity C. Low freezing point D. None of these

A

D. None of these

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144
Q

The wetted wall tower is used to determine A. individual mass transfer co-efficient (M.T.C.) in gaseous system. B. M.T.C. of individual components in a liquid-liquid system. C. M.T.C. of liquid in liquid-gas system. D. the overall M.T.C. of the system.

A

A. individual mass transfer co-efficient (M.T.C.) in gaseous system.

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145
Q

Weight of 1 m3 of humid air as compared to 1 m3 of dry air, under the same conditions, is A. less B. more C. same D. unpredictable

A

A. less

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146
Q

Positive deviation from Raoult’s law means a mixture whose total pressure is A. greater than that computed for ideality. B. less than that computed for ideality. C. less than the sum of the vapour pressure of the components. D. none of these.

A

A. greater than that computed for ideality.

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147
Q

With increase in gas rate, the number of transfer units, NtoG, for a fixed degree of absorption by a fixed amount of solvent A. increases B. decreases C. decreases linearly D. remains unaffected

A

A. increases

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148
Q

Schmidt number is given by A. μ/ρDAB B. Re.Pe C. Sh x Pe D. Re/Pe

A

A. μ/ρDAB

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149
Q

The caking of crystals can be prevented by A. maintaining high critical humidity. B. maintaining low critical humidity. C. coating the product with inert material. D. both (a) and (c)

A

D. both (a) and (c)

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150
Q

Prandtl number for water at 20°C is about A. 7 B. 70 C. 0.7 D. 150

A

A. 7

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151
Q

Boiling point diagram is A. not affected by pressure. B. affected by pressure. C. a plot of temperature vs. liquid composition. D. a plot of temperature vs. vapour composition.

A

B. affected by pressure.

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152
Q

When acetone is added in a two layer mixture of methyl isobutyl ketone and water at 30°C, the acetone distributes between the two layers and the composition of the layer follows two solubility curves. For this system, A. as the acetone concentration increases, the solubility curves approach each other. B. both the phases become identical at a particular common point on both the solubility curves called the plait point. C. the distribution curve which is a plot between x (acetone concentration in one phase) and y (acetone concentration in other phase) is analogous to x-y curve used in distillation and absorption terminates on the x = y diagonal at the concentration of the plait point. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

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153
Q

Steam distillation is used to A. reduce the number of plates. B. avoid thermal decomposition of a component. C. increase the efficiency of separation. D. increase the total pressure of distillation.

A

B. avoid thermal decomposition of a component.

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154
Q

Freundlich equation applies to the adsorption of solute from A. dilute solutions, over a small concentration range. B. gaseous solutions at high pressure. C. concentrated solutions. D. none of these.

A

A. dilute solutions, over a small concentration range.

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155
Q

For ethanol-water system, the lowering of distillate quality from 95% to 92% will cause __________ plate requirement. A. no change in theoretical B. marginal decrease in the number of C. major decrease in the number of D. none of these

A

B. marginal decrease in the number of

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156
Q

The apex of an equilateral-triangular coordinate (in ternary liquid system) represents a/an A. pure component B. binary mixture C. ternary mixture D. insoluble binary system

A

A. pure component

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157
Q

The diffusivity (D) in a binary gas mixture is related to the pressure (P) as A. D ∝ P^0.5 B. D ∝ 1/P^0.5 C. D ∝ 1/P D. D ∝ 1/P^1.5

A

C. D ∝ 1/P

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158
Q

A slurry is to be dried to produce flaky solid. Which dryer would you recommend? A. Spray dryer B. Drum dryer C. Rotary dryer D. Dielectric dryer

A

A. Spray dryer

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159
Q

Which of the following psychrometric processes is followed by water vapour laden unsaturated air, when it is passed through solid or liquid adsorbent? A. Cooling and dehumidification. B. Heating and dehumidification at almost constant wet bulb temperature. C. Dehumidification with dry bulb temperature remaining constant. D. None of these.

A

B. Heating and dehumidification at almost constant wet bulb temperature.

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160
Q

In gas-liquid contact operation, the number of ideal stages, https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/331-646-1.png . This is true when the stripping factor ‘S’ is (see picture) A. S > 1 B. S < 1 C. S = 1 D. S = ∞

A

A. S > 1

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161
Q

The cooling effect in a cooling tower can not be increased by A. increasing the air velocity over the wet surfaces. B. reducing the humidity of entering air. C. lowering the barometric pressure. D. none of these.

A

D. none of these.

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162
Q

The value of NA/(NA + NB) for steady state molecular diffusion of gas ‘A’ through non-diffusing gas ‘B’ is A. 1 B. ∞ C. 0.5 D. 2

A

A. 1

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163
Q

The humid volume may be increased by increasing the A. temperature at constant humidity. B. humidity at constant temperature. C. both (a) and (b). D. neither (a) nor (b).

A

C. both (a) and (b).

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164
Q

Pick out the wrong statement A. Co-current absorbers are usually used, when the gas to be dissolved in the liquid is a pure substance. B. In case of gas absorption, HETP is equal to HTU, when both the operating line & the equilibrium lines are parallel. C. Hatta number is important in case of gas absorption with chemical reaction. D. In actual practice, absorption is an en-dothermic process, while stripping is an exothermic process.

A

D. In actual practice, absorption is an en-dothermic process, while stripping is an exothermic process.

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165
Q

When the mixture to be distilled has a very high boiling point and the product material is heat sensitive, the separation technique to be used is __________ distillation. A. continuous B. steam C. azerotropic D. none of these

A

B. steam

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166
Q

Large scale drying of wheat is done in a __________ dryer. A. fluidised bed B. spouted bed C. tray D. vacuum rotary

A

B. spouted bed

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167
Q

Azeotropic distillation is employed to separate A. constant boiling mixture. B. high boiling mixture. C. mixture with very high relative volatility. D. heat sensitive materials.

A

A. constant boiling mixture.

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168
Q

The drying time between fixed moisture content within diffusion controlled ‘falling rate period’ is proportional to (assuming that drying occurs from all surfaces of the solid) (where, T = thickness of the solid) A. sqrt*(T) B. T C. T^2 D. T^3

A

C. T^2

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169
Q

At the boiling point of the liquid at the prevailing pressure, the saturated absolute humidity becomes A. 1 B. 0 C. ∞ D. none of these

A

C. ∞

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170
Q

Use of natural draft cooling tower is practised, when the air has low A. humidity B. temperature C. both ‘a’ & ‘b’ D. neither ‘a’ nor ‘b’

A

C. both ‘a’ & ‘b’

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171
Q

Pressure drop through plate tower as compared to that through packed tower, for the same duty will be A. less B. more C. equal D. either (a) or (b); depends on the packing height

A

B. more

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172
Q

Dimension of mass diffusivity is the same as that of A. kinematic viscosity B. dynamic viscosity C. surface tension D. pressure

A

A. kinematic viscosity

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173
Q

Dorr thickener is an equipment used for A. classification B. sedimentation C. clarification D. leaching

A

B. sedimentation

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174
Q

Steam distillation is used to separate A. azeotropes. B. high boiling substances from nonvolatile impurities. C. heat sensitive materials. D. mixtures of low relative volatility.

A

B. high boiling substances from nonvolatile impurities.

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175
Q

In distillation where q is defined as the moles of liquid flow in the stripping section per mole of feed introduced, for saturated liquid feed A. q > 1 B. q < 1 C. q = 1 D. q = 0

A

C. q = 1

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176
Q

Which of the following is an undesirable property in a tower packing? A. Large surface per unit volume. B. Large free cross-section. C. Low weight per unit volume. D. Large weight of liquid retained.

A

D. Large weight of liquid retained.

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177
Q

Water entrained by circulating air in cooling towers is termed as A. drift B. blow down C. vapor load D. none of these.

A

A. drift

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178
Q

A 25 cm x 25 cm x 1 cm flat sheet weighing 1.2 kg initially was dried from both sides under constant drying rate conditions. It took 1500 seconds for the weight of the sheet to reduce to 1.05 kg. Another 1m x 1m x 1cm flat sheet of the same material is to be dried from one side only.Under the same constant drying rate conditions, the time required for drying (in seconds) from its initial weight of 19.2 kg to 17.6 kg is A. 1000 B. 1500 C. 2000 D. 2500

A

A. 1000

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179
Q

With increase in temperature, the rate of leaching increases, because the A. diffusivity of solute increases. B. viscosity of solvent decreases. C. thermal conductivity of solute increases. D. none of these.

A

A. diffusivity of solute increases.

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180
Q

Humidity chart is useful for the solution of problems concerning condensation, vaporisation and air conditioning. At a given dry bulb temperature, value of humidity obtained from the humidity chart directly, is in terms of __________ humidity.
molal A. molal B. relative C. percentage D. none of these

A

A. molal

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181
Q

The Kundsen diffusivity is proportional to (where, T = absolute temperature) A. sqrt(T) B. T^2 C. T D. T^4

A

A. sqrt(T)

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182
Q

In case of constant underflow extraction operation, the __________ at all solute concentration. A. solids are drained to the same extent B. ratio of the insoluble to solution is constant C. both(a) & (b) D. neither (a) nor (b)

A

C. both(a) & (b)

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183
Q

In an absorption coloumn, the flooding velocity for random packing is __________ that for stacked/regular packing. A. greater than B. smaller than C. equal to D. either (a), or (b) ; depends on the type of packing

A

B. smaller than

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184
Q

The relation among various mass transfer co-efficients (M.T.C) for ideal gases is given by (where, Kc & Km are M.T.C. for equimolar counter diffusion with concentration & mole fraction respectively as the driving force. and, Kp = M.T.C. for diffusion of a gas through a stagnant inert gas with pressure as driving force.) A. Kc = Kp = Km B. Kc = Kp/RT = Km . RT/P C. Kc = Kp . RT = Km . RT/p D. none of these

A

C. Kc = Kp . RT = Km . RT/p

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185
Q

With increase in temperature, the leaching rate increases because of the A. increased diffusivity. B. decreased viscosity of liquid. C. both (a) and (b). D. neither (a) nor (b).

A

C. both (a) and (b).

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186
Q

Leaching of uranium ore and gold ore is done in A. centrifugal extractor B. Pachuka tanks C. Bollman extractor D. none of these

A

B. Pachuka tanks

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187
Q

Blowdown in a cooling tower A. means discarding a small fraction of circulating water to prevent and limit the concentration of salt and impurities. B. increases the scale forming tendencies of water. C. is undesirable. D. all (a), (b) & (c).

A

A. means discarding a small fraction of circulating water to prevent and limit the concentration of salt and impurities.

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188
Q

During constant rate period, the rate of drying decreases with the A. decrease in air temperature B. increase in air humidity C. both (a) and (b) D. neither (a) nor (b)

A

C. both (a) and (b)

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189
Q

Antibiotics are best handled in a A. Podbielniak extractor. B. sieve tray contractor. C. rotating disc contactor. D. pulsed column extractor.

A

A. Podbielniak extractor.

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190
Q

The fixed cost of a distillation column at minimum reflux ratio is A. minimum B. infinite C. optimum D. none of these

A

B. infinite

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191
Q

__________ extractor uses centrifugal force for separating the two phases. A. Treybal B. Schiebel C. Podbielniak D. None of these

A

C. Podbielniak

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192
Q

In a binary distillation column, if the feed contains 40 mole % vapour, the q line will have a slope of A. 1.5 B. -0.6 C. -1.5 D. 0.6

A

C. -1.5

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193
Q

Pick out the wrong statement. A. Mechanical agitation is required, if the system has low interfacial tension. B. Seive tray towers are generally used for systems having low interfacial tension. C. When Henry’s law constant is very small, then the mass transfer rate is controlled by the gas film resistance. D. Taylor-Prandtl analogy for heat and mass transfer considers the transfer through both laminar and turbulent layers.

A

A. Mechanical agitation is required, if the system has low interfacial tension.

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194
Q

Acetic acid will be most economically separated from a dilute solution of acetic acid in water by A. solvent extraction B. continuous distillation C. evaporation D. absoprtion

A

A. solvent extraction

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195
Q

Design calculation for multiple component distillation is done by A. Ponchon-Savarit method B. Mccabe-Thiele method C. enthalpy concentration method D. tray to tray calculations.

A

D. tray to tray calculations.

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196
Q

To get high tray efficiency A. interfacial surface between liquid and gas phase should be large. B. time of contact between the two phases should be less. C. gas velocity should be very low. D. liquid entrainment should be severe.

A

A. interfacial surface between liquid and gas phase should be large.

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197
Q

The mass transfer co-efficient for a solid sphere of radius ‘a’ dissolving in a large volume of quiescent liquid, in which D is the diffusivity of solute, is A. D/a B. D/2a C. proportional to sqrt(D) D. dependent on the Reynolds number

A

D. dependent on the Reynolds number

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198
Q

Pick out the wrong statement. Generally for physical adsorption, a gas of A. higher molecular weight is adsorbed in preference to a gas of low molecular weight. B. high critical temperature is adsorbed in preference to a gas of low critical temperature. C. low volatility is adsorbed in preference to a gas of high volatility. D. none of these.

A

D. none of these.

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199
Q

In most of the mechanically agitated liquid-liquid extractors, baffles or horizontal compartmental plates are provided, which helps in A. reducing the axial mixing. B. increasing the rate of extraction. C. maintaining the concentration difference between the two phases. D. all ‘a’, ‘b’ & ‘c’.

A

D. all ‘a’, ‘b’ & ‘c’.

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200
Q

In a vapor-liquid contacting equipment, the overall gas phase mass transfer co-efficient (M.T.C), KG is related to individual co-efficients (KG and KL) as A. KG = 1/KG + m/KL B. 1/KG = 1/KG + m/KL C. 1/KG = 1/KL + m/KG D. KG = 1/KL + m/KG

A

B. 1/KG = 1/KG + m/KL

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201
Q

Solvent extraction is the terminology applied to the liquid-liquid extraction, which is preferred for the separation of the components of liquids, when A. extracting solvent is cheaply & abundantly available. B. one of the liquid components is heat sensitive. C. viscosity of liquid components is very high. D. one of the liquid components has very high affinity towards the solvent.

A

D. one of the liquid components has very high affinity towards the solvent.

202
Q

Inside the distillation column, the A. driving force for the vapour flow is the pressure drop. B. liquids are not always at their bubble points. C. pressure increases gradually from bottom to the top of the column. D. none of these

A

A. driving force for the vapour flow is the pressure drop.

203
Q

Diffusivity in concentrated solutions differs from that in dilute solutions, because of the changes in A. viscosity with concentration. B. degree of ideality of the solution. C. both (a) and (b). D. neither (a) nor (b).

A

C. both (a) and (b).

204
Q

Occurrence of ‘case hardening’ during drying of a high moisture solid cake __________ the drying rate. A. increases B. decreases C. does not affect D. exponentially increases

A

B. decreases

205
Q

Which of the following is not a continuous drier? A. Drum drier B. Spray drier C. Tunnel drier D. Tray drier

A

D. Tray drier

206
Q

Humidification involves mass transfer between a pure liquid phase and a fixed gas, which is A. insoluble in the liquid B. soluble in the liquid C. non-ideal in nature D. at a fixed temperature

A

A. insoluble in the liquid

207
Q

__________ is the temperature at which a gas-vapor mixture becomes saturated, when cooled at constant total pressure out of contact with a liquid. A. Dew point B. Bubble point C. Dry bulb temperature D. Wet bulb temperature

A

A. Dew point

208
Q

Rate of leaching increases with increasing A. temperature B. viscosity of solvent C. pressure D. size of the solid

A

A. temperature

209
Q

An azeotropic mixture is a __________ mixture. A. binary B. ternary C. constant boiling point D. none of these

A

C. constant boiling point

210
Q

Pick out the wrong statement. A. In the McCabe-Thiele diagram for binary distillation, vertical feed line represents saturated liquid feed and horizontal feed line represents saturated vapour feed. B. In small columns, local efficiency is larger than Murphree efficiency; in large columns local efficiency is smaller than Murphree efficiency. C. For Laminar flow over a plate of length L, the local mass transfer co-efficient at a distance L from the leading edge is 1.5 x 10-2m/s. Then the average mass transfer co-efficient for the plate is 2 x 10-2m/s. D. The concentration and hydrodynamic boundary layers over a flat plate are of equal thickness, if Schmidt number is equal to unity.

A

C. For Laminar flow over a plate of length L, the local mass transfer co-efficient at a distance L from the leading edge is 1.5 x 10-2m/s. Then the average mass transfer co-efficient for the plate is 2 x 10-2m/s.

211
Q

Molecular seives are regenerated by heating to __________ °C. A. < 150 B. 200-330 C. > 500 D. > 1000

A

B. 200-330

212
Q

In continuous distillation, the internal reflux ratio (Ri) and the external reflux ratio (Re) are related as A. Ri = Re/1-Re B. Ri = 1-Re/Re C. Ri = Re D. Ri = Re/1+Re

A

D. Ri = Re/1+Re

213
Q

In a counter-current extractor, as the axial mixing increases, the extraction efficiency A. increases B. decreases C. remains unchanged D. depends on the pressure of the system

A

B. decreases

214
Q

Heat sensitive materials like certain pharmaceuticals and food stuffs can be dried in a/an __________ dryer. A. indirect tray B. spray C. freeze D. none of these

A

C. freeze

215
Q

In extractive distillation, solvent is A. added to alter the relative volatility of the mixture. B. of high volatility. C. present in overhead stream. D. of high viscosity to give high tray efficiency.

A

A. added to alter the relative volatility of the mixture.

216
Q

Radioactive nuclear waste is treated in A. mixer-settler extractor B. rotating-disc contactor C. pulsed column extractor D. Bollman extractor

A

C. pulsed column extractor

217
Q

Large scale drying of sugar is done in a __________ dryer. A. spouted bed B. tray C. rotary D. truck

A

C. rotary

218
Q

__________ temperature is the steady state temperature attained by a small amount of liquid evaporating into a large quantity of unsaturated gas-vapor mixture. A. Dry bulb B. Wet bulb C. Dew point D. none of these

A

B. Wet bulb

219
Q

The drying time between fixed moisture contents within the ‘constant rate period’ is proportional to (assuming that drying occurs from all surfaces of the solid) (where, T = thickness of the solid) A. sqrt(T) B. T C. T^1.5 D. T^3

A

B. T

220
Q

__________ equation applies to diffusivities in liquids. A. Gilliland B. Hirschfelder C. Wilke and Chang D. none of these

A

A. Gilliland

221
Q

A packed tower compared to a plate tower for a particular mass transfer operation A. incurs smaller pressure drop. B. allows installation of cooling coils. C. is less costly when built in large sizes/diameters. D. is more suitable, if suspended solids are present in fluid streams.

A

A. incurs smaller pressure drop.

222
Q

Which of the following is the most commonly used leaching solvent in vegetable oil industry? A. Phenol B. Hexane C. Furfurol D. Liquid SO2

A

B. Hexane

223
Q

In an absorber, HETP does not vary with the A. flow rate of liquid B. flow rate of gas C. type and size of packing D. none of these

A

D. none of these

224
Q

Large quantity of silica gel is normally dried in a __________ dryer. A. freeze B. through circulation C. rotary vacuum D. tray

A

B. through circulation

225
Q

For the same system, if the same liquid used in an absorber is decreased, the tower height will A. increase B. decrease C. remain unaffected D. decrease or increase ; depends on the type of liquid

A

A. increase

226
Q

Hydrogenation of oil is carried out in a/an __________ in Vanaspati manufacturing plant. A. agitated vessel B. sieve tray column C. bubble cap column D. packed tower

A

A. agitated vessel

227
Q

Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent A. a pure component. B. a binary mixture. C. a ternary mixture. D. partially miscible ternary system.

A

B. a binary mixture.

228
Q

In distillation column design, the McCabe-Thiele procedure is inadequate and a Ponchan-Savarit procedure is needed, when A. saturated feed is not used. B. an azeotrope forms. C. the latent heat of vaporisation of the more and less volatile components are greatly different. D. a total condenser is used.

A

D. a total condenser is used.

229
Q

In an interphase mass transfer process, the lesser the solubility of a given solute in a liquid, the higher are the chances that the transfer process will be A. liquid phase resistance-controlled. B. gas phase resistance controlled. C. impossible. D. driven by a non-linear driving force.

A

B. gas phase resistance controlled.

230
Q

As the reflux ratio decreases, the A. separation becomes more efficient. B. number of plates increases. C. column diameter increases. D. none of these.

A

B. number of plates increases.

231
Q

Which of the following equipments is not used for gas dispersion? A. agitated vessel B. Bubble cap tray towers C. Perforated sieve tray towers D. Spray towers

A

D. Spray towers

232
Q

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 A. the product composition but not the fraction vaporised. B. the product composition as well as the fraction vaporised. C. the fraction vaporised but not the product composition. D. neither the product composition nor the fraction vaporised.

A

C. the fraction vaporised but not the product composition.

233
Q

The equation, https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/315-483-1.png is for (see attached picture) A. steady state equimolar counter diffusion B. Fick’s first law of diffusion C. steady state diffusion for stagnant case D. liquid M.T.C. by penetration theory.

A

A. steady state equimolar counter diffusion

234
Q

With increase in the liquid flow rate at a fixed gas velocity in a randomly packed counter current gas-liquid absorption column, the gas pressure drop A. decreases B. remains unchanged C. increases D. decreases exponentially

A

C. increases

235
Q

The equation, https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/314-467-1.png is for (see attached ppicture) A. Fick’s second law of diffusion. B. stready state diffusion for stagnant case. C. liquid M.T.C. by Higbie penetration theory. D. none of these.

A

B. stready state diffusion for stagnant case.

236
Q

Which of these columns incurs the lowest pressure drop? A. Packed column (with stacked packing) B. Packed column (with dumped packing) C. Bubble plate column D. Pulse column

A

A. Packed column (with stacked packing)

237
Q

In the desorption of highly soluble gas from the liquid, the main resistance will be in the __________ phase. A. gas B. liquid C. both (a) & (b) D. neither (a) nor (b)

A

B. liquid

238
Q

If G = insoluble gas in gas stream and L = non-volatile solvent in liquid stream, then the slope of the operating line for the absorber is A. L/G B. G/L C. always < 1 D. none of these

A

A. L/G

239
Q

Which of the following remains constant during evaporative cooling process with recirculated water supply? A. Relative humidity B. Partial pressure of vapour C. Wet bulb temperature D. None of these

A

C. Wet bulb temperature

240
Q

For stripping of a gas in a counter current stripper, the operating line A. lies above the equilibrium curve. B. lies below the equilibrium curve. C. can lie above or below the equilibrium curve. D. is always parallel to the equilibrium curve.

A

C. can lie above or below the equilibrium curve.

241
Q

Which of the following same diameter columns gives lowest pressure drop per unit height? A. Bubble-cap column B. Sieve-plate column C. Packed column (stacked) D. Randomly packed column

A

C. Packed column (stacked)

242
Q

Diffusion in concentrated solutins differs from that in dilute solutions, because of the change in the __________ with the concentration of the solution. A. degree of ideality B. viscosity C. both ‘a ‘& ‘b’ D. neither ‘a’ nor ‘b’

A

C. both ‘a ‘& ‘b’

243
Q

Stage efficiency in a leaching process depends on the A. time of contact between the solid and the solution B. rate of diffusion of the solute through the solid and into the liquid C. both (a) and (b) D. vapour pressure of the solution

A

C. both (a) and (b)

244
Q

Operating velocity in a packed tower is usually __________ the flooding velocity. A. half B. twice C. equal to D. more than

A

A. half

245
Q

The Knudsen diffusivity is dependent on the A. molecular velocity only. B. pore radius of the catalyst only. C. molecular mean free path only. D. molecular velocity and por radius of the catalyst.

A

D. molecular velocity and por radius of the catalyst.

246
Q

Minimum possible diameter of a packed coloumn is decided mainly by the A. flooding B. gas viscosity C. liquid density D. liquid hold up

A

A. flooding

247
Q

Solvent used in extractive distillation A. is of low volatility. B. forms a low boiling azeotrope. C. forms a high boiling azeotrope. D. does not alter the relative volatility of the original components.

A

B. forms a low boiling azeotrope.

248
Q

Capacity of a rotary dryer depends on its A. r.p.m B. inclination with ground surface C. both (a) and (b) D. neither (a) nor (b)

A

C. both (a) and (b)

249
Q

The cooling effect in a cooling tower can be speeded up by A. increasing the air velocity and area of exposed wet surface. B. reducing the barometric pressure. C. reducing the humidity of the air. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

250
Q

The following plot gives the saturated humidity (He) versus temperature (T).Line joining (H1, T1) and (H2, T2) is the constant enthalpy line. Choose the correct one from among the alternatives A, B, C and D. The following plot gives the saturated humidity (He) versus temperature (T).Line joining (H1, T1) and (H2, T2) is the constant enthalpy line. Choose the correct one from among the alternatives A, B, C and D. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/335-677-1.png A. T1-Dew point temp; T2-Dry bulb temp; T3-Wet bulb temp. B. T1-Dew point temp; T2-Wet bulb temp; T3-Dry bulb temp. C. T1-Wet bulb temp; T2-Dry bulb temp; T3-Dew point temp. D. T1-Dry bulb temp; T2-Wet bulb temp; T3-Dew point temp.

A

D. T1-Dry bulb temp; T2-Wet bulb temp; T3-Dew point temp.

251
Q

When both the fluids flow concurrently in an absorber, the slope of the operating line is A. - ve B. (+) ve C. 1 D. -1

A

A. - ve

252
Q

The percentage humidity is less than the relative humidity only at __________ percent humidity. A. zero B. hundred C. both zero and hundred D. none of these

A

C. both zero and hundred

253
Q

Back-trapping in a distillation column A. increases tray efficiency. B. decreases tray efficiency. C. reduces pressure drop. D. is desirable, as it provides improved vapour-liquid contact.

A

B. decreases tray efficiency.

254
Q

Flooding in a vapor-liquid contacting equipment occurs in a tray, when the pressure drop through a tray is __________ the liquid head available in the downcomer. A. less than B. more than C. same as D. very much less

A

B. more than

255
Q

Milk is dried usually in a __________ dryer. A. freeze B. spray C. tray D. rotary

A

B. spray

256
Q

At a given equilibrium pressure, with increase in temperature, the concentration of adsorbed gas on solid adsorbant A. increases B. decreases C. remains unchanged D. increases exponentially

A

B. decreases

257
Q

Which of the following adsorbent is used to decolourise yellow glycerine? A. Silica gel B. Alumina C. Fuller’s earth D. Activated carbon

A

D. Activated carbon

258
Q

Which of the following liquid temperature (T) Vs. vapor-gas mixture enthalpy (H) diagram is valid for humidification operation? A. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-499-1.png B. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-499-2.png C. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-499-3.png D. none of these.

A

B. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-499-2.png

259
Q

In a distillation column, with increase in the reflux ratio, the heat removed in the cooler A. increases. B. decreases. C. remains unaffected. D. and the heat required in reboiler decreases.

A

A. increases.

260
Q

Pick out the wrong statement. A. Constant pressure distillation can not separate an azeotropic mixture. B. Relative volatility of a binary mixture changes appreciably with the minor change in temperature. C. The relative volatility of a binary mixture at azeotropic composition is unity. D. Flash distillation is practised on wide spread scale in petroleum refinery.

A

B. Relative volatility of a binary mixture changes appreciably with the minor change in temperature.

261
Q

Which of the following is not a unit of mass transfer co-efficient? A. Moles transferred/(time)(area)(mole fraction) B. Moles transferred/(time)(area)(pressure) C. Moles transferred/(time)(area)(mass A/mass B) D. None of these

A

D. None of these

262
Q

The falling rate period in the drying of a solid is characterised by A. increase in rate of drying. B. increasing temperatures both on the surface and within the solid. C. decreasing temperatures. D. none of these.

A

B. increasing temperatures both on the surface and within the solid.

263
Q

In which of the following unit operations, the selectivity is an important parameter? A. Distillation B. Solvent extraction C. Absorption D. None of these

A

B. Solvent extraction

264
Q

Which of the following is an undesirable characteristic for the solvent used in gas absorption? A. Low vapor pressure B. Low viscosity C. High gas solubility D. None of these

A

D. None of these

265
Q

Which of the following equipments is not used for liquid dispersion? A. Wetted wall towers B. Packed towers C. Venturi scrubers D. Agitated vessels

A

D. Agitated vessels

266
Q

Diameter of raschig rings used in packed tower in industry is normally around __________ inches. A. 2 B. 8 C. 12 D. 18

A

A. 2

267
Q

The diffusion co-efficient in m2 /s. of acetic acid in benzene (liquid in liquid) is A. 2.09 x 10-4 B. 2.09 x 10-5 C. 2.09 x 10-9 D. 2.09 x 10-12

A

C. 2.09 x 10-9

268
Q

Pick out the wrong statement. A. The Reynolds analogy for mass transfer is given by Lewis relation and is applicable, when Schmidt number is one. B. Sherwood number for flow in pipes can be expressed as the ratio of the concentration gradient at wall to the overall concentration difference. C. According to film theory for equimolar counter diffusion, the mass transfer coefficient is given by sqrt(DAB)(b)P - 3, Q - 2 D. The z-component of the total mass flux of a component A in binary mixture of A and B is given by - Dab’.dCA/dz.

A

C. According to film theory for equimolar counter diffusion, the mass transfer coefficient is given by sqrt(DAB)(b)P - 3, Q - 2

269
Q

In case of non-ideal gases and liquids, the molal diffusivity A. varies inversely as the pressure. B. varies directly as the pressure. C. is independent of pressure. D. is equal to the volumetric diffusivity.

A

C. is independent of pressure.

270
Q

Condensation of a vapour-gas mixture just begins, when (where, p = partial pressure of the vapour P = vapour pressure of the liquid) A. p = P B. p&raquo_space;P C. p < P D. p &laquo_space;P

A

A. p = P

271
Q

__________ number indicates the ratio of the rates of the heat and mass transfer incase of a cooling tower. A. Sherwood B. Stanton C. Lewis D. Peclet

A

C. Lewis

272
Q

The expression, y(1 - x)/x(1 - y) is for A. absorption factor B. relative volatility C. selectivity D. Murphree efficiency

A

B. relative volatility

273
Q

In physical terms, Schmidt number means A. thermal diffusivity/mass diffusivity. B. thermal diffusivity/momentum diffusivity. C. momentum diffusivity/mass diffusivity. D. mass diffusivity/thermal diffusivity.

A

C. momentum diffusivity/mass diffusivity.

274
Q

In case of liquids, the binary diffusivity is proportional to (where, T = temperature) A. T B. sqrt(T) C. T^2 D. 1/T

A

A. T

275
Q

The diffusivity, DAB (for component A diffusing in B) is equal to the diffusivity DBA (for component B diffusing in A) for a binary mixture of A. Newtonion liquids B. non-Newtonion liquids C. ideal gases D. real gases

A

C. ideal gases

276
Q

Mass transfer co-efficient is directly proportional to DAB0.5, according to __________ theory. A. penetration B. surface renewal C. film D. none of these

A

A. penetration

277
Q

Sand is dried in foundaries in a___drier. A. rotary B. fluidised bed C. vacuum D. spray

A

B. fluidised bed

278
Q

Which of the following employs an accessory known as ‘drift eliminator’? A. Multiple effect evaporator. B. Mechanical draft cooling tower. C. Rotary dryer. D. Rotating disc contactor.

A

B. Mechanical draft cooling tower.

279
Q

Pick out the correct statement. A. Higher hold up of the solid in the rotary dryer results in better exposure of the solids to the gas. B. The ‘Hatta number’ is important in problems involving gas absorption without chemical reaction. C. For a non-reacting binary mixture of ideal gases, the partial pressure distribution of both components is linear in the case of steady state equimolal counter-diffusion. D. Total reflux in case of distillation operation requires infinite number of plates for a binary system separation.

A

C. For a non-reacting binary mixture of ideal gases, the partial pressure distribution of both components is linear in the case of steady state equimolal counter-diffusion.

280
Q

Pick out the correct statement. A. For identical gas flow rates, less pressure drop occurs through a plate tower than through a packed tower. B. Plate column can handle greater liquid loads without flooding than packed column, but the liquid hold up is more in the case of plate column. C. For the same duty, plate columns weigh less than packed columns. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

281
Q

Humid volume is the total volume in m3 of 1 kg of A. vapour laden gas at 1 atm. and room temperature. B. gas plus its accompanying vapour at 1 atm. and room temperature. C. gas plus its accompanying vapour at 1 atm. and gas temperature. D. vapour laden gas at 1 atm. and gas temperature.

A

C. gas plus its accompanying vapour at 1 atm. and gas temperature.

282
Q

Diameter to height ratio for a rashig ring is A. 1 B. 0.5 C. 2 D. 8

A

A. 1

283
Q

The equipment used in the extraction of highly corrosive radio active liquids is A. pulse column B. spray column C. mixer settler D. baffle tower

A

A. pulse column

284
Q

Advantage of continuous drying over batch drying is that the 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’

A

D. all ‘a’, ‘b’ & ‘c’

285
Q

With increase in temperature, the rate of extraction in leaching (solid-liquid extraction system) A. increases B. decreases C. remains unaffected D. increases linearly

A

A. increases

286
Q

In a packed bed absorption column, the channelling will be noted by the A. increase in flow rate. B. sharp drop in pressure drop. C. sharp rise in pressure drop. D. none of these.

A

B. sharp drop in pressure drop.

287
Q

Gaseous diffusivity at atmospheric pressure is of the order of __________ cm2/second. A. 1 B. 1 to 5 C. 5 to 10 D. > 10

A

A. 1

288
Q

In liquid-liquid extraction, the number of phases at plait point is A. 1 B. 2 C. 3 D. 4

A

A. 1

289
Q

In a liquid-liquid extraction, 10 kg of a solution containing 2 kg of solute C and 8 kg of solvent A is brought into contact with 10 kg of solvent B. Solvent A and B are completely immiscible in each other whereas solute C is soluble in both the solvents. The extraction process attains equilibrium. The equilibrium relationship between the two phases is Y* = 0.9X, where Y* is the kg of C/kg of B and X is kg of C/kg of A. Choose the correct answer. A. The entire amount of C is transferred to solvent B. B. Less than 2 kg but more than 1 kg of C is transferred to solvent B. C. Less than 1 kg of C is transferred to B. D. No amount of C is tranferred to B.

A

A. The entire amount of C is transferred to solvent B.

290
Q

The surface renewal frequency in Danckwerts’ model of mass transfer is given by (KL: mass transfer co-efficient) A. sqrt(KL2.DA) B. KL2.DA C. KL2/DA D. KL/DA2

A

A. sqrt(KL2.DA)

291
Q

If Rm is the minimum reflux ratio, the optimum reflux ratio may be around __________ Rm. A. 1.2 to 1.5 B. 2.5 to 3 C. 3 to 4 D. 5

A

A. 1.2 to 1.5

292
Q

During dehumidification of unsaturated air wet bulb temperature & partial pressure of vapor are not constant. However, during evaporative cooling process with recirculated water supply, the __________ remains constant. A. wet bulb temperature B. partial pressure of water vapor C. relative humidity D. none of these

A

A. wet bulb temperature

293
Q

In case of absorption, both the operating and equilibrium lines will be straight for A. isothermal operation. B. dilute solutions. C. dilute solutions and isothermal operation. D. none of these.

A

C. dilute solutions and isothermal operation.

294
Q

Mass transfer co-efficient varies as DAB0.5, according to the __________ theory. A. film B. surface renewal C. penetration D. none of these

A

B. surface renewal

295
Q

For an absorber, both equilibrium and operating line will be straight for 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.

A

C. dilute solution and isothermal operation.

296
Q

A distillation column separates 10000 kg/hr of a benzene-toluene mixture as shown in the figure below: https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/335-680-1.png In the figure xF, xD and xW represent the weight fraction of benzene in the feed, distillate and residue respectively. The reflux ratio is A. 0.5 B. 0.6 C. 1 D. 2

A

B. 0.6

297
Q

Unsaturated air (with dry bulb and wet bulb temperatures being 45°C and 25°C respectively) is passed through a water spray chamber maintained at 23°C. The air will be cooled and A. humidified with wet bulb temperature decreasing. B. humidified at constant wet bulb temperature. C. dehumidified. D. none of these

A

A. humidified with wet bulb temperature decreasing.

298
Q

Humid volume, at a given temperature is a/an __________ function of humidity. A. inverse B. exponential C. linear D. logarithmic

A

C. linear

299
Q

The Schmidt number which is defined as, μ/ρ D, is the ratio of the A. momentum diffusivity to the mass diffusivity. B. thermal diffusivity to the mass diffusivity. C. momentum diffusivity to the thermal diffusivity. D. none of these.

A

A. momentum diffusivity to the mass diffusivity.

300
Q

If f is defined as above, then which of the following applies to a feed at dew point ? A. f = 1 B. f < 1 C. f > 1 D. 0 < f < 1

A

A. f = 1

301
Q

Perforated plate towers are unique for solvent extraction because, they provide A. higher contact area. B. better contact of the phase. C. repeated coalescence & redispersion of the drop phase. D. none of these.

A

C. repeated coalescence & redispersion of the drop phase.

302
Q

In case of absorption & stripping, the interface of the liquid & gas phases are present in equilibrium, when the diffusional resistance of __________ is zero. A. interface B. gas phase C. liquid phase D. all ‘a’, ‘b’ & ‘c’

A

A. interface

303
Q

Pick out the wrong statement pertaining to the analogy between equations of heat and mass transfer operations. A. Sherwood number in mass transfer is analogous to Nusselt number in heat transfer. B. Prandtl number in heat transfer is analogous to Schmidt number in mass transfer. C. Reynolds number in mass transfer is analogous to Grashoff number in heat transfer. D. Reynolds number remains the same in both heat and mass transfer.

A

C. Reynolds number in mass transfer is analogous to Grashoff number in heat transfer.

304
Q

The slope of the operating line for a single component co-current absorber when plotted in terms of mole ratio units is A. 0 B. ∞ C. (-) ve D. (+) ve

A

C. (-) ve

305
Q

The individual mass transfer co-efficients (moles/m2 . s) for absorption of a solute from a gas mixture into a liquid solvent are, KL = 4.5 and KG = 1.5. The slope of the equilibrium line is 3. Which of the following resistance (s) is (are) controlling? A. liquid side B. gas side C. interfacial D. both liquid and gas side

A

B. gas side

306
Q

Pore size of the molecular seive 5A is __________ mm. A. 5 B. 0.5 C. 0.05 D. 50

A

B. 0.5

307
Q

Swenson-Walker crystalliser is a __________ unit A. continuous B. batch C. semi-batch D. cooling (adiabatic)-cum-evaporation

A

A. continuous

308
Q

According to the Fenske equation, what will be the minimum number of plates required in a distillation column to separate an equimolar binary mixture of components A and B into an overhead fraction containing 99 mol% A and a bottom fraction containing 98 mol% B ? Assume that relative volatility (αAB = 2) does not change appreciably in the coloumn. A. 5 B. 9 C. 12 D. 28

A

C. 12

309
Q

Absorption (liquid-gas system) with evolution of heat as compared to isothermal absorption results in A. decreased solute solubility. B. large minimum liquid to gas (L/G) ratio. C. large number of trays. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

310
Q

With increase in temperature, the mutual solubility of two liquids A. increases B. decreases C. remains unchanged D. decreases exponentially

A

A. increases

311
Q

Pick out the wrong statement. A. In solvent extraction, the distribution co-efficient should be as large as possible for solvent economy. B. With increase in pressure, the solubility of gases in solvent increases at a fixed temperature. C. Decrease in Murphree plate efficiency is an indication of entrainment in distillation column. D. The capacity of a distillation coloumn is maximum at total reflux.

A

D. The capacity of a distillation coloumn is maximum at total reflux.

312
Q

The relative volatility of a binary mixture at the azeotropic composition is A. 1 B. > 1 C. 0 D. ∞

A

A. 1

313
Q

Relative volatility varies with the concentration of component for an ideal solution. The relative volatity of a binary mixture may be defined as the ratio of vapor pressure of component ‘A’ to that of component ‘B’, when A. only vapor phase follows Raoult’s law. B. only liquid phase obeys Dalton’s law. C. liquid phase obeys Dalton’s law and vapor phase obeys Raoult’s law. D. Vapor phase obeys Dalton’s law and liquid phase obeys Raoult’s law.

A

D. Vapor phase obeys Dalton’s law and liquid phase obeys Raoult’s law.

314
Q

Bound moisture is that liquid which exerts an equilibrium vapor pressure __________ that of the pure liquid at the given temperature. A. less than B. more than C. equal to D. either (o) or (b); depends on the solid

A

A. less than

315
Q

Lewis number (Le) is A. Sc / Pr B. Pr x St C. Sh x Pr D. St x Sh

A

A. Sc / Pr

316
Q

Which of the following is not a continuous leaching equipment? A. Pachuka tank B. Kennedy extractor C. Bollman extractor D. Hydrocyclones

A

A. Pachuka tank

317
Q

__________ extractor is used for the concentration of radioactive nuclear waste. A. Pulsed column B. Sieve plate C. Mixer-settler D. Ballman

A

A. Pulsed column

318
Q

Moisture content of a substance when at equilibrium with a given partial pressure of the vapour is called the __________ moisture. A. free B. unbound C. equilibrium D. bound

A

C. equilibrium

319
Q

All moisture in a non-hygroscopic material is the __________ moisture. A. free B. equilibrium C. unbound D. bound

A

C. unbound

320
Q

Pick out the correct relationship. (where, Ri = internal reflux ratio Ro = external reflux ratio.) A. (1 + Ro) = Ro/Ri B. (1 - Ro) = Ro/Ri C. (1 + Ri) = Ro/Ri D. (1 - Ri) = Ro/Ri

A

A. (1 + Ro) = Ro/Ri

321
Q

Separation of __________ employs gaseous diffusion process. A. N2 and O2 from air B. isotopes of uranium C. isotopes of helium D. SO2 and air

A

B. isotopes of uranium

322
Q

For water-ethanol system, the minimum reflux ratio A. is computed from the slope of the upper operating line that is tangent to the equilibrium curve. B. is computed from the intercept of the operating line. C. cannot be computed. D. is the optimum reflux ratio.

A

A. is computed from the slope of the upper operating line that is tangent to the equilibrium curve.

323
Q

The interfacial area per unit volume of dispersion, in a gas-liquid contactor, for fractional hold up of gas = 0.1 and gas bubble diameter = 0.5 mm is given by (in m2/m3) A. 500 B. 1200 C. 900 D. 800

A

A. 500

324
Q

Though, theoretically the adsorption & desorption isotherms is expected to coincide but sometimes at least a part of the isotherms does not coincide and this phenomenon is known as adsorption hysterisis. In such cases, the desorption equilibrium pressure is __________ that obtained for adsorption. A. lower than B. higher than C. same as D. either same or higher than

A

A. lower than

325
Q

Experimental determination of __________ is done by wetted wall column method. A. diffusion co-efficient B. mass transfer co-efficient C. NTU D. none of these

A

B. mass transfer co-efficient

326
Q

Pick out the wrong statement: A. Absorption factor is constant, when the equilibrium and operating lines are straight. B. In case of a stripper, the equilibrium curve is always below the operating line. C. In case of an absorber, the operating line is always above the equilibrium curve. D. In the absorption of low solubility gases, the liquid film is the controlling resistance.

A

B. In case of a stripper, the equilibrium curve is always below the operating line.

327
Q

In liquid extraction, if the selectivity is unity, then A. separation of the constituents is the most effective. B. no separation will occur. C. amount of solvent required will be minimum. D. solvent flow rate should be very low.

A

B. no separation will occur.

328
Q

Paper industry employs __________ driers. A. cylinder B. rotary C. spray D. fluidised bed

A

A. cylinder

329
Q

Which of the following has the same dimension as mass diffusivity? A. Momentum flux B. Kinematic viscosity C. Thermal diffusivity D. Both (b) and (c)

A

D. Both (b) and (c)

330
Q

Pick out the wrong statement pertaining to the cooling towers. A. In case of induced draft cooling tower, the fan is placed at the top of the tower. B. Effectiveness of forced draft cooling tower is reduced by the recirculation of the humid and hot discharged air. C. A natural draft cooling tower is recommended to be used, when the air humidity is low and air temperature is also low. D. Effectiveness of a mechanical draft cooling tower is reduced with increase in air wet-bulb temperature.

A

D. Effectiveness of a mechanical draft cooling tower is reduced with increase in air wet-bulb temperature.

331
Q

Experiments were conducted to determine the flux of a species A in a stagnant medium across a gas-liquid interface. The overall mass transfer co-efficient based on the liquid side for dilute systems for the above was estimated to be 4 x 10-3 kg mole/m2.s. The equilibrium data for the system is given as y = 2x. The flux across the interface (in kg mole/m2 .s) for bulk concentrations of A in gas phase and liquid phase as y = 0.4 and x = 0.01 respectively is A. 5.6 x 10-4 B. 8.5 x 10-4 C. 5.6 x 10-3 D. 8.5 x 10-3

A

B. 8.5 x 10-4

332
Q

Leaching of coarse solid lumps is also termed as A. decoction B. dissolution C. percolation D. agitation and settling

A

C. percolation

333
Q

The main reason for dividing a tall packed tower into series of small towers is to A. minimise the overall pressure drop. B. avoid flooding. C. reduce liquid hold up. D. avoid channeling.

A

D. avoid channeling.

334
Q

Co-current absorbers are usually used when the gas to be dissolved in the liquid is A. sparingly soluble B. highly soluble C. a pure substance D. a mixture

A

C. a pure substance

335
Q

At what percentage (by volume) of alcohol composition, it forms an azeotrope with water? A. 90 B. 91.5 C. 95 D. 99

A

C. 95

336
Q

Measurement of the interfacial area of mass transfer is achieved easily & accurately in case of a __________ coloumn. A. spray B. packed C. bubble cap plate D. wetted wall

A

D. wetted wall

337
Q

With the lowering of equiliDrium pressure, at a given temperature, the amount of ad-sorbate on the adsorbent A. increases. B. decreases. C. remains same. D. either (a) or (b), depends on the system.

A

B. decreases.

338
Q

Mass transfer co-efficient is defined as A. Flux = Co-efficient/concentration difference. B. Co-efficient = Flux/concentration difference. C. Flux=concentration difference/co-effi-cient. D. none of these.

A

B. Co-efficient = Flux/concentration difference.

339
Q

When an unsaturated air-water mixture is heated at constant pressure, then A. the partial pressure of water vapour increases. B. the specific humidity decreases. C. The relative humidity increases. D. the relative humidity decreases.

A

D. the relative humidity decreases.

340
Q

During sensible cooling process A. relative humidity decreases B. relative humidity increases C. wet bulb temperature decreases D. both (b) and (c)

A

D. both (b) and (c)

341
Q

At a fixed pressure, the humidity depends upon the partial pressure of vapor in the mixture. Humidity of a vapour free gas is __________ percent. A. 100 B. 0 C. 50 D. between 0 and 100

A

B. 0

342
Q

In case of physical adsorption, the difference between heat of adsorption and heat of normal condensation is A. equal to the heat of formation of surface compound. B. equal to the heat of wetting. C. zero. D. called integral heat of adsorption.

A

B. equal to the heat of wetting.

343
Q

Pick out the wrong statement: A. Change in barometric pressure does not affect the relative humidity. B. In case of a packed tower, the operating velocity is about half of the flooding velocity, generally. C. Elution’ means the desorption of the adsorbed solute by a solvent. D. The equilibrium moisture content of the solid can be reduced by increasing the absolute humidity.

A

D. The equilibrium moisture content of the solid can be reduced by increasing the absolute humidity.

344
Q

The value of L/mG ratio for economical absorption operation ranges from A. 0.5 to 0.8 B. 0.8 to 1.2 C. 1.25 to 2.0 D. 2.5 to 3.5

A

C. 1.25 to 2.0

345
Q

Large scale usage of flash distillation is practised in A. soap manufacturing B. ammonia synthesis plant C. polymerisation industry D. petroleum refinning

A

D. petroleum refinning

346
Q

High pressure at the bottom of a distillation tower handling heat sensitive materials results in A. thermal decomposition of bottoms. B. increased relative volatility. C. erosion of the tower. D. very efficient operation.

A

A. thermal decomposition of bottoms.

347
Q

Alcohol is dehydrated using __________ distillation. A. extractive B. azeotropic C. steam D. molecular

A

B. azeotropic

348
Q

Separation of two volatile liquids by distillation makes use of their A. selectivity B. relative volatility C. solubility D. density difference

A

B. relative volatility

349
Q

Which of the following increases during evaporative cooling process with recirculated water supply? A. Wet bulb temperature B. Relative humidity C. Partial pressure of vapour D. Both (b) and (c)

A

D. Both (b) and (c)

350
Q

Dried finished product sampled from various parts of a __________ dryer exhibits non-uniformity in the moisture content. A. rotary B. tray C. freeze D. none of these

A

B. tray

351
Q

__________ is used as an ‘entrainer’ for the separation of acetic acid-water mixture by distillation. A. Furfural B. Benzol C. Butyl acetate D. Hexane

A

C. Butyl acetate

352
Q

Rotary dryers cannot handle __________ materials. A. free flowing B. dry C. sticky D. granular

A

C. sticky

353
Q

Pick out the correct statement. A. Diffusivity decreases with increase in temperature. B. Diffusivity increases with increase in molecular weight. C. Diffusivity increases with the size of the individual molecule. D. none of these.

A

D. none of these.

354
Q

An example of elution is A. separation of uranium oxide from its ore by H2SO4 in a Pachuca tank. B. separation of sugar from sugar beet by hot water. C. dissolution of tannin out of tree barks by water. D. recovery of vegetable oils from seeds.

A

A. separation of uranium oxide from its ore by H2SO4 in a Pachuca tank.

355
Q

The operating line for an absorber is curved, when plotted in terms of A. mole fractions B. mole ratios C. partial pressure D. mass fractions

A

C. partial pressure

356
Q

Relative volatility does not change appreciably with the change in A. temperature B. vapour pressure of either component C. total pressure D. none of these

A

A. temperature

357
Q

Boiling point diagram is not affected by the ambient A. pressure B. humidity C. temperature D. both (b) and (c)

A

D. both (b) and (c)

358
Q

The dew point of a saturated gas phase equals the __________ temperature. A. gas B. room C. wet bulb D. none of these

A

A. gas

359
Q

A solid material shows case hardening properties while drying. Which of the following should be controlled to control the drying process? A. Flow rate of inlet air B. Relative humidity of outlet air C. Humidity of inlet air D. Temperature of the solid

A

D. Temperature of the solid

360
Q

In case of liquid-liquid binary diffusion, diffusivity of one constituent into another is not dependent on the A. temperature and pressure B. concentration C. nature of the constituents D. none of these

A

D. none of these

361
Q

For continuous drying of grannular or crystalline material, the dryer used is the __________ dryer. A. tunnel B. tray C. rotary D. none of these

A

C. rotary

362
Q

When adsorption hysteresis is observed, the desorption equilibrium pressure is __________ that obtained by adsorption. A. always lower than B. always higher than C. same as D. dependent on the system; can be either lower or higher than

A

A. always lower than

363
Q

Moisture in a substance exerting an equilibrium vapour pressure less than that of pure liquid at the same temperature is called the __________ moisture. A. bound B. unbound C. critical D. none of these

A

A. bound

364
Q

For a binary mixture with low relative volatility, continuous rectification to get pure products will require A. low reflux ratio B. less number of trays C. small cross-section column D. high reflux ratio

A

D. high reflux ratio

365
Q

The efficiency of a plate column will be maximum, when the flow is ideal __________ the plate. A. across B. above C. both (a) & (b) D. neither (a) nor (b)

A

C. both (a) & (b)

366
Q

Heat load in a cooling tower A. means the amount of heat thrown away (KCal/hr.) by the cooling tower. B. is equal to the number of kg, of water circulated times the cooling range. C. both (a) & (b). D. neither (a) nor (b).

A

C. both (a) & (b).

367
Q

In case of absorption with exothermic reaction, for fluids having A. Pr = Sc; percentage change in heat and mass transfer flux will be the same for a given change in the degree of turbulence. B. Pr = Sc = 1; total mass, momentum and thermal diffusivity will be the same. C. both (a) and (b) D. Pr = Sc ; there won’t be any change in heat and mass transfer flux with changes in degree of turbulence.

A

C. both (a) and (b)

368
Q

Detergent solution is dried to a powder in a A. spray dryer B. spouted bed dryer C. tunnel dryer D. pan open to atmosphere

A

A. spray dryer

369
Q

Which of the following mixtures does not form an azeotrope at atmosheric pressure? A. Water-alcohol B. Methyl alcohol-acetone C. Butyl acetate-water D. None of these

A

D. None of these

370
Q

During bottling of cold drinks (e.g. Pepsi), the main resistance to mass transfer for the absorption of carbon dioxide in water lies in the A. gas film B. liquid film C. liquid-gas interface D. none of these

A

B. liquid film

371
Q

The overall mass transfer co-efficient for the absorption of SO2 in air with dilute NaOH solution can be increased substantially by A. increasing the gas film co-efficient. B. increasing the liquid film co-efficient. C. increasing the total pressure. D. decreasing the total pressure.

A

A. increasing the gas film co-efficient.

372
Q

Flooding results in A. high tray efficiency B. low tray efficiency C. high gas velocity D. good contact between the fluids

A

B. low tray efficiency

373
Q

For the air water system under ambient conditions, the adiabatic saturation temperature and the wet bulb temperature are nearly equal, because A. water has a high latent heat of evaporation. B. Lewis number is close to unity. C. they are always equal under all circumstances. D. solubility of the components of air in water is very small.

A

A. water has a high latent heat of evaporation.

374
Q

In an operating distillation column, the A. vapors and liquids are at their dew point and bubble point respectively B. driving force for the liquid flow is its specific weight. C. driving force for the vapor flow is the pressure drop, as the pressure decreases gradually from the bottom to the top of the column. D. highest temperature is encountered at the top of the column.

A

C. driving force for the vapor flow is the pressure drop, as the pressure decreases gradually from the bottom to the top of the column.

375
Q

In a forced draft cooling tower, water is cooled from 95 to 80°F by exposure to air with a wet bulb temperature of 70°F. In this case, the A. range is 15°F. B. approach is 10°F. C. both (a) & (b). D. neither (a) nor (b).

A

C. both (a) & (b).

376
Q

The diffusivity (D) in a binary gas mixture is related to the temperature (T) as A. D ∝ T B. D ∝ T^0.5 C. D ∝ T^1.5 D. D ∝ T^2

A

C. D ∝ T^1.5

377
Q

For which of the following unit operations, Lewis number is of significance? A. Adsorption B. Binary distillation C. Gas absorption D. Humidification

A

D. Humidification

378
Q

Tray spacing in a distillation column of dia 10-12 ft. used in petroleum refinery may be around __________ inches. A. 5 B. 30 C. 60 D. 100

A

B. 30

379
Q

If a1 and a2 are the relative volatilities when the pressure in the distillation column is 1 and 2 atm respectively. Pick out the correct statement. A. a1 = a2 B. a1 = 2a2 C. a1 = 0.5 a2 D. none of these

A

D. none of these

380
Q

The dimension of diffusivity is same as that of the A. density B. molal concentration C. kinematic viscosity D. velocity head

A

C. kinematic viscosity

381
Q

The temperature to which a vapour gas mixture must be cooled (at varying humidity) to become saturated is called the __________ temperature. A. dew point B. wet bulb C. dry bulb D. none of these

A

D. none of these

382
Q

Entrainer used in azeotropic distillation should A. form a low boiling azeotrope with one of the constituents of the mixture. B. form a new azeotrope of low relative volatility with one of the constituents of the mixture. C. have high latent heat of vaporisation. D. have high viscosity to provide high tray efficiency.

A

A. form a low boiling azeotrope with one of the constituents of the mixture.

383
Q

In case of steam distillation, the steam leaving the liquid is not completely saturated with distillate vapour, because A. temperature is less. B. total pressure is less. C. mixing of steam with the material being vaporised is not so intimate as to result in equilibrium condition. D. saturated steam is used for steam distillation.

A

C. mixing of steam with the material being vaporised is not so intimate as to result in equilibrium condition.

384
Q

Pick out the wrong statement. A. The operating line always lies above the equilibrium solubility curve in case of a single component absorber. B. The operating line always lies below the equilibrium solubility curve in case of a single component stripper. C. The operating pressure in solvent extraction system should be below vapor pressures of all components. D. The solubility of a particular gas in ideal solution in any solvent is always the same.

A

C. The operating pressure in solvent extraction system should be below vapor pressures of all components.

385
Q

Leaching of coffee from coffee beans is done by A. hot water B. hexane C. lime water D. dilute H2SO4 (hot)

A

A. hot water

386
Q

For contacting a highly soluble gas with a liquid A. bubble the gas through liquid. B. spray the liquid on gas stream. C. either (a) or (b) would suffice. D. none of these.

A

A. bubble the gas through liquid.

387
Q

During drying operation, it is easier to remove the __________ moisture. A. equilibrium B. critical C. unbound D. bound

A

C. unbound

388
Q

With increase in solvent rate, the number of transfer units, NtoG, for a fixed degree of absorption from a fixed amount of gas A. increases B. decreases C. decreases linearly D. remains unaffected

A

B. decreases

389
Q

Ion exchange process is similar to A. absorption B. adsorption C. extraction D. leaching

A

B. adsorption

390
Q

A distillation column with N plates is being operated under normal conditions. At some point of time, the operation is shifted to total reflux condition (i.e., no product and residue are being withdrawn and feed to the column is stopped). At the new steady state, A. composition of vapors and that of liquid do not vary throughout the column. B. reboiler load and condenser load are minimum. C. the top and bottom compositions are unchanged with and without total reflux. D. the top and bottom compositions correspond to the maximum enrichment available.

A

D. the top and bottom compositions correspond to the maximum enrichment available.

391
Q

Dryer widely used in a textile industry is __________ dryer. A. festoon B. cylinder C. conveyor D. tunnel

A

C. conveyor

392
Q

Solvent used in extractive distillation A. changes the relative volatility of the original components. B. should be of high volatility. C. should form azeotropes with the original components. D. all (a), (b) and (c)

A

A. changes the relative volatility of the original components.

393
Q

Air at a particular humidity is heated in a furnace. The new dew point A. decreases B. increases C. depends on the extent of heating D. remain unchanged

A

B. increases

394
Q

In a packed tower, the value of HETP equals HTUOG, when the equilibrium and the operating lines are (where, HETP = height equivalant to a theoretical plate HTUOG = overall gas phase height of a transfer unit) A. straight B. parallel C. both (a) & (b) D. neither (a) nor (b)

A

C. both (a) & (b)

395
Q

The vapour pressure exerted by the moisture contained in a wet solid depends upon the A. nature of the moisture. B. temperature. C. nature of the solid. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

396
Q

The absorption factor is defined as (where, L = liquid flow rate, G = gas flow rate and, m = slope of the equilibrium line) A. L/mG B. G/mL C. mL/G D. LG/m

A

A. L/mG

397
Q

Smoke is an example of A. solid dispersed in liquid B. solid dispersed in gas C. liquid dispersed in gas D. gas dispersed in liquid

A

B. solid dispersed in gas

398
Q

Which of the following adsorbant is used in the refinning of sugar? A. Bone charcoal B. Wood charcoal C. Silica gel D. Activated clay

A

A. Bone charcoal

399
Q

Stacked packing compared to dumped packing A. provides poorer contact between the fluids. B. gives lower pressure drop. C. both (a) and (b). D. gives higher pressure drop.

A

C. both (a) and (b).

400
Q

In McCabe-Thiele method of theoretical plate calculation for a distillation column, the operating lines of stripping and rectifying sections coincide with the diagonal at __________ reflux. A. total B. minimum C. operating D. maximum permissible

A

A. total

401
Q

Which of the following parameters remains constant during chemical dehumidification? A. Dry bulb temperature B. Partial pressure of vapour C. Wet bulb temperature D. None of these

A

A. Dry bulb temperature

402
Q

Drying of a solid involves __________ transfer. A. only heat B. only mass C. both heat and mass D. none of these

A

C. both heat and mass

403
Q

Mechanism of moisture removal in case of freeze drying of food stuff is by A. evaporation B. sublimation C. dehydration D. adsorption

A

B. sublimation

404
Q

The dew point of an unsaturated gas-vapor mixture does not depend upon the __________ of the mixture. A. composition B. temperature C. total pressure D. all (a), (b) and (c)

A

B. temperature

405
Q

Which is not concerned directly with mass transfer? A. Schmidt number B. Sherwood number C. Lewis relationship D. Froude number

A

D. Froude number

406
Q

Removal of __________ exemplifies an adsorption unit operation. A. uranium from its ore B. water from petrol C. ammonia from coke oven gas D. mustard oil from mustard seed

A

B. water from petrol

407
Q

Can the efficiency of a plate in the distillation tower be greater than 100%? A. Yes B. Normally not; but is possible if infinite number of plates are put. C. Never D. Yes ; if the reflux ratio is maximum.

A

C. Never

408
Q

With increase in the mass velocity of the gas, the rate of drying during the constant rate period __________ , if the conduction and radiation through the solid are negligible. A. increases B. decreases C. remains same D. increases linearly

A

A. increases

409
Q

For gas absorption, low viscosity solvents are preferred, because of their A. better flow characteristics. B. low pumping pressure drop. C. rapid absorption rates. D. all (a), (b) and (c).

A

D. all (a), (b) and (c).

410
Q

To remove all the moisture from a wet solid it requires exposure to __________ air. A. perfectly dry B. highly humid C. high temperature D. none of these

A

A. perfectly dry

411
Q

The operating cost of a distillation column at minimum reflux ratio is A. minimum B. maximum C. infinite D. zero

A

A. minimum

412
Q

The reflux to a distillation column is 100 moles/hr, when the overhead product rate is 50 moles/hr. The reflux ratio is A. 2 B. 0.5 C. 50 D. 150

A

A. 2

413
Q

Molecular diffusivity of a liquid A. increases with temperature. B. decreases with temperature. C. may increase or decrease with temperature. D. is independent of temperature.

A

A. increases with temperature.

414
Q

The wet and ‘dry bulb temperature for a vapour-gas mixture are 25°C and 30°C respectively. If the mixture is heated to 45°C at constant pressure, the wet bulb temperature will be __________ °C. A. 25 B. > 25 C. < 25 D. -25

A

B. > 25

415
Q

Henry’s law states that the A. partial pressure of a component over a solution is proportional to its mole fraction in the liquid. B. partial pressure of a component over a solution is proportional to the mole fraction in the vapour. C. vapour pressure is equal to the product of the mole fraction and total pressure. D. partial pressure is equal to the product of the mole fraction and total pressure.

A

A. partial pressure of a component over a solution is proportional to its mole fraction in the liquid.

416
Q

Ammonia present in the coke oven gas is removed by washing with A. caustic solution B. dilute ammoniacal liquor C. dilute HCl D. ethanolamine

A

B. dilute ammoniacal liquor

417
Q

With increase in temperature, the leaching rate increases due to A. decreased liquid viscosity B. increased diffusivity C. both (a) and (b) D. neither (a) nor (b)

A

C. both (a) and (b)

418
Q

Which of the following processes is not an example of adsorption applied to gaseous separations? A. Recovery of valuable solvent vapors from dilute mixture with air and other gases. B. Dehumidification of air and gas. C. Removal of objectionable odour and impurities from industrial gases. D. Decolouration of yellow glycerene.

A

D. Decolouration of yellow glycerene.

419
Q

The critical moisture content in case of drying indicates the __________ rate period. A. beginning of falling B. beginning of constant C. end of falling D. none of these

A

A. beginning of falling

420
Q

Pick out the wrong statement A. A horizontal line on the humidity chart indicates the temperature changes at constant molal humidity. B. When water is cooled from 80 to 70°C by exposure to the air with a wet bulb temperature of 60°C, then both the approach & the range would be 10°C. C. For unsaturated air-water vapor mixture at atmospheric conditions, the wet bulb temperature & adiabatic cooling lines are the same. D. Relative saturation of unsaturated mixture of water vapor & air can not be increased by either reducing the mixture temperature or by increasing the total pressure.

A

D. Relative saturation of unsaturated mixture of water vapor & air can not be increased by either reducing the mixture temperature or by increasing the total pressure.

421
Q

According to Poiseuille’s law, the permeability for gas flow through a capillary is proportional to (where, μ = gas viscosity) A. μ B. 1/μ C. sqrt(μ) D. μ^2

A

B. 1/μ

422
Q

For a binary mixture distillation process, the degree of freedom is 2. However, if the pressure is fixed in this process, the number of independent variables in this process will be A. 1 B. 0 C. 2 D. 3

A

A. 1

423
Q

H2S is being absorbed in a gas absorber unit. The height of the transfer unit based on the overall mass transfer coefficient on the gas side is 0.4 m. The equilibrium data is given by, y = 1.5 x. The bulk concentration of H2S has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The height of the tower (in metres) corresponding to an operating line given by, y = 5x + 0.001 is A. 2 B. 1.56 C. 1 D. 0.56

A

A. 2

424
Q

Packed column distillation is limited to the column __________ metres. A. height < 6 B. diameter < 0.6 C. both (a) & (b) D. neither (a) nor (b).

A

C. both (a) & (b)

425
Q

For the flow of gases through a capillary, with increase in temperature, the permeability __________ as per Knudsen law. A. increases B. decreases C. remains same D. either (a) or (b); depends on the gas

A

A. increases

426
Q

Which of the following is directly concerned with psychrometry? A. Lewis relationship B. Galileo number C. Weber number D. Dean number

A

A. Lewis relationship

427
Q

Plate efficiency in a distillation column is reduced due to the __________ of liquid. A. entrainment B. foaming C. weeping & dumping D. all (a), (b) & (c)

A

D. all (a), (b) & (c)

428
Q

The most efficient cooling tower out of the following is A. induced draft B. forced draft C. natural draft D. atmospheric

A

A. induced draft

429
Q

Sodium bicarbonate is produced during soda ash manufacture using a __________ tower. A. plate B. baffle C. packed D. none of these

A

B. baffle

430
Q

Powdery materials can be guarded against caking tendency on storage by A. providing irregular grain size. B. providing minimum percentage of voids. C. having maximum possible points of contact. D. none of these.

A

D. none of these.

431
Q

In case of cooling towers, the ratio of the rates of heat and mass transfer is indicated by the __________ number. A. Lewis B. Grashoff C. Sherwood D. none of these

A

A. Lewis

432
Q

Which one of the following devices is not used for both the absorption as well as the liquid-liquid extraction processes? A. Packed towers B. Plate towers C. Spray towers D. Wetted wall columns

A

D. Wetted wall columns

433
Q

The temperature of water cooled in cooling tower is always __________ temperature of entering air. A. more than the wet bulb B. less than the wet bulb C. equal to the wet bulb D. equal to the dry bulb

A

A. more than the wet bulb

434
Q

Which of the following processes is followed by unsaturated air (with dry bulb temperature 12°C and relative humidity 47%) passing through water spray washer (temperature of water being constant at 40°C? A. Humidification only B. Heating only C. Both heating and humidification D. Evaporative cooling

A

C. Both heating and humidification

435
Q

Mass transfer co-efficient is directly proportional to DAB according to the __________ theory. A. film B. penetration C. surface-renewal D. none of these

A

A. film

436
Q

The relative volatility of a binary mixture at constant temperature __________ the total pressure. A. decreases with increase in B. increases with increase in C. is independent of D. none of these

A

A. decreases with increase in

437
Q

Tower diameter may be decreased by A. using higher reflux ratio. B. use of increased tray spacing. C. increasing the liquid flow rate. D. increasing the vapour flow rate.

A

B. use of increased tray spacing.

438
Q

Rayleigh’s equation applies to __________ distillation. A. continuous B. steam C. differential D. flash

A

C. differential

439
Q

Steady state equimolal counter diffusion is encountered in A. separation of a binary mixture by distillation. B. absorption of NH3 from air by water. C. all liquid-liquid diffusion systems. D. all liquid-solid diffusion systems.

A

A. separation of a binary mixture by distillation.

440
Q

Which of the following is considered equivalent to one theoretical stage in Mc-Cabe Thiele’s method? A. Partial condenser B. Total condenser C. Reboiler D. Both (b) and (c)

A

D. Both (b) and (c)

441
Q

Polar organic compounds are normally used as separating agents for the azeotropic and extractive distillation. Which of the following is the most important factor to be considered for the choice of the separating agent for extractive distillation? A. Cost B. Availability C. Toxicity D. Selectivity

A

D. Selectivity

442
Q

As the reflux ratio increases, the slope of the operating line for rectifying section A. increases B. decreases C. remains constant D. data insufficient, cannot be predicted

A

A. increases

443
Q

Cox chart, which is useful in the design of distillation column particularly for petroleum hydrocarbons, is a plot of (where, P = vapor pressure, T = temperature) A. log P vs . T B. log P vs. log T C. T vs. P D. P vs . log T

A

A. log P vs . T

444
Q

The unit of volumetric diffusivity is A. cm2/sec B. cm/sec C. cm3/sec D. cm2/sec2

A

A. cm2/sec

445
Q

For a ternery mixture, in which equilateral triangular co-ordinate is used in leaching and extraction, a __________ of the equilateral triangular co-ordinates. A. binary mixture is represented by the apex B. binary mixture is represented by any point inside C. ternery mixture is represented by the sides D. pure component is represented by the apex.

A

D. pure component is represented by the apex.

446
Q

Steady state temperature reached by a small amount of liquid evaporating into a large amount of unsaturated vapour-gas mixture is called the __________ temperature. A. dry-bulb B. wet-bulb C. dew point D. adiabatic saturation

A

B. wet-bulb

447
Q

The Reynolds number of the liquid was increased 100 fold for a laminar falling film used for gas-liquid contacting. Assuming penetrating theory is applicable, the fold increase in the mass transfer co-efficient (Kc) for the same sytem is A. 100 B. 10 C. 5 D. 1

A

B. 10

448
Q

The slope of 9-line is determined by the A. reflux ratio B. plate efficiency to be achieved C. thermal condition of the feed D. relative volatility.

A

C. thermal condition of the feed

449
Q

In steam distillation, the A. temperature is 100°C. B. temperature is more than 100° C. C. product must be immiscible with water. D. temperature is higher than the boiling point of either component.

A

C. product must be immiscible with water.

450
Q

Which of the following can be calculated theoretically using steam table and Dalton’s law of partial pressure; if the relative humidity and dry bulb temperature of moist air is known? A. Dew point B. Humidity ratio C. Wet bulb temperature D. None of these

A

C. Wet bulb temperature

451
Q

Steam distillation is used for separation of high boiling A. substances from non-volatile impurities. B. volatile impurity from still higher boiling substances. C. both (a) and (b). D. neither (a) nor (b).

A

C. both (a) and (b).

452
Q

The feed to fractionating column is changed from saturated vapour to saturated liquid. If the separation and reflux ratio remains unchanged, the number of ideal stages will A. increase B. decrease C. remains same D. depend on saturated boiling point; may increase or decrease

A

A. increase

453
Q

Rose oil is extracted from rose leaves using __________ distillation. A. high pressure B. low pressure C. extractive D. steam

A

D. steam

454
Q

Hypersorption refers to a __________ process. A. fixed bed absorption B. moving bed absorption C. fixed bed adsorption D. moving bed adsorption

A

D. moving bed adsorption

455
Q

Which of the following is the correct ternery diagram for liquid-liquid extraction system comprising of two pairs partly soluble (e.g., chlorobenzene-water-methyl ethyl ketone system)? A. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-500-1.png B. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-500-2.png C. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-500-3.png D. None of these.

A

A. https://www.indiabix.com/_files/images/chemical-engineering/mass-transfer/317-500-1.png

456
Q

Extraction of coffee from its seed is done by A. liquid-liquid extraction. B. leaching. C. extractive distillation. D. steam distillation.

A

B. leaching.

457
Q

In azeotropic mixture, the equilibrium vapour composition is A. more than liquid composition. B. less than liquid composition. C. same as liquid composition. D. independent of pressure.

A

C. same as liquid composition.

458
Q

With lapse of time, the overhead composition of light component in case of batch distillation with constant reflux A. increases B. decreases C. remains same D. may increase or decrease ; depends on system.

A

B. decreases

459
Q

Lewis number, which is important in problems involving simultaneous heat and mass transfer, is the ratio of A. mass diffusivity to momentum diffusivity. B. thermal diffusivity to mass diffusivity. C. momentum diffusivity to thermal diffusivity. D. none of these.

A

B. thermal diffusivity to mass diffusivity.

460
Q

According to the film theory of mass transfer, the mass transfer co-efficient is proportional to (where, D = molecular diffusivity) A. D B. D^2 C. D^0.5 D. 1/D

A

A. D

461
Q

Dry bulb temperature of the gas is __________ the wet bulb temperature. A. less than B. more than C. equal to D. none of these

A

B. more than

462
Q

Decoction refers to the use of solvent A. at ambient temperature B. at its boiling point C. in its vapor form D. none of these

A

B. at its boiling point

463
Q

Flash distillation is suitable for separating the constituents of a binary system, which A. form minimum boiling azeotrope. B. have very wide boiling points. C. have very close boiling points. D. form constant boiling azeotrope.

A

B. have very wide boiling points.

464
Q

The ratio of Murphree plate efficiency to point efficiency is 1 in a __________ flow model. A. plug B. perfectly mixed C. both (a) & (b) D. neither (a) nor (b)

A

B. perfectly mixed

465
Q

The rough value of diffusion co-efficient of water vapor into air at 25°C may be about __________ cm2/sec. A. 0.25 B. 2.5 C. 1.25 D. 0.0025

A

A. 0.25

466
Q

Flooding in a column results due to A. high pressure drop B. low pressure drop C. low velocity of the liquid D. high temperature

A

A. high pressure drop

467
Q

Which of the following gas-liquid contacting devices incurs the least pressure drop for a particular duty? A. Grid tray tower B. Perforated tray tower C. Wetted wall tower D. Bubble cap tower

A

C. Wetted wall tower

468
Q

A liquid mixture contains 30% o-xylene, 60% p-xylene and 10%. m-xylene (all percentages in w/w). Which of the following statements would be true in respect of this mixture? A. The mixture exhibits an azeotrope at 101.3 kPa. B. The composition of the mixture, in percent by volume is: o-xylene 30, p-xylene 60. and m-xylene 10. C. The composition of the mixture in mole percent is: o-xylene 30, p-xylene 60 and m-xyoene 10. D. The mixture contain optical isomers.

A

A. The mixture exhibits an azeotrope at 101.3 kPa.

469
Q

Unsaturated air (with dry bulb temperature and dew point being 35°C and 18°C respectively) is passed through a water spray chamber maintained at 15°C. The air will be cooled A. and humidified. B. and dehumidified with increase in wet bulb temperature. C. at the same relative humidity. D. and dehumidified with decrease in wet bulb temperature.

A

D. and dehumidified with decrease in wet bulb temperature.

470
Q

The process employing desorption of the absorbed solute by a solvent is called A. elution B. osmosis C. reverse osmosis D. sublimation

A

A. elution

471
Q

If the overall efficiency and Murphree plate efficiency are equal, then both the equilibrium and operating lines are A. straight B. parallel C. both (a) & (b) D. neither (a) nor (b)

A

C. both (a) & (b)

472
Q

Which of the following operations does not involve leaching? A. Dissolving gold from ores. B. Dissolving pharmaceutical products from bark or roots. C. Dissolving sugar from the cells of the beet. D. Removing nicotine from its water solution by kerosene.

A

D. Removing nicotine from its water solution by kerosene.

473
Q

The recovery of pencillin from the acidified fermentation broth is done by A. distillation B. evaporation C. absorption D. liquid extraction

A

D. liquid extraction

474
Q

Unit operation involved in the prilling of urea is A. evaporation B. drying C. crystallisation D. both (b) and (c)

A

D. both (b) and (c)

475
Q

Molecular seives are porous A. alumina. B. silica. C. synthetic zeolites crystals/metal alumino-silicates. D. none of these.

A

C. synthetic zeolites crystals/metal alumino-silicates.

476
Q

Calcium ammonium nitrate (a fertiliser) is dried in a __________ dryer. A. rotary B. vacuum C. tunnel D. tray

A

A. rotary

477
Q

A binary mixture of benzene and cyclohexane is separated by A. flash vaporisation B. extractive distillation C. solvent extraction D. ordinary distillation

A

B. extractive distillation

478
Q

Component A is diffusing in a medium B. The flux NA relative to a stationary point is equal to the flux due to molecular difusion, if A. mass transfer is accompanied by reaction. B. diffusion of A is in stagnant medium B. C. molecular mean free path is high. D. there is equimolar counter diffusion.

A

D. there is equimolar counter diffusion.

479
Q

Cox chart is useful in the design of A. distillation column B. evaporator C. dryer D. crystalliser

A

A. distillation column

480
Q

Dew point of an air-water vapor mixture A. decreases with decrease in pressure. B. at constant humidity & total pressure is fixed. C. corresponding to any point on the humidity chart is obtained by projecting a line through this point parallel to the temperature axis and to the saturation curve. D. all ‘a’, ‘b’ & ‘c’.

A

D. all ‘a’, ‘b’ & ‘c’.

481
Q

Can a cooling tower cool water below the wet bulb temperature of inlet air? A. yes B. no C. yes ; but height of cooling tower will be prohibitively high. D. yes ; but the air flow rate should be excessively high.

A

B. no

482
Q

The solvent used in liquid-liquid extraction should have __________ less than one. A. selectivity B. distribution co-efficient C. both (a) and (b) D. neither (a) nor (b).

A

D. neither (a) nor (b).

483
Q

The suitable evaporator for concentration of foaming liquids is a __________ evaporator. A. long tube B. short tube C. vacuum D. falling film

A

A. long tube

484
Q

The ratio of Murphree plate efficiency to point efficiency is always > 1 in a __________ flow model. A. plug B. perfectly mixed C. both (a) & (b) D. neither (a) nor (b)

A

A. plug

485
Q

Tea percolation employs A. liquid-liquid extraction B. leaching C. absorption D. none of these

A

B. leaching

486
Q

Which of the following assumes constant molal vaporisation and overflow? A. McCabe-Thiele method B. Ponchan-Savarit method C. Enthalpy concentration method D. Plate absorption column

A

A. McCabe-Thiele method

487
Q

Absorption factor, for a fixed degree of absorption from a fixed amount of gas should be A. 1 B. > 1 C. < 1 D. ≤ 1

A

B. > 1

488
Q

Selectivity of the solvent used in solvent extraction should be A. 1 B. > 1 C. < 1 D. 0

A

B. > 1

489
Q

Pick out the wrong statement pertaining to leaching. A. Fine solids can not be leached in a Pachuka tank. B. Door classifier can be used for leaching of coarse solids. C. Vegetable seeds can be leached in either of Bollman extractor, Rotocel or Kennedy extractor. D. Very high temperature is not needed for the leaching of sugar beet.

A

A. Fine solids can not be leached in a Pachuka tank.

490
Q

Wet bulb and dry bulb temperatures becomes identical at __________ percent saturation curve. A. 100 B. 50 C. 78 D. none of these

A

A. 100

491
Q

NSc/NPr is called the A. psychrometric ratio B. Lewis number C. Sherwood number D. Stantan number

A

B. Lewis number

492
Q

McCabe-Thiele method 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 Ponchan-Savarit method.

A

A. uses molal units for material and energy balance.

493
Q

The film penetration model of mass transfer was enunciated by A. Gilliland B. Toor and Marchello C. Stefan D. Fick

A

B. Toor and Marchello

494
Q

The most economical range of absorption factor is A. 0 to 0.5 B. 0 to 3 C. 1.25 to 2 D. 5 to 15

A

C. 1.25 to 2

495
Q

Channelling is most severe A. in towers packed with stacked packing. B. in towers packed randomly with crushed solids. C. in dumped packing of regular units. D. at very high liquid flow rate.

A

A. in towers packed with stacked packing.

496
Q

Out of two equilibrium curves, first one lies above the diagonal and the second lies below the diagonal in the x-y plot. It means that separation by distillation is A. not possible in the second case unless vacuum is applied. B. not possible in the second case unless high pressure is applied. C. more readily done in the second case compared to first one. D. none of these

A

C. more readily done in the second case compared to first one.

497
Q

ADDUCTS’ and ‘CLATHRATES’ are used in case of A. extractive distillation. B. crystallisation. C. absorption. D. none of these.

A

B. crystallisation.

498
Q

Adsorption is an unit operation which generally involves __________ systems. A. liquid-solid B. gas-solid C. fluid-solid D. solid-solid

A

C. fluid-solid

499
Q

In case of __________ distillation, a solvent is added to alter the relative volatility of the mixture to be separated. A. molecular B. azeotropic C. extractive D. flash.

A

C. extractive

500
Q

Separation of the isotopes of helium for scientific investigations is done by A. reverse osmosis B. thermal diffusion C. leaching D. solvent extraction

A

B. thermal diffusion