Mass Transfer Flashcards

1
Q

Mass transfer rate between two fluid phases does not necessarily depend on the __________ of the two phases.

chemical properties
physical properties
degree of turbulence
interfacial area

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

0.50
0.60
2
1

A

0.50

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3
Q

Fenske equation determines the

maximum number of ideal plates.
height of the distillation column.
minimum number of theoretical plates.
optimum reflux ratio.

A

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

cold water leaving the tower and the wet bulb temperature of the surrounding air.
hot water entering the tower and the wet bulb temperature of the surrounding air.
hot water entering the tower and the cooled water leaving the tower.
none of these

A

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 ?

Mixer-settler extractor
Centrifugal extractor
Pulsed extractor
Packed extraction tower

A

Centrifugal extractor

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6
Q

Total reflux in a distillation operation requires minimum

reboiler load
number of plates
condenser load
all (a), (b) and (c)

A

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

raising the temperature.
lowering the total pressure.
both (a) and (b).
neither (a) nor (b).

A

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

+ve
-ve
zero
none of these

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

relative volatility is reasonably constant.
mixture (to be separated) shows negative deviation from ideality.
mixture (to be separated) shows positive deviation from ideality.
multicomponent distillation is involved.

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.

natural
forced
induced
none of these

A

natural

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11
Q

Pick out the correct statement.

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

A

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

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12
Q

__________ columns are used for liquid dispersion in a continuous gas phase.

Packed
Pulse
Bubble cap
Sieve plate

A

Packed

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13
Q

Overall efficiency of the distillation column is

the ratio of number of ideal plates to actual plates.
the ratio of number of actual plates to ideal plates.
same as the Murphree efficiency.
always more than the point efficiency.

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.

boiling point
freezing point
vapour pressure
both (b) and (c)

A

both (b) and (c)

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15
Q

Which is the controlling factor for a drum drier?

Diffusion
Heat transfer
Both (a) and (b)
Neither (a) nor (b)

A

Heat transfer

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16
Q

Drying operation under vacuum is carried out to

dry those materials which have very high unbound mositure content.
reduce drying temperature.
increase drying temperature.
dry materials having high bound moisture content.

A

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

higher dew point.
higher absolute (specific) humidity.
higher relative humidity
higher wet bulb temperature.

A

higher relative humidity

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18
Q

Separation of two or more components of a liquid solution can not be achieved by

fractional crystallisation
liquid extraction
absorption
evaporation

A

absorption

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19
Q

Stefan’s law describes the mass transfer by

diffusion
bulk flow
both ‘a’ & ‘b’
neither ‘a’ nor ‘b’

A

both ‘a’ & ‘b’

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20
Q

At minimum reflux ratio for a given separation

number of plates is zero.
number of plates is infinity.
minimum number of the theoretical plates is required.
separation is most efficient.

A

number of plates is infinity.

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21
Q

Relative humidity is the ratio of the

partial pressure of the vapour to the vapour pressure of the liquid at room temperature.
partial pressure of the vapour to the vapour pressure of the liquid at gas temperature.
actual humidity to saturation humidity.
none of these

A

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.

increases
decreases
does not vary
may increase on decrease, depends on the system.

A

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.

electrical resistance
thermal conductivity
strength
none of these.

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

latent heat
humid heat
specific heat
sensible heat

A

specific heat

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25
Q

To increase the absorption factor, (where, G = gas flow rate, S = solvent flow rate)

increase both ‘G’ and ‘S’.
decrease both ‘G’ and ‘S’.
increase ‘S’ and decrease ‘G’.
increase ‘G’ and decrease ‘S’

A

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 = __________

1
0.5
10
0

A

1

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27
Q

Dew point of a gas-vapour mixture

increases with temperature rise.
decreases with temperature rise.
decreases with decrease in pressure.
increases with increase in pressure.

A

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.

increases with increase in
is one at unity value of
both (a) and (b)
neither (a) nor (b)

A

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 ?

Lewis number
Schmidt number
Prandtl number
Sherwood number

A

Lewis number

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30
Q

In case of an absorber, the operating

line always lies above the equilibrium curve.
line always lies below the equilibrium curve.
line can be either above or below the equilibrium curve.
velocity is more than the loading velocity.

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

slope of the operating line in stripping section decreases.
number of plates decreases very slowly first and then more and more rapidly.
total cost first decreases and then increases.
liquid flow increases while the vapor flow decreases for a system.

A

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)

S2/S1
S1/S2
S1 - S2
S1 x S2

A

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 two pairs of partially miscible liquids ?

0
1
2
3

A

0

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34
Q

Which of the following remains constant during sensible cooling process ?

Specific humidity
Partial pressure of vapour
Both (a) and (b)
Neither (a) nor (b)

A

Both (a) and (b)

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35
Q

Physical absorption is

an irreversible phenomenon.
a reversible phenomenon.
accompanied by evolution of heat.
both (b) and (c)

A

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

evaporation
drift
blowdown and leakage
all (a), (b) and (c)

A

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 ?

Heat gain or loss
Flow rate of entering liquid
Flow rate of gas
None of these

A

Flow rate of entering liquid

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38
Q

Mass transfer co-efficient of liquid is

affected more by temperature than that for gases.
affected much less by temperature than that for gases.
not affected by the temperature.
none of these.

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

ammonia in water.
benzol present in coke oven gas by wash oil.
SO2 in alkaline solution.
all (a), (b) and (c).

A

SO2 in alkaline solution.

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40
Q

Which of the following unit operations makes use of Thiele-Geddes equation ?

Liquid-liquid extraction
Solid-liquid extraction
Multicomponent absorption with chemical reaction
Multicomponent distillation.

A

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 ?

Sieve plate column
Bubble cap column
Randomly packed column
Wetted wall column

A

Wetted wall column

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42
Q

The equipment frequently used for adiabatic humidification-cooling operation with recirculating liquid is

natural draft cooling tower
induced draft cooling tower
spray chamber
none of these

A

spray chamber

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43
Q

Chemisorption (chemical adsorption) is

same as “Van der Waals” adsorption.
characterised by adsorption of heat.
an irreversible phenomenon.
a reversible phenomenon.

A

an irreversible phenomenon.

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44
Q

The rate of solid-liquid extraction is limited by the

phase change of the solute as it dissolves in the solvent.
diffusion of the solute through the solvent in the pores to the outside of the particle.
diffusion of the solute from the solution in contact with the particle to the main bulk of the solution.
all ‘a’, ‘b’ & ‘c’.

A

all ‘a’, ‘b’ & ‘c’.

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45
Q

Raoult’s law applies to the

all liquid solutions
non-ideal solution only.
non-volatile solute.
solvents.

A

solvents.

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46
Q

In distillation columns, the number of bubble caps per tray primarily depends upon the

allowable liquid velocity.
allowable gas velocity.
allowable gas and liquid velocities.
feed composition.

A

allowable gas and liquid velocities.

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47
Q

In distillation, overhead product contains

only one component
two components
any number of components
only saturated liquid

A

any number of components

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48
Q

With increase in pressure, the relative volatility for a binary system

increases.
decreases.
remains same.
either (a) or (b), depends on the system.

A

decreases.

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49
Q

Low viscosity absorbent is preferred for reasons of

rapid absorption rates and good heat transfer characteristics.
improved flooding characteristics.
low pressure drop on pumping.
all (a), (b) and (c).

A

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

K ∝ D
K ∝ √D
K ∝ D^1.5
K ∝ D^2

A

K ∝ D

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51
Q

The McCabe Δ L law states that the

molar heats of vaporisation of components are nearly equal.
linear crystal growth rate depends on the degree of supersaturation.
linear crystal growth rate does not depend on the crystal size.
linear crystal growth rate depends on the crystal size.

A

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

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52
Q

Bollman extractor

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

A

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 __________ transfer is same.

heat and mass
mass and momentum
heat and momentum
heat, momentum and mass

A

heat and mass

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54
Q

A coalescer in a mixer-settler liquid-liquid extraction coloumn

comprises of thin bed of substances of extended surface having high porosity.
helps in increasing the bubble size entering the settler.
helps in increasing the settling rate of the bubbles.
all ‘a’, ‘b’, & ‘c’.

A

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

increase
decrease
remain same
data insufficient, can’t be predicted

A

increase

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56
Q

Pick out the correct statement.

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.
A sharp decrease in pressure drop is an indication of flooding in a distillation coloumn.
Solvent used in extractive distillation should be of high volatility.
Flash distillation is suitable for separating components which have very close boiling temperature.

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

vapour pressure of component A to that of component B.
vapour pressure of component A to the total pressure.
vapour pressure of component A to the partial pressure of A.
partial pressure of component A to the total pressure.

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

decoction
percolation
elutriation or elution
none of these

A

none of these

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59
Q

In the constant rate period of the rate of drying curve for batch drying,

cracks develop on the surface of the solid.
rate of drying decreases abruptly.
surface evaporation of unbound moisture occurs.
none of these.

A

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%).

15 min
51 min
71 min
94 min

A

71 min

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61
Q

Agitator is provided in a crystalliser for

avoiding deposition on cooler surfaces.
formation of nuclei.
crystal growth.
all (a), (b) and (c).

A

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

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62
Q

__________ diffusion is used for separating the isotopes of methane.

Thermal
Pressure
Concentration
Force

A

Thermal

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63
Q

Ordinary diffusion process is also called __________ diffusion.

pressure
thermal
concentration
forced.

A

concentration

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64
Q

Pick out the wrong statement.

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

A

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.

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.
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.
Rotary dryer is suitable for drying sticky material.
Recommended peripherial speed of a rotary drier is in the range of 10 to 30 metres/minute.

A

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

low pressure drop and high hold up.
high pressure drop and low hold up.
low pressure drop and low hold up.
high pressure drop and high hold up.

A

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.

100
> 100
< 100
none of these

A

> 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

25%
50%
70%
90%

A

50%

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69
Q

Raoult’s law is applicable to the

ideal solutions
real solutions
mixture of water and alcohol
non-ideal gases

A

ideal solutions

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70
Q

Weeping in a distillation column

increases tray efficiency.
provides large interfacial surface for mass transfer.
results due to very high gas velocity.
results due to very low gas velocity.

A

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

area between operating line and 45° diagonal x-y diagram.
condenser and reboiler surfaces.
tower cross-section.
none of these.

A

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

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72
Q

Wetted wall tower experiment determines the

molal diffusivity.
volumetric co-efficient.
mass transfer co-efficient.
none of these.

A

mass transfer co-efficient.

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73
Q

In McCabe-Thiele method, at infinite reflux ratio

the overhead product is minimum.
both the operating lines coincide with diagonal.
both (a) and (b).
neither (a) nor (b).

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

increases
decreases
remains same
may increase or decrease ; depends on individual design

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

packing may be crushed due to thermal expansion/contraction of the components of the equipments.
pressure drop in the equipment will be very high.
viscosity variation of the fluids may cause channeling/flooding.
none of these.

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

more
less
same
either more or less; depends on the system

A

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.

wetted wall
bubble cap
perforated tray
packed

A

wetted wall

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78
Q

Pick out the system with minimum boiling azeotrope at 1 atm.

benzene-toluene
ethyl alcohol-water
hydrochloric acid-water
all (a), (b) and (c)

A

ethyl alcohol-water

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79
Q

Free flowing granular materials can be best dried in a __________ drier.

rotary
cylinder
drum
freeze

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,

inversely
linearly
exponentially
none of these

A

linearly

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81
Q

Corresponding to Nusselt number in heat transfer, the dimensionless group in mass transfer is the __________ number.

Sherwood
Schmidt
Peclet
Stanton

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

0.31
0.107
0.017
0.215

A

0.215

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83
Q

Liquid diffusivity is of the order of __________ cm^2 /second.

0.01
0.1
10^-5 to 10^-6
> 1

A

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

the pressure drop and hence the pumping cost will be very high.
it cannot be recovered by distillation.
its recovery cost by distillation may be prohibitatively high.
it will decompose while recovering by distillation.

A

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.

is greater than
is lower than
is same as
cannot be predicted as data are insufficient

A

is greater than

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86
Q

Molarity is defined as the number of gm moles of solute per __________ of solvent.

litre
kg
gm
c.c

A

litre

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87
Q

The value of Lewis number (Le = Sc/Pr) for air-water vapour system is around

1
0.24
3.97
600

A

1

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88
Q

Which of the following T-H diagram is valid for dehumidification operation ?

(insert graph here)
(insert graph here)
(insert graph here)
(insert graph here)

A

(insert graph here)

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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)

less number of trays are required.
composition of the residue remains unchanged.
more number of trays are required but the residue composition remains unchanged.
more number of trays are required and the residue composition is more dilute in methanol.

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.

exponential
parabolic
linear
cubic

A

exponential

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91
Q

Which of the following binary systems is an example of a maximum boiling azeotrope ?

Water-hydrochloric acid.
Acetone-carbon disulphide.
Water-ethyl alcohol.
n-heptane-n-octane.

A

Water-hydrochloric acid.

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92
Q

(NRe . NSc) is termed in mass transfer operation as the __________ number.

Stanton
Sherwood
Peclet
none of these

A

Peclet

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93
Q

The binary diffusivity in gases and liquids vary respectively as

T^3/2 and T
T and T^3/2
(T)^1/2 and T^3/2/
T^3/2 and (T)^1/2

A

T^3/2 and T

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94
Q

Pick out the correct statement.

The slope of the stripping line is always less than unity.
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.
In Ponchon-Savarit method of no. of theoretical plate determination, the stripping and rectifying operating lines are vertical at total reflux.
Kremsor-Brown-Souder’s equation is used to calculate the efficiency of a plate tower.

A

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.

Dialysis process is used for the production of fresh water from brine.
Electrodylsis is used in the manufacture of NaOH.
Electrodylsis is used for the refin-ning/purification of petrol.
both (b) and (c).

A

Electrodylsis is used in the manufacture of NaOH.

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96
Q

Pick out the correct statement.

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

A

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

reduce the overall pressure drop
avoid channelling
reduce liquid hold-up
avoid flooding

A

avoid channelling

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98
Q

Moisture contained by a substance in excess of the equilibrium moisture is called the __________ moisture.

unbound
free
critical
bound

A

free

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99
Q

With increase in temperature, the solubility of gases in liquids, at fixed pressure

increases
decreases
remains same
either (a) or (b), depends on the system

A

decreases

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100
Q

In most of the vacuum crystalliser, vacuum is generally produced by means of a

suction pump
compressed air jet
steam jet ejector with a barometric condenser
none of these

A

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

greater degree of separation with a fixed number of trays
increased reboiler load
increased reflux ratio
None of these.

A

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.

Watted wall
Packed
Plate
Spray

A

Plate

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103
Q

Deairation (removal of O2) of water is done by

rectification
absorption
ion-exchange
adsorption

A

ion-exchange

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104
Q

Make up water is supplied during cooling tower operation to compensate for water losses due to

evaporation
blowdown
entrainment
all (a), (b)&(c)

A

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

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105
Q

Pick out the wrong statement.

The mole fraction of solute is directly proportional to the molality of a ‘dilute’ solution.
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.
Azeotropes obey Raoult’s law at all temperature.
The relative volatility of a binary mixture at the azeotropic composition is 1.

A

Azeotropes obey Raoult’s law at all temperature.

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106
Q

A minimum boiling azeotrope is exemplified by

toluene-benzene
acetone-carbon disulphide
water-isobutyl alcohol
none of these

A

acetone-carbon disulphide

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107
Q

Which of the following solutions will follow Raoult’s law most closely ?

A solution of benzene, toluene and oxylene.
35% solution of camphor in water.
35% solution of NH3 in water.
A solution of polar organic compounds (not of homologs of a series).

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)

increases pressure drop, increases surface area.
increases pressure drop, decreases surface area.
decreases pressure drop, increases surface area.
decreases pressure drop, decreases surface area.

A

decreases pressure drop, increases surface area.

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109
Q

Critical humidity of a solid salt means the humidity

above which it will always become damp.
below which it will always stay dry.
both (a) and (b).
above Which it will always become dry and below which it will always stay damp.

A

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

parallel
straight
both parallel and straight
neither parallel nor straight

A

both parallel and straight

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111
Q

As complete saturation of an adsorbent is approached, the differential heat of adsorption approaches

that of normal condensation.
integral heat of adsorption.
zero.
none of these.

A

that of normal condensation.

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112
Q

‘Absorption with chemical reaction’ is involved in the removal of

carbon dioxide from gaseous stream using alkaline solution.
benzol from coke oven gas using solar oil/wash oil.
ammonia from coke oven gas using refrigerated water.
tar from coke oven gas in primary gas coolers using chilled water.

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

0
1
> 1
< 1

A

> 1

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114
Q

Pick out the wrong statement:

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

A

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.

tunnel
heated cylinder
conveyor
festoon

A

heated cylinder

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116
Q

Pick out the wrong statement.

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

A

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

large latent heat
low viscosity
small latent heat
none of these

A

large latent heat

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118
Q

The most common packing used in industrial operations is __________ rings.

raschig
lessing
cross-partition
single spiral

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

zero
unity
infinity
none of these

A

infinity

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120
Q

Leaching of sugar from sugar beets is done by

hot water
hexane
dilute H2SO4
lime water

A

hot water

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121
Q

Absorption factor method is used to calculate the number of ideal stages, when

operating line lies above the equilibrium line.
operating line lies below the equilibrium line.
both operating and equilibrium lines are parallel.
pressure drop in the column is very high.

A

both operating and equilibrium lines are parallel.

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122
Q

Flights in a rotary dryer are provided to

lift and shower the solids thus exposing it thoroughly to the drying action of the gas.
reduce the residence time of solid.
increase the residence time of the solid.
none of these.

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)

(1-f)/f
- (f-1)/f
-1/f
-f/(1-f)

A

-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

the system comprises of partially mis-cible liquids.
the system comprises of miscible liquids.
the system comprises of an azeotrope.
on heating, a vapor phase will appear ; while on cooling, a solid phase will appear.

A

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

degree of dispersion of one fluid in the other.
interfacial surface exposed between the phases.
both (a) & (b).
none of these.

A

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

0.0
0.2
0.4
1.0

A

0.4

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127
Q

Dry bulb temperature of unsaturated air is more than its __________ temperature.

dew point
wet bulb
both ‘a’ & ‘b’
neither ‘a’ nor ‘b’

A

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

0.60
0.24
1
0.72

A

1

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129
Q

The reciprocal of stripping factor is termed as

selectivity index
relative volatility
absorption factor
Murphree efficiency

A

absorption factor

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130
Q

Ponchan-Savarit method analyses the fractional equipment based on

enthalpy balance only.
material balance only.
both enthalpy and material balances.
the assumption of constant molaloverflow.

A

both enthalpy and material balances.

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131
Q

The binary diffusivity in gases at atmospheric conditions is about

10^-9 cm/sec
10^-1 cm^2/sec
10^-3 sec/cm
10^-4 cm^2/sec^2

A

10^-1 cm^2/sec

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132
Q

Percentage saturation is __________ the relative saturation.

always smaller than
always greater than
not related to
none of these

A

always smaller than

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133
Q

In case of a desorber (stripper), the

operating line always lies above the equilibrium curve.
operating line always lies below the equilibrium curve.
temperature remains unaffected.
temperature always increases.

A

operating line always lies below the equilibrium curve.

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134
Q

What is the reflux ratio at total reflux ?

Zero
Infinity
Unity
Data insufficient

A

Infinity

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135
Q

Under conditions of flooding in packed tower, the gas pressure drop

decreases rapidly
increases rapidly
remains constant
is maximum

A

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).

1-5
10-60
200-300
> 500

A

10-60

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137
Q

For absorbing a sparingly soluble gas in a liquid

gas side mass transfer co-efficient should be increased.
liquid side mass transfer co-efficient should be increased.
liquid side mass transfer co-efficient should be decreased.
mass transfer co-efficient must be kept constant.

A

liquid side mass transfer co-efficient should be increased.

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138
Q

Channelling in a packed tower results from the

high pressure drop
maldistribution of liquid
non-uniformity of packing
both (b) and (c)

A

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

integral heat of adsorption.
heat of wetting.
differential heat of adsorption.
heat of normal condensation.

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

no reflux
total reflux
zero reflux ratio
minimum reflux ratio

A

total reflux

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141
Q

A good solvent used for absorption should not have very high

viscosity
vapor pressure
freezing point
all (a), (b) & (c)

A

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

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142
Q

In a counter-current liquid extractor

both liquids flow at fixed rate.
both liquids can have any desired flow rate.
only one of the liquids may be pumped at any desired rate.
liquid’s flow rate depends upon the temperature and pressure.

A

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 ?

Low vapour pressure
Low velocity
Low freezing point
None of these

A

None of these

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144
Q

The wetted wall tower is used to determine

individual mass transfer co-efficient (M.T.C.) in gaseous system.
M.T.C. of individual components in a liquid-liquid system.
M.T.C. of liquid in liquid-gas system.
the overall M.T.C. of the system.

A

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

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145
Q

Weight of 1 m^3 of humid air as compared to 1 m^3 of dry air, under the same conditions, is

less
more
same
unpredictable

A

less

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146
Q

Positive deviation from Raoult’s law means a mixture whose total pressure is

greater than that computed for ideality.
less than that computed for ideality.
less than the sum of the vapour pressure of the components.
none of these.

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

increases
decreases
decreases linearly
remains unaffected

A

increases

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148
Q

Schmidt number is given by

μ/ρ.DAB
Re.Pe
Sh x Pe
Re/Pe

A

μ/ρ.DAB

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149
Q

The caking of crystals can be prevented by

maintaining high critical humidity.
maintaining low critical humidity.
coating the product with inert material.
both (a) and (c)

A

both (a) and (c)

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150
Q

Prandtl number for water at 20°C is about

7
70
0.7
150.

A

7

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151
Q

Boiling point diagram is

not affected by pressure.
affected by pressure.
a plot of temperature vs. liquid composition.
a plot of temperature vs. vapour composition.

A

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,

as the acetone concentration increases, the solubility curves approach each other.
both the phases become identical at a particular common point on both the solubility curves called the plait point.
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.
all (a), (b) and (c).

A

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

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153
Q

Steam distillation is used to

reduce the number of plates.
avoid thermal decomposition of a component.
increase the efficiency of separation.
increase the total pressure of distillation.

A

avoid thermal decomposition of a component.

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154
Q

Freundlich equation applies to the adsorption of solute from

dilute solutions, over a small concentration range.
gaseous solutions at high pressure.
concentrated solutions.
none of these.

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.

no change in theoretical
marginal decrease in the number of
major decrease in the number of
none of these

A

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

pure component
binary mixture
ternary mixture
insoluble binary system

A

pure component

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157
Q

The diffusivity (D) in a binary gas mixture is related to the pressure (P) as

D ∝ P^0.5
D ∝ 1/p^0.5
D ∝ 1/p
D ∝ 1/p^1.5

A

D ∝ 1/p

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158
Q

A slurry is to be dried to produce flaky solid. Which dryer would you recommend ?

Spray dryer
Drum dryer
Rotary dryer
Dielectric dryer

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 ?

Cooling and dehumidification.
Heating and dehumidification at almost constant wet bulb temperature.
Dehumidification with dry bulb temperature remaining constant.
None of these.

A

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, . This is true when the stripping factor ‘S’ is

S > 1
S < 1
S = 1
S = ∞

A

S > 1

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161
Q

The cooling effect in a cooling tower can not be increased by

increasing the air velocity over the wet surfaces.
reducing the humidity of entering air.
lowering the barometric pressure.
none of these.

A

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

1

0.5
2

A

1

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163
Q

The humid volume may be increased by increasing the

temperature at constant humidity.
humidity at constant temperature.
both (a) and (b).
neither (a) nor (b).

A

both (a) and (b).

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164
Q

Pick out the wrong statement

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

A

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.

continuous
steam
azerotropic
none of these

A

steam

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166
Q

Large scale drying of wheat is done in a __________ dryer.

fluidised bed
spouted bed
tray
vacuum rotary

A

spouted bed

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167
Q

Azeotropic distillation is employed to separate

constant boiling mixture.
high boiling mixture.
mixture with very high relative volatility.
heat sensitive materials.

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 )

T^1/2
T
T^2
T^3

A

T^2

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169
Q

At the boiling point of the liquid at the prevailing pressure, the saturated absolute humidity becomes

1
0

none of these

A

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170
Q

Use of natural draft cooling tower is practised, when the air has low

humidity
temperature
both ‘a’ & ‘b’
neither ‘a’ nor ‘b’

A

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

less
more
equal
either (a) or (b); depends on the packing height

A

more

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172
Q

Dimension of mass diffusivity is the same as that of

kinematic viscosity
dynamic viscosity
surface tension
pressure

A

kinematic viscosity

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173
Q

Dorr thickener is an equipment used for

classification
sedimentation
clarification
leaching

A

sedimentation

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174
Q

Steam distillation is used to separate

azeotropes.
high boiling substances from nonvolatile impurities.
heat sensitive materials.
mixtures of low relative volatility.

A

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

q > 1
q < 1
q = 1
q = 0

A

q = 1

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176
Q

Which of the following is an undesirable property in a tower packing ?

Large surface per unit volume.
Large free cross-section.
Low weight per unit volume.
Large weight of liquid retained.

A

Large weight of liquid retained.

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177
Q

Water entrained by circulating air in cooling towers is termed as

drift
blow down
vapor load
none of these.

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

1000
1500
2000
2500

A

1000

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179
Q

With increase in temperature, the rate of leaching increases, because the

diffusivity of solute increases.
viscosity of solvent decreases.
thermal conductivity of solute increases.
none of these.

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
relative
percentage
none of these

A

molal

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181
Q

The Kundsen diffusivity is proportional to (where, T = absolute temperature)

T^1/2
T^2
T
T^4

A

T^1/2

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182
Q

In case of constant underflow extraction operation, the __________ at all solute concentration.

solids are drained to the same extent
ratio of the insoluble to solution is constant
both(a) & (b)
neither (a) nor (b)

A

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.

greater than
smaller than
equal to
either (a), or (b) ; depends on the type of packing

A

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.)

Kc = Kp = Km
Kc = Kp/RT = Km . RT/P
Kc = Kp . RT = Km . RT/p
none of these

A

Kc = Kp . RT = Km . RT/p

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185
Q

With increase in temperature, the leaching rate increases because of the

increased diffusivity.
decreased viscosity of liquid.
both (a) and (b).
neither (a) nor (b).

A

both (a) and (b).

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186
Q

Leaching of uranium ore and gold ore is done in

centrifugal extractor
Pachuka tanks
Bollman extractor
none of these

A

Pachuka tanks

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187
Q

Blowdown in a cooling tower

means discarding a small fraction of circulating water to prevent and limit the concentration of salt and impurities.
increases the scale forming tendencies of water.
is undesirable.
all (a), (b) & (c).

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

decrease in air temperature
increase in air humidity
both (a) and (b)
neither (a) nor (b)

A

both (a) and (b)

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189
Q

Antibiotics are best handled in a

Podbielniak extractor.
sieve tray contractor.
rotating disc contactor.
pulsed column extractor.

A

Podbielniak extractor.

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190
Q

The fixed cost of a distillation column at minimum reflux ratio is

minimum
infinite
optimum
none of these

A

infinite

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191
Q

__________ extractor uses centrifugal force for separating the two phases.

Treybal
Schiebel
Podbielniak
None of these

A

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

1.5
-0.6
-1.5
0.6

A

-1.5

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193
Q

Pick out the wrong statement.

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

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

solvent extraction
continuous distillation
evaporation
absorption

A

solvent extraction

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195
Q

Design calculation for multiple component distillation is done by

Ponchon-Savarit method
Mccabe-Thiele method
enthalpy concentration method
tray to tray calculations.

A

tray to tray calculations.

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196
Q

To get high tray efficiency

interfacial surface between liquid and gas phase should be large.
time of contact between the two phases should be less.
gas velocity should be very low.
liquid entrainment should be severe.

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

D/a
D/2a
proportional to D^1/2
dependent on the Reynolds number

A

dependent on the Reynolds number

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198
Q

Pick out the wrong statement. Generally for physical adsorption, a gas of

higher molecular weight is adsorbed in preference to a gas of low molecular weight.
high critical temperature is adsorbed in preference to a gas of low critical temperature.
low volatility is adsorbed in preference to a gas of high volatility.
none of these.

A

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

reducing the axial mixing.
increasing the rate of extraction.
maintaining the concentration difference between the two phases.
all ‘a’, ‘b’ & ‘c’.

A

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

KG = 1/KG + m/KL
1/KG = 1/KG + m/KL
1/KG = 1/KL + m/KG
KG = 1/K/l + m/KG

A

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

extracting solvent is cheaply & abundantly available.
one of the liquid components is heat sensitive.
viscosity of liquid components is very high.
one of the liquid components has very high affinity towards the solvent.

A

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

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202
Q

Inside the distillation column, the

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

A

driving force for the vapour flow is the pressure drop.

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203
Q

Diffusivity in concentrated solutions differs from that in dilute solutions, because of the changes in

viscosity with concentration.
degree of ideality of the solution.
both (a) and (b).
neither (a) nor (b).

A

both (a) and (b).

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204
Q

Occurrence of ‘case hardening’ during drying of a high moisture solid cake __________ the drying rate.

increases
decreases
does not affect
exponentially increases

A

decreases

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205
Q

Which of the following is not a continuous drier ?

Drum drier
Spray drier
Tunnel drier
Tray drier

A

Tray drier

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206
Q

Humidification involves mass transfer between a pure liquid phase and a fixed gas, which is

insoluble in the liquid
soluble in the liquid
non-ideal in nature
at a fixed temperature

A

insoluble in the liquid

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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.

Dew point
Bubble point
Dry bulb temperature
Wet bulb temperature

A

Dew point

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208
Q

Rate of leaching increases with increasing

temperature
viscosity of solvent
pressure
size of the solid

A

temperature

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209
Q

An azeotropic mixture is a __________ mixture.

binary
ternary
constant boiling point
none of these

A

constant boiling point

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210
Q

Pick out the wrong statement.

In the McCabe-Thiele diagram for binary distillation, vertical feed line represents saturated liquid feed and horizontal feed line represents saturated vapour feed.
In small columns, local efficiency is larger than Murphree efficiency; in large columns local efficiency is smaller than Murphree efficiency.
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^-2 m/s. Then the average mass transfer co-efficient for the plate is 2 x 10^-2 m/s.
The concentration and hydrodynamic boundary layers over a flat plate are of equal thickness, if Schmidt number is equal to unity.

A

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^-2 m/s. Then the average mass transfer co-efficient for the plate is 2 x 10^-2 m/s.

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211
Q

Molecular seives are regenerated by heating to __________ °C.

< 150
200-330
> 500
> 1000

A

200-330

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212
Q

In continuous distillation, the internal reflux ratio (Ri) and the external reflux ratio (Re) are related as

Ri = Re / 1-Re
Ri = 1-Re/ Re
Ri = Re
Ri = Re/ 1+Re

A

Ri = Re/ 1+Re

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213
Q

In a counter-current extractor, as the axial mixing increases, the extraction efficiency

increases
decreases
remains unchanged
depends on the pressure of the system

A

decreases

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214
Q

Heat sensitive materials like certain pharmaceuticals and food stuffs can be dried in a/an __________ dryer.

indirect tray
spray
freeze
none of these

A

freeze

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215
Q

In extractive distillation, solvent is

added to alter the relative volatility of the mixture.
of high volatility.
present in overhead stream.
of high viscosity to give high tray efficiency.

A

added to alter the relative volatility of the mixture.

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216
Q

Radioactive nuclear waste is treated in

mixer-settler extractor
rotating-disc contactor
pulsed column extractor
Bollman extractor

A

pulsed column extractor

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217
Q

Large scale drying of sugar is done in a __________ dryer.

spouted bed
tray
rotary
truck

A

rotary

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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.

Dry bulb
Wet bulb
Dew point
none of these

A

Wet bulb

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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 )

T^1/2
T
T^1.5
T^3

A

T

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220
Q

__________ equation applies to diffusivities in liquids.

Gilliland
Hirschfelder
Wilke and Chang
none of these

A

Gilliland

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221
Q

A packed tower compared to a plate tower for a particular mass transfer operation

incurs smaller pressure drop.
allows installation of cooling coils.
is less costly when built in large sizes/diameters.
is more suitable, if suspended solids are present in fluid streams.

A

incurs smaller pressure drop.

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222
Q

Which of the following is the most commonly used leaching solvent in vegetable oil industry ?

Phenol
Hexane
Furfurol
Liquid SO2

A

Hexane

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223
Q

In an absorber, HETP does not vary with the

flow rate of liquid
flow rate of gas
type and size of packing
none of these

A

none of these

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224
Q

Large quantity of silica gel is normally dried in a __________ dryer.

freeze
through circulation
rotary vacuum
tray

A

through circulation

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225
Q

For the same system, if the same liquid used in an absorber is decreased, the tower height will

increase
decrease
remain unaffected
decrease or increase ; depends on the type of liquid

A

increase

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226
Q

Hydrogenation of oil is carried out in a/an __________ in Vanaspati manufacturing plant.

agitated vessel
sieve tray column
bubble cap column
packed tower

A

agitated vessel

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227
Q

Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent

a pure component.
a binary mixture.
a ternary mixture.
partially miscible ternary system.

A

a binary mixture.

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228
Q

In distillation column design, the McCabe-Thiele procedure is inadequate and a Ponchan-Savarit procedure is needed, when

saturated feed is not used.
an azeotrope forms.
the latent heat of vaporisation of the more and less volatile components are greatly different.
a total condenser is used.

A

a total condenser is used.

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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

liquid phase resistance-controlled.
gas phase resistance controlled.
impossible.
driven by a non-linear driving force.

A

gas phase resistance controlled.

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230
Q

As the reflux ratio decreases, the

separation becomes more efficient.
number of plates increases.
column diameter increases.
none of these.

A

number of plates increases.

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231
Q

Which of the following equipments is not used for gas dispersion ?

Agitated vessels
Bubble cap tray towers
Perforated sieve tray towers
Spray towers

A

Spray towers

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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

the product composition but not the fraction vaporised.
the product composition as well as the fraction vaporised.
the fraction vaporised but not the product composition.
neither the product composition nor the fraction vaporised.

A

the fraction vaporised but not the product composition.

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233
Q

The equation, NA = DAB. Pt / RTZ is for

steady state equimolar counter diffusion
Fick’s first law of diffusion
steady state diffusion for stagnant case
liquid M.T.C. by penetration theory.

A

steady state equimolar counter diffusion

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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

decreases
remains unchanged
increases
decreases exponentially

A

increases

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235
Q

The equation, Na = (DAB.Pt / RTZ.PBM)(PA1 - PA2) is for

Fick’s second law of diffusion.
steady state diffusion for stagnant case.
liquid M.T.C. by Higbie penetration theory.
none of these.

A

steady state diffusion for stagnant case.

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236
Q

Which of these columns incurs the lowest pressure drop ?

Packed column (with stacked packing)
Packed column (with dumped packing)
Bubble plate column
Pulse column

A

Packed column (with stacked packing)

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237
Q

In the desorption of highly soluble gas from the liquid, the main resistance will be in the __________ phase.

gas
liquid
both (a) & (b)
neither (a) nor (b)

A

liquid

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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

L/G
G/L
always < 1
none of these

A

L/G

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239
Q

Which of the following remains constant during evaporative cooling process with recirculated water supply ?

Relative humidity
Partial pressure of vapour
Wet bulb temperature
None of these

A

Wet bulb temperature

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240
Q

For stripping of a gas in a counter current stripper, the operating line

lies above the equilibrium curve.
lies below the equilibrium curve.
can lie above or below the equilibrium curve.
is always parallel to the equilibrium curve.

A

can lie above or below the equilibrium curve.

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241
Q

Which of the following same diameter columns gives lowest pressure drop per unit height ?

Bubble-cap column
Sieve-plate column
Packed column (stacked)
Randomly packed column

A

Packed column (stacked)

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242
Q

Diffusion in concentrated solutins differs from that in dilute solutions, because of the change in the __________ with the concentration of the solution.

degree of ideality
viscosity
both ‘a ‘& ‘b’
neither ‘a’ nor ‘b’

A

both ‘a ‘& ‘b’

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243
Q

Stage efficiency in a leaching process depends on the

time of contact between the solid and the solution
rate of diffusion of the solute through the solid and into the liquid
both (a) and (b)
vapour pressure of the solution

A

both (a) and (b)

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244
Q

Operating velocity in a packed tower is usually __________ the flooding velocity.

half
twice
equal to
more than

A

half

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245
Q

The Knudsen diffusivity is dependent on the

molecular velocity only.
pore radius of the catalyst only.
molecular mean free path only.
molecular velocity and pore radius of the catalyst.

A

molecular velocity and pore radius of the catalyst.

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246
Q

Minimum possible diameter of a packed coloumn is decided mainly by the

flooding
gas viscosity
liquid density
liquid hold up

A

flooding

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247
Q

Solvent used in extractive distillation

is of low volatility.
forms a low boiling azeotrope.
forms a high boiling azeotrope.
does not alter the relative volatility of the original components.

A

forms a low boiling azeotrope.

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248
Q

Capacity of a rotary dryer depends on its

r.p.m
inclination with ground surface
both (a) and (b)
neither (a) nor (b)

A

both (a) and (b)

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249
Q

The cooling effect in a cooling tower can be speeded up by

increasing the air velocity and area of exposed wet surface.
reducing the barometric pressure.
reducing the humidity of the air.
all (a), (b) and (c).

A

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

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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.
(insert graph here-S5P10)

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

A

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

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251
Q

When both the fluids flow concurrently in an absorber, the slope of the operating line is

-ve
+ve
1
-1

A

-ve

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252
Q

The percentage humidity is less than the relative humidity only at __________ percent humidity.

zero
hundred
both zero and hundred
none of these

A

both zero and hundred

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253
Q

Back-trapping in a distillation column

increases tray efficiency.
decreases tray efficiency.
reduces pressure drop.
is desirable, as it provides improved vapour-liquid contact.

A

decreases tray efficiency.

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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.

less than
more than
same as
very much less

A

more than

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255
Q

Milk is dried usually in a __________ dryer.

freeze
spray
tray
rotary

A

spray

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256
Q

At a given equilibrium pressure, with increase in temperature, the concentration of adsorbed gas on solid adsorbant

increases
decreases
remains unchanged
increases exponentially

A

decreases

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257
Q

Which of the following adsorbent is used to decolourise yellow glycerine ?

Silica gel
Alumina
Fuller’s earth
Activated carbon

A

Activated carbon

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258
Q

Which of the following liquid temperature (T) Vs. vapor-gas mixture enthalpy (H) diagram is valid for humidification operation?

(insert graph here-S6P2)
(insert graph here-S6P2)
(insert graph here-S6P2)
none of these.

A

(insert graph here-S6P2)

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259
Q

In a distillation column, with increase in the reflux ratio, the heat removed in the cooler

increases.
decreases.
remains unaffected.
and the heat required in reboiler decreases.

A

increases.

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260
Q

Pick out the wrong statement.

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

A

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

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261
Q

Which of the following is not a unit of mass transfer co-efficient ?

moles transferred / (time)(area)(mole fraction)
moles transferred / (time)(area)(pressure)
moles transferred / (time)(area)(massA/massB)
none of these

A

none of these

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262
Q

The falling rate period in the drying of a solid is characterised by

increase in rate of drying.
increasing temperatures both on the surface and within the solid.
decreasing temperatures.
none of these.

A

increasing temperatures both on the surface and within the solid.

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263
Q

In which of the following unit operations, the selectivity is an important parameter ?

Distillation
Solvent extraction
Absorption
None of these

A

Solvent extraction

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264
Q

Which of the following is an undesirable characteristic for the solvent used in gas absorption ?

Low vapor pressure
Low viscosity
High gas solubility
None of these

A

None of these

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265
Q

Which of the following equipments is not used for liquid dispersion ?

Wetted wall towers
Packed towers
Venturi scrubbers
Agitated vessels

A

Agitated vessels

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266
Q

Diameter of raschig rings used in packed tower in industry is normally around __________ inches.

2
8
12
18

A

2

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267
Q

The diffusion co-efficient in m2 /s. of acetic acid in benzene (liquid in liquid) is

2.09 x 10^-4
2.09 x 10^-5
2.09 x 10^-9
2.09 x 10^-12

A

2.09 x 10^-9

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268
Q

Pick out the wrong statement.

The Reynolds analogy for mass transfer is given by Lewis relation and is applicable, when Schmidt number is one.
Sherwood number for flow in pipes can be expressed as the ratio of the concentration gradient at wall to the overall concentration difference.
According to film theory for equimolar counter diffusion, the mass transfer coefficient is given by (DAB)^1/2 (b)P - 3, Q - 2
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

According to film theory for equimolar counter diffusion, the mass transfer coefficient is given by (DAB)^1/2 (b)P - 3, Q - 2

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269
Q

In case of non-ideal gases and liquids, the molal diffusivity

varies inversely as the pressure.
varies directly as the pressure.
is independent of pressure.
is equal to the volumetric diffusivity.

A

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 )

p = P
p&raquo_space;P
p < P
p &laquo_space;P

A

p = P

271
Q

__________ number indicates the ratio of the rates of the heat and mass transfer incase of a cooling tower.

Sherwood
Stanton
Lewis
Peclet

A

Lewis

272
Q

The expression, y(1 - x)/x(1 - y) is for

absorption factor
relative volatility
selectivity
Murphree efficiency

A

relative volatility

273
Q

In physical terms, Schmidt number means

thermal diffusivity/mass diffusivity.
thermal diffusivity/momentum diffusivity.
momentum diffusivity/mass diffusivity.
mass diffusivity/thermal diffusivity.

A

momentum diffusivity/mass diffusivity.

274
Q

In case of liquids, the binary diffusivity is proportional to (where, T = temperature)

T
T^1/2
T^2
1/T

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

Newtonion liquids
non-Newtonion liquids
ideal gases
real gases

A

ideal gases

276
Q

Mass transfer co-efficient is directly proportional to DAB0.5, according to __________ theory.

penetration
surface renewal
film
none of these

A

penetration

277
Q

Sand is dried in foundaries in a___drier.

rotary
fluidized bed
vacuum
spray

A

fluidized bed

278
Q

Which of the following employs an accessory known as ‘drift eliminator’ ?

Multiple effect evaporator.
Mechanical draft cooling tower.
Rotary dryer.
Rotating disc contactor.

A

Mechanical draft cooling tower.

279
Q

Pick out the correct statement.

Higher hold up of the solid in the rotary dryer results in better exposure of the solids to the gas.
The ‘Hatta number’ is important in problems involving gas absorption without chemical reaction.
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.
Total reflux in case of distillation operation requires infinite number of plates for a binary system separation.

A

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.

For identical gas flow rates, less pressure drop occurs through a plate tower than through a packed tower.
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.
For the same duty, plate columns weigh less than packed columns.
all (a), (b) and (c).

A

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

281
Q

Humid volume is the total volume in m3 of 1 kg of

vapour laden gas at 1 atm. and room temperature.
gas plus its accompanying vapour at 1 atm. and room temperature.
gas plus its accompanying vapour at 1 atm. and gas temperature.
vapour laden gas at 1 atm. and gas temperature.

A

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

282
Q

Diameter to height ratio for a rashig ring is

1
0.5
2
8

A

1

283
Q

The equipment used in the extraction of highly corrosive radio active liquids is

pulse column
spray column
mixer settler
baffle tower

A

pulse column

284
Q

Advantage of continuous drying over batch drying is that the

drying cost per unit weight of dried product is less.
product with more uniform moisture content is produced.
equipment size required is smaller.
all ‘a’, ‘b’ & ‘c’

A

all ‘a’, ‘b’ & ‘c’

285
Q

With increase in temperature, the rate of extraction in leaching (solid-liquid extraction system)

increases
decreases
remains unaffected
increases Linearly

A

increases

286
Q

In a packed bed absorption column, the channelling will be noted by the

increase in flow rate.
sharp drop in pressure drop.
sharp rise in pressure drop.
none of these.

A

sharp drop in pressure drop.

287
Q

Gaseous diffusivity at atmospheric pressure is of the order of __________ cm^2/second.

1
1 to 5
5 to 10
> 10

A

1

288
Q

In liquid-liquid extraction, the number of phases at plait point is

1
2
3
4

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.

The entire amount of C is transferred to solvent B.
Less than 2 kg but more than 1 kg of C is transferred to solvent B.
Less than 1 kg of C is transferred to B.
No amount of C is tranferred to B.

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)

(KL^2.DA)^1/2
KL^2.DA
KL^2/DA
KL/DA^2

A

(KL^2.DA)^1/2

291
Q

If Rm is the minimum reflux ratio, the optimum reflux ratio may be around __________ Rm.

1.2 to 1.5
2.5 to 3
3 to 4
5

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.

wet bulb temperature
partial pressure of water vapor
relative humidity
none of these

A

wet bulb temperature

293
Q

In case of absorption, both the operating and equilibrium lines will be straight for

isothermal operation.
dilute solutions.
dilute solutions and isothermal operation.
none of these.

A

dilute solutions and isothermal operation.

294
Q

Mass transfer co-efficient varies as DAB0.5, according to the __________ theory.

film
surface renewal
penetration
none of these

A

surface renewal

295
Q

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

concentrated solution and non-isothermal operation.
dilute solution and non-isothermal operation.
dilute solution and isothermal operation.
concentrated solution and isothermal operation.

A

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 :
(insert image here - S6P10)
In the figure xF, xD and xW represent the weight fraction of benzene in the feed, distillate and residue respectively. The reflux ratio is

0.5
0.6
1.0
2.0

A

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

humidified with wet bulb temperature decreasing.
humidified at constant wet bulb temperature.
dehumidified.
none of these

A

humidified with wet bulb temperature decreasing.

298
Q

Humid volume, at a given temperature is a/an __________ function of humidity.

inverse
exponential
linear
logarithmic

A

linear

299
Q

The Schmidt number which is defined as, μ/ρ D, is the ratio of the

momentum diffusivity to the mass dif-fusivity.
thermal diffusivity to the mass diffusivity.
momentum diffusivity to the thermal diffusivity.
none of these.

A

momentum diffusivity to the mass dif-fusivity.

300
Q

If f is defined as above, then which of the following applies to a feed at dew point ?

f = 1
f < 1
f > 1
0 < f < 1

A

f = 1

301
Q

Perforated plate towers are unique for solvent extraction because, they provide

higher contact area.
better contact of the phase.
repeated coalescence & redispersion of the drop phase.
none of these.

A

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.

interface
gas phase
liquid phase
all ‘a’, ‘b’ & ‘c’

A

interface

303
Q

Pick out the wrong statement pertaining to the analogy between equations of heat and mass transfer operations.

Sherwood number in mass transfer is analogous to Nusselt number in heat transfer.
Prandtl number in heat transfer is analogous to Schmidt number in mass transfer.
Reynolds number in mass transfer is analogous to Grashoff number in heat transfer.
Reynolds number remains the same in both heat and mass transfer.

A

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

0

-ve
+ve

A

-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 ?

liquid side
gas side
interfacial
both liquid and gas side

A

gas side

306
Q

Pore size of the molecular seive 5A is __________ mm.

5
0.5
0.05
50

A

0.5

307
Q

Swenson-Walker crystalliser is a __________ unit

continuous
batch
semi-batch
cooling (adiabatic)-cum-evaporation

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.

5
9
12
28

A

12

309
Q

Absorption (liquid-gas system) with evolution of heat as compared to isothermal absorption results in

decreased solute solubility.
large minimum liquid to gas (L/G) ratio.
large number of trays.
all (a), (b) and (c).

A

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

310
Q

With increase in temperature, the mutual solubility of two liquids

increases
decreases
remains unchanged
decreases exponentially

A

increases

311
Q

Pick out the wrong statement.

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

A

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

1
> 1
0

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

only vapor phase follows Raoult’s law.
only liquid phase obeys Dalton’s law.
liquid phase obeys Dalton’s law and vapor phase obeys Raoult’s law.
Vapor phase obeys Dalton’s law and liquid phase obeys Raoult’s law.

A

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.

less than
more than
equal to
either (o) or (b); depends on the solid

A

less than

315
Q

Lewis number (Le) is

Sc / Pr
Pr x St
Sh x Pr
St x Sh

A

Sc / Pr

316
Q

Which of the following is not a continuous leaching equipment ?

Pachuka tank
Kennedy extractor
Bollman extractor
Hydrocyclones

A

Pachuka tank

317
Q

__________ extractor is used for the concentration of radioactive nuclear waste.

Pulsed column
Seive plate
Mixer-settler
Ballman

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.

free
unbound
equilibrium
bound

A

equilibrium

319
Q

All moisture in a non-hygroscopic material is the __________ moisture.

free
equilibrium
unbound
bound

A

unbound

320
Q

Pick out the correct relationship. (where, Ri = internal reflux ratio Ro = external reflux ratio. )

(1 + Ro) = Ro/Ri
(1 - Ro) = Ro/Ri
(1 + Ri) = Ro/Ri
(1 - Ri) = Ro/Ri

A

(1 + Ro) = Ro/Ri

321
Q

Separation of __________ employs gaseous diffusion process.

N2 and O2 from air
isotopes of uranium
isotopes of helium
SO2 and air

A

isotopes of uranium

322
Q

For water-ethanol system, the minimum reflux ratio

is computed from the slope of the upper operating line that is tangent to the equilibrium curve.
is computed from the intercept of the operating line.
cannot be computed.
is the optimum reflux ratio.

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 m^2/m^3)

500
1200
900
800

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.

lower than
higher than
same as
either same or higher than

A

lower than

325
Q

Experimental determination of __________ is done by wetted wall column method.

diffusion co-efficient
mass transfer co-efficient
NTU
none of these

A

mass transfer co-efficient

326
Q

Pick out the wrong statement:

Absorption factor is constant, when the equilibrium and operating lines are straight.
In case of a stripper, the equilibrium curve is always below the operating line.
In case of an absorber, the operating line is always above the equilibrium curve.
In the absorption of low solubility gases, the liquid film is the controlling resistance.

A

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

separation of the constituents is the most effective.
no separation will occur.
amount of solvent required will be minimum.
solvent flow rate should be very low.

A

no separation will occur.

328
Q

Paper industry employs __________ driers.

cylinder
rotary
spray
fluidised bed

A

cylinder

329
Q

Which of the following has the same dimension as mass diffusivity ?

Momentum flux
Kinematic viscosity
Thermal diffusivity
Both (b) and (c)

A

Both (b) and (c)

330
Q

Pick out the wrong statement pertaining to the cooling towers.

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

A

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/m^2 .s) for bulk concentrations of A in gas phase and liquid phase as y = 0.4 and x = 0.01 respectively is

5.6 x 10^-4
8.5 x 10^-4
5.6 x 10^-3
8.5 x 10^-3

A

8.5 x 10^-4

332
Q

Leaching of coarse solid lumps is also termed as

decoction
dissolution
percolation
agitation and settling

A

percolation

333
Q

The main reason for dividing a tall packed tower into series of small towers is to

minimise the overall pressure drop.
avoid flooding.
reduce liquid hold up.
avoid channeling.

A

avoid channeling.

334
Q

Co-current absorbers are usually used when the gas to be dissolved in the liquid is

sparingly soluble
highly soluble
a pure substance
a mixture

A

a pure substance

335
Q

At what percentage (by volume) of alcohol composition, it forms an azeotrope with water ?

90
91.5
95
99

A

95

336
Q

Measurement of the interfacial area of mass transfer is achieved easily & accurately in case of a __________ coloumn.

spray
packed
bubble cap plate
wetted wall

A

wetted wall

337
Q

With the lowering of equilibrium pressure, at a given temperature, the amount of adsorbate on the adsorbent

increases.
decreases.
remains same.
either (a) or (b), depends on the system.

A

decreases.

338
Q

Mass transfer co-efficient is defined as

Flux = Co-efficient/concentration difference.
Co-efficient = Flux/concentration difference.
Flux=concentration difference/co-effi-cient.
none of these.

A

Co-efficient = Flux/concentration difference.

339
Q

When an unsaturated air-water mixture is heated at constant pressure, then

the partial pressure of water vapour increases.
the specific humidity decreases.
The relative humidity increases.
the relative humidity decreases.

A

the relative humidity decreases.

340
Q

During sensible cooling process

relative humidity decreases
relative humidity increases
wet bulb temperature decreases
both (b) and (c)

A

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.

100
0
50
between 0 and 100

A

0

342
Q

In case of physical adsorption, the difference between heat of adsorption and heat of normal condensation is

equal to the heat of formation of surface compound.
equal to the heat of wetting.
zero.
called integral heat of adsorption.

A

equal to the heat of wetting.

343
Q

Pick out the wrong statement:

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

A

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

0.5 to 0.8
0.8 to 1.2
1.25 to 2.0
2.5 to 3.5

A

1.25 to 2.0

345
Q

Large scale usage of flash distillation is practised in

soap manufacturing
ammonia synthesis plant
polymerisation industry
petroleum refinning

A

petroleum refinning

346
Q

High pressure at the bottom of a distillation tower handling heat sensitive materials results in

thermal decomposition of bottoms.
increased relative volatility.
erosion of the tower.
very efficient operation.

A

thermal decomposition of bottoms.

347
Q

Alcohol is dehydrated using __________ distillation.

extractive
azeotropic
steam
molecular

A

azeotropic

348
Q

Separation of two volatile liquids by distillation makes use of their

selectivity
relative volatility
solubility
density difference

A

relative volatility

349
Q

Which of the following increases during evaporative cooling process with recirculated water supply ?

Wet bulb temperature
Relative humidity
Partial pressure of vapour
Both (b) and (c)

A

Both (b) and (c)

350
Q

Dried finished product sampled from various parts of a __________ dryer exhibits non-uniformity in the moisture content.

rotary
tray
freeze
none of these

A

tray

351
Q

__________ is used as an ‘entrainer’ for the separation of acetic acid-water mixture by distillation.

Furfural
Benzol
Butyl acetate
Hexane

A

Butyl acetate

352
Q

Rotary dryers cannot handle __________ materials.

free flowing
dry
sticky
grannular

A

sticky

353
Q

Pick out the correct statement.

Diffusivity decreases with increase in temperature.
Diffusivity increases with increase in molecular weight.
Diffusivity increases with the size of the individual molecule.
none of these.

A

none of these.

354
Q

An example of elution is

separation of uranium oxide from its ore by H2SO4 in a Pachuca tank.
separation of sugar from sugar beet by hot water.
dissolution of tannin out of tree barks by water.
recovery of vegetable oils from seeds.

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

mole fractions
mole ratios
partial pressure
mass fractions

A

partial pressure

356
Q

Relative volatility does not change appreciably with the change in

temperature
vapour pressure of either component
total pressure
none of these

A

temperature

357
Q

Boiling point diagram is not affected by the ambient

pressure
humidity
temperature
both (b) and (c)

A

both (b) and (c)

358
Q

The dew point of a saturated gas phase equals the __________ temperature.

gas
room
wet bulb
none of these

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 ?

Flow rate of inlet air
Relative humidity of outlet air
Humidity of inlet air
Temperature of the solid

A

Temperature of the solid

360
Q

In case of liquid-liquid binary diffusion, diffusivity of one constituent into another is not dependent on the

temperature and pressure
concentration
nature of the constituents
none of these

A

none of these

361
Q

For continuous drying of grannular or crystalline material, the dryer used is the __________ dryer.

tunnel
tray
rotary
none of these

A

rotary

362
Q

When adsorption hysteresis is observed, the desorption equilibrium pressure is __________ that obtained by adsorption.

always lower than
always higher than
same as
dependent on the system; can be either lower or higher than

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.

bound
unbound
critical
none of these

A

bound

364
Q

For a binary mixture with low relative volatility, continuous rectification to get pure products will require

low reflux ratio
less number of trays
small cross-section column
high reflux ratio

A

high reflux ratio

365
Q

The efficiency of a plate column will be maximum, when the flow is ideal __________ the plate.

across
above
both (a) & (b)
neither (a) nor (b)

A

both (a) & (b)

366
Q

Heat load in a cooling tower

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

A

both (a) & (b).

367
Q

In case of absorption with exothermic reaction, for fluids having

Pr = Sc; percentage change in heat and mass transfer flux will be the same for a given change in the degree of turbulence.
Pr = Sc = 1; total mass, momentum and thermal diffusivity will be the same.
both (a) and (b)
Pr = Sc ; there won’t be any change in heat and mass transfer flux with changes in degree of turbulence.
both (a) and (b)

A

both (a) and (b)

368
Q

Detergent solution is dried to a powder in a

spray dryer
spouted bed dryer
tunnel dryer
pan open to atmosphere

A

spray dryer

369
Q

Which of the following mixtures does not form an azeotrope at atmosheric pressure?

Water-alcohol
Methyl alcohol-acetone
Butyl acetate-water
None of these

A

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

gas film
liquid film
liquid-gas interface
none of these

A

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

increasing the gas film co-efficient.
increasing the liquid film co-efficient.
increasing the total pressure.
decreasing the total pressure.

A

increasing the gas film co-efficient.

372
Q

Flooding results in

high tray efficiency
low tray efficiency
high gas velocity
good contact between the fluids

A

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

water has a high latent heat of evaporation.
Lewis number is close to unity.
they are always equal under all circumstances.
solubility of the components of air in water is very small.

A

water has a high latent heat of evaporation.

374
Q

In an operating distillation column, the

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

A

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

range is 15°F.
approach is 10°F.
both (a) & (b).
neither (a) nor (b).

A

both (a) & (b).

376
Q

The diffusivity (D) in a binary gas mixture is related to the temperature (T) as

D ∝ T
D ∝ T^0.5
D ∝ T^1.5
D ∝ T^2

A

D ∝ T^1.5

377
Q

For which of the following unit operations, Lewis number is of significance ?

Adsorption
Binary distillation
Gas absorption
Humidification

A

Humidification

378
Q

Tray spacing in a distillation column of dia 10-12 ft. used in petroleum refinery may be around __________ inches.

5
30
60
100

A

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.

a1 = a2
a1 = 2a2
a1 = 0.5 a2
none of these

A

none of these

380
Q

The dimension of diffusivity is same as that of the

density
molal concentration
kinematic viscosity
velocity head

A

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.

dew point
wet bulb
dry bulb
none of these

A

none of these

382
Q

Entrainer used in azeotropic distillation should

form a low boiling azeotrope with one of the constituents of the mixture.
form a new azeotrope of low relative volatility with one of the constituents of the mixture.
have high latent heat of vaporisation.
have high viscosity to provide high tray efficiency.

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

temperature is less.
total pressure is less.
mixing of steam with the material being vaporised is not so intimate as to result in equilibrium condition.
saturated steam is used for steam distillation.

A

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.

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

A

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

hot water
hexane
lime water
dilute H2SO4 (hot)

A

hot water

386
Q

For contacting a highly soluble gas with a liquid

bubble the gas through liquid.
spray the liquid on gas stream.
either (a) or (b) would suffice.
none of these.

A

bubble the gas through liquid.

387
Q

During drying operation, it is easier to remove the __________ moisture.

equilibrium
critical
unbound
bound

A

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

increases
decreases
decreases linearly
remains unaffected

A

decreases

389
Q

Ion exchange process is similar to

absorption
adsorption
extraction
leaching

A

adsorption

390
Q

Dryer widely used in a textile industry is __________ dryer.

festoon
cylinder
conveyor
tunnel

A

conveyor

391
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,

composition of vapors and that of liquid do not vary throughout the column.
reboiler load and condenser load are minimum.
the top and bottom compositions are unchanged with and without total reflux.
the top and bottom compositions correspond to the maximum enrichment available.

A

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

392
Q

Solvent used in extractive distillation

changes the relative volatility of the original components.
should be of high volatility.
should form azeotropes with the original components.
all (a), (b) and (c)

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

decreases
increases
depends on the extent of heating
remain unchanged

A

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)

straight
parallel
both (a) & (b)
neither (a) nor (b)

A

both (a) & (b)

395
Q

The vapour pressure exerted by the moisture contained in a wet solid depends upon the

nature of the moisture.
temperature.
nature of the solid.
all (a), (b) and (c).

A

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)

L/mG
G/mL
mL/G
LG/m

A

L/mG

397
Q

Smoke is an example of

solid dispersed in liquid
solid dispersed in gas
liquid dispersed in gas
gas dispersed in liquid

A

solid dispersed in gas

398
Q

Which of the following adsorbant is used in the refining of sugar ?

Bone charcoal
Wood charcoal
Silica gel
Activated clay

A

Bone charcoal

399
Q

Stacked packing compared to dumped packing

provides poorer contact between the fluids.
gives lower pressure drop.
both (a) and (b).
gives higher pressure drop.

A

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.

total
minimum
operating
maximum permissible

A

total

401
Q

Which of the following parameters remains constant during chemical dehumidifica-tion?

Dry bulb temperature
Partial pressure of vapour
Wet bulb temperature
None of these

A

Dry bulb temperature

402
Q

Drying of a solid involves __________ transfer.

only heat
only mass
both heat and mass
none of these

A

both heat and mass

403
Q

Mechanism of moisture removal in case of freeze drying of food stuff is by

evaporation
sublimation
dehydration
adsorption

A

sublimation

404
Q

The dew point of an unsaturated gas-vapor mixture does not depend upon the __________ of the mixture.

composition
temperature
total pressure
all (a), (b) and (c)

A

temperature

405
Q

Which is not concerned directly with mass transfer ?

Schmidt number
Sherwood number
Lewis relationship
Froude number

A

Froude number

406
Q

Removal of __________ exemplifies an adsorption unit operation.

uranium from its ore
water from petrol
ammonia from coke oven gas
mustard oil from mustard seed

A

water from petrol

407
Q

Can the efficiency of a plate in the distillation tower be greater than 100% ?

Yes
Normally not; but is possible if infinite number of plates are put.
Never
Yes ; if the reflux ratio is maximum.

A

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.

increases
decreases
remains same
increases linearly

A

increases

409
Q

For gas absorption, low viscosity solvents are preferred, because of their

better flow characteristics.
low pumping pressure drop.
rapid absorption rates.
all (a), (b) and (c).

A

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

410
Q

To remove all the moisture from a wet solid it requires exposure to __________ air.

perfectly dry
highly humid
high temperature
none of these

A

perfectly dry

411
Q

The operating cost of a distillation column at minimum reflux ratio is

minimum
maximum
infinite
zero

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

2
0.5
50
150

A

2

413
Q

Molecular diffusivity of a liquid

increases with temperature.
decreases with temperature.
may increase or decrease with temperature.
is independent of temperature.

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.

25
> 25
< 25
- 25

A

> 25

415
Q

Henry’s law states that the

partial pressure of a component over a solution is proportional to its mole fraction in the liquid.
partial pressure of a component over a solution is proportional to the mole fraction in the vapour.
vapour pressure is equal to the product of the mole fraction and total pressure.
partial pressure is equal to the product of the mole fraction and total pressure.

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

caustic solution
dilute ammoniacal liquor
dilute HCl
ethanolamine

A

dilute ammoniacal liquor

417
Q

With increase in temperature, the leaching rate increases due to

decreased liquid viscosity
increased diffusivity
both (a) and (b)
neither (a) nor (b)

A

both (a) and (b)

418
Q

Which of the following processes is not an example of adsorption applied to gaseous separations ?

Recovery of valuable solvent vapors from dilute mixture with air and other gases.
Dehumidification of air and gas.
Removal of objectionable odour and impurities from industrial gases.
Decolouration of yellow glycerene.

A

Decolouration of yellow glycerene.

419
Q

The critical moisture content in case of drying indicates the __________ rate period.

beginning of falling
beginning of constant
end of falling
none of these

A

beginning of falling

420
Q

Pick out the wrong statement

A horizontal line on the humidity chart indicates the temperature changes at constant molal humidity.
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.
For unsaturated air-water vapor mixture at atmospheric conditions, the wet bulb temperature & adiabatic cooling lines are the same.
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

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)

μ
1/μ
μ^1/2
μ^2

A

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

1
0
2
3

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

2.0
1.56
1.0
0.56

A

2.0

424
Q

Packed column distillation is limited to the column __________ metres.

height < 6
diameter < 0.6
both (a) & (b)
neither (a) nor (b).

A

both (a) & (b)

425
Q

For the flow of gases through a capillary, with increase in temperature, the permeability __________ as per Knudsen law.

increases
decreases
remains same
either (a) or (b); depends on the gas

A

increases

426
Q

Which of the following is directly concerned with psychrometry ?

Lewis relationship
Galileo number
Weber number
Dean number

A

Lewis relationship

427
Q

Plate efficiency in a distillation column is reduced due to the __________ of liquid.

entrainment
foaming
weeping & dumping
all (a), (b) & (c)

A

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

428
Q

The most efficient cooling tower out of the following is

induced draft
forced draft
natural draft
atmospheric

A

induced draft

429
Q

Sodium bicarbonate is produced during soda ash manufacture using a __________ tower.

plate
baffle
packed
none of these

A

baffle

430
Q

Powdery materials can be guarded against caking tendency on storage by

providing irregular grain size.
providing minimum percentage of voids.
having maximum possible points of contact.
none of these.

A

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.

Lewis
Grashoff
Sherwood
none of these

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 ?

Packed towers
Plate towers
Spray towers
Wetted wall columns

A

Wetted wall columns

433
Q

The temperature of water cooled in cooling tower is always __________ temperature of entering air.

more than the wet bulb
less than the wet bulb
equal to the wet bulb
equal to the dry bulb

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?

Humidification only
Heating only
Both heating and humidification
Evaporative cooling

A

Both heating and humidification

435
Q

Mass transfer co-efficient is directly proportional to DAB according to the __________ theory.

film
penetration
surface-renewal
none of these

A

film

436
Q

The relative volatility of a binary mixture at constant temperature __________ the total pressure.

decreases with increase in
increases with increase in
is independent of
none of these

A

decreases with increase in

437
Q

Tower diameter may be decreased by

using higher reflux ratio.
use of increased tray spacing.
increasing the liquid flow rate.
increasing the vapour flow rate.

A

use of increased tray spacing.

438
Q

Rayleigh’s equation applies to __________ distillation.

continuous
steam
differential
flash

A

differential

439
Q

Steady state equimolal counter diffusion is encountered in

separation of a binary mixture by distillation.
absorption of NH3 from air by water.
all liquid-liquid diffusion systems.
all liquid-solid diffusion systems.

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 ?

Partial condenser
Total condenser
Reboiler
Both (b) and (c)

A

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 ?

Cost
Availability
Toxicity
Selectivity

A

Selectivity

442
Q

As the reflux ratio increases, the slope of the operating line for rectifying section

increases
decreases
remains constant
data insufficient, cannot be predicted

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)

log P vs . T
log P vs. log T
T vs. P
P vs . log T

A

log P vs . T

444
Q

The unit of volumetric diffusivity is

cm^2/sec
cm/sec
cm^3/sec
cm^2/sec^2

A

cm^2/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.

binary mixture is represented by the apex
binary mixture is represented by any point inside
ternery mixture is represented by the sides
pure component is represented by the apex.

A

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.

dry-bulb
wet-bulb
dew point
adiabatic saturation

A

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

100
10
5
1

A

10

448
Q

The slope of 9-line is determined by the

reflux ratio
plate efficiency to be achieved
thermal condition of the feed
relative volatility.

A

thermal condition of the feed

449
Q

In steam distillation, the

temperature is 100°C.
temperature is more than 100° C.
product must be immiscible with water.
temperature is higher than the boiling point of either component.

A

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 ?

Dew point
Humidity ratio
Wet bulb temperature
None of these

A

Wet bulb temperature

451
Q

Steam distillation is used for separation of high boiling

substances from non-volatile impurities.
volatile impurity from still higher boiling substances.
both (a) and (b).
neither (a) nor (b).

A

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

increase
decrease
remains same
depend on saturated boiling point; may increase or decrease

A

increase

453
Q

Rose oil is extracted from rose leaves using __________ distillation.

high pressure
low pressure
extractive
steam

A

steam

454
Q

Hypersorption refers to a __________ process.

fixed bed absorption
moving bed absorption
fixed bed adsorption
moving bed adsorption

A

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) ?

(insert graph here-S10P1)
(insert graph here-S10P1)
(insert graph here-S10P1)
None of these.

A

(insert graph here-S10P1)

456
Q

Extraction of coffee from its seed is done by

liquid-liquid extraction.
leaching.
extractive distillation.
steam distillation.

A

leaching.

457
Q

In azeotropic mixture, the equilibrium vapour composition is

more than liquid composition.
less than liquid composition.
same as liquid composition.
independent of pressure.

A

same as liquid composition.

458
Q

With lapse of time, the overhead composition of light component in case of batch distillation with constant reflux

increases
decreases
remains same
may increase or decrease ; depends on system.

A

decreases

459
Q

Lewis number, which is important in problems involving simultaneous heat and mass transfer, is the ratio of

mass diffusivity to momentum diffusivity.
thermal diffusivity to mass diffusivity.
momentum diffusivity to thermal diffusivity.
none of these.

A

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)

D
D^2
D^0.5
1/D

A

D

461
Q

Dry bulb temperature of the gas is __________ the wet bulb temperature.

less than
more than
equal to
none of these

A

more than

462
Q

Decoction refers to the use of solvent

at ambient temperature
at its boiling point
in its vapor form
none of these

A

at its boiling point

463
Q

Flash distillation is suitable for separating the constituents of a binary system, which

form minimum boiling azeotrope.
have very wide boiling points.
have very close boiling points.
form constant boiling azeotrope.

A

have very wide boiling points.

464
Q

The ratio of Murphree plate efficiency to point efficiency is 1 in a __________ flow model.

plug
perfectly mixed
both (a) & (b)
neither (a) nor (b)

A

perfectly mixed

465
Q

The rough value of diffusion co-efficient of water vapor into air at 25°C may be about __________ cm^2/sec.

0.25
2.5
1.25
0.0025

A

0.25

466
Q

Flooding in a column results due to

high pressure drop
low pressure drop
low velocity of the liquid
high temperature

A

high pressure drop

467
Q

Which of the following gas-liquid contacting devices incurs the least pressure drop for a particular duty ?

Grid tray tower
Perforated tray tower
Wetted wall tower
Bubble cap tower

A

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?

The mixture exhibits an azeotrope at 101.3 kPa.
The composition of the mixture, in percent by volume is: o-xylene 30, p-xylene 60. and m-xylene 10.
The composition of the mixture in mole percent is: o-xylene 30, p-xylene 60 and m-xyoene 10.
The mixture contain optical isomers.

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

and humidified.
and dehumidified with increase in wet bulb temperature.
at the same relative humidity.
and dehumidified with decrease in wet bulb temperature.

A

and dehumidified with decrease in wet bulb temperature.

470
Q

The process employing desorption of the absorbed solute by a solvent is called

elution
osmosis
reverse osmosis
sublimation

A

elution

471
Q

If the overall efficiency and Murphree plate efficiency are equal, then both the equilibrium and operating lines are

straight
parallel
both (a) & (b)
neither (a) nor (b)

A

both (a) & (b)

472
Q

Which of the following operations does not involve leaching ?

Dissolving gold from ores.
Dissolving pharmaceutical products from bark or roots.
Dissolving sugar from the cells of the beet.
Removing nicotine from its water solution by kerosene.

A

Removing nicotine from its water solution by kerosene.

473
Q

The recovery of pencillin from the acidified fermentation broth is done by

distillation
evaporation
absorption
liquid extraction

A

liquid extraction

474
Q

Unit operation involved in the prilling of urea is

evaporation
drying
crystallisation
both (b) and (c)

A

both (b) and (c)

475
Q

Molecular seives are porous

alumina.
silica.
synthetic zeolites crystals/metal alumino-silicates.
none of these.

A

synthetic zeolites crystals/metal alumino-silicates.

476
Q

Calcium ammonium nitrate (a fertiliser) is dried in a __________ dryer.

rotary
vacuum
tunnel
tray

A

rotary

477
Q

A binary mixture of benzene and cyclohexane is separated by

flash vaporisation
extractive distillation
solvent extraction
ordinary distillation

A

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

mass transfer is accompanied by reaction.
diffusion of A is in stagnant medium B.
molecular mean free path is high.
there is equimolar counter diffusion.

A

there is equimolar counter diffusion.

479
Q

Cox chart is useful in the design of

distillation column
evaporator
dryer
crystalliser

A

distillation column

480
Q

Dew point of an air-water vapor mixture

decreases with decrease in pressure.
at constant humidity & total pressure is fixed.
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.
all ‘a’, ‘b’ & ‘c’.

A

all ‘a’, ‘b’ & ‘c’.

481
Q

Can a cooling tower cool water below the wet bulb temperature of inlet air ?

yes
no
yes ; but height of cooling tower will be prohibitively high.
yes ; but the air flow rate should be excessively high.

A

no

482
Q

The solvent used in liquid-liquid extraction should have __________ less than one.

selectivity
distribution co-efficient
both (a) and (b)
neither (a) nor (b).

A

neither (a) nor (b).

483
Q

The suitable evaporator for concentration of foaming liquids is a __________ evaporator.

long tube
short tube
vacuum
falling film

A

long tube

484
Q

The ratio of Murphree plate efficiency to point efficiency is always > 1 in a __________ flow model.

plug
perfectly mixed
both (a) & (b)
neither (a) nor (b)

A

plug

485
Q

Tea percolation employs

liquid-liquid extraction
leaching
absorption
none of these

A

leaching

486
Q

Which of the following assumes constant molal vaporisation and overflow ?

McCabe-Thiele method
Ponchan-Savarit method
Enthalpy concentration method
Plate absorption column

A

McCabe-Thiele method

487
Q

Absorption factor, for a fixed degree of absorption from a fixed amount of gas should be

1
> 1
< 1
≤ 1

A

> 1

488
Q

Selectivity of the solvent used in solvent extraction should be

1
> 1
< 1
0

A

> 1

489
Q

Pick out the wrong statement pertaining to leaching.

Fine solids can not be leached in a Pachuka tank.
Door classifier can be used for leaching of coarse solids.
Vegetable seeds can be leached in either of Bollman extractor, Rotocel or Kennedy extractor.
Very high temperature is not needed for the leaching of sugar beet.

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.

100
50
78
none of these

A

100

491
Q

NSc/NPr is called the

psychrometric ratio
Lewis number
Sherwood number
Stantan number

A

Lewis number

492
Q

McCabe-Thiele method

uses molal units for material and energy balance.
uses weight fractions to express liquid and vapour composition.
can use any type of units.
is more accurate than Ponchan-Savarit method.

A

uses molal units for material and energy balance.

493
Q

The film penetration model of mass transfer was enunciated by

Gilliland
Toor and Marchello
Stefan
Fick

A

Toor and Marchello

494
Q

The most economical range of absorption factor is

0 to 0.5
0 to 3
1.25 to 2
5 to 15

A

1.25 to 2

495
Q

Channelling is most severe

in towers packed with stacked packing.
in towers packed randomly with crushed solids.
in dumped packing of regular units.
at very high liquid flow rate.

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

not possible in the second case unless vacuum is applied.
not possible in the second case unless high pressure is applied.
more readily done in the second case compared to first one.
none of these

A

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

497
Q

‘ADDUCTS’ and ‘CLATHRATES’ are used in case of

extractive distillation.
crystallisation.
absorption.
none of these.

A

crystallisation.

498
Q

Adsorption is an unit operation which generally involves __________ systems.

liquid-solid
gas-solid
fluid-solid
solid-solid

A

fluid-solid

499
Q

In case of __________ distillation, a solvent is added to alter the relative volatility of the mixture to be separated.

molecular
azeotropic
extractive
flash.

A

extractive

500
Q

Separation of the isotopes of helium for scientific investigations is done by

reverse osmosis
thermal diffusion
leaching
solvent extraction

A

thermal diffusion

501
Q

In a binary system, separation is very efficient, when the relative volatility is

1
> 1
< 1
0.5

A

> 1

502
Q

Fenske-Underwood equation used for calculating the minimum number of theoretical plates in distillation column is valid for

constant molal overflow
total reflux
constant relative volatility
all (a), (b) and (c)

A

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

503
Q

The binary diffusivity in gases does not depend upon the

pressure
temperature
nature of the components
none of these

A

none of these

504
Q

Berl saddle made of carbon cannot be used for

alkalis
SO2
H2SO4
oxidising atmosphere

A

oxidising atmosphere

505
Q

1 kg of a saturated aqueous solution of a highly soluble component A at 60°C is cooled to 25°C. The solubility limits of A are (0.6 kgA/kg water) at 60°C and (0.2 kgA/kg water) at 25°C. The amount in kg of the crystals formed is

0.4
0.25
0.2
0.175

A

0.2

506
Q

During drying of a solid, the critical moisture content increases with

decreased drying rate
increased thickness of the solid
increased drying rate
both (b) and (c).

A

both (b) and (c).

507
Q

Priming in a distillation column

results from very low gas velocity.
is desirable from point efficiency consideration.
is characterised by the presence of foam throughout the space between trays.
reduces the overall pressure drop.

A

is characterised by the presence of foam throughout the space between trays.

508
Q

The commonly used solvent in supercritical extraction is

methyl ethyl ketone.
water.
carbon tetrachloride.
carbon dioxide.

A

carbon dioxide.

509
Q

When the liquid over a plate is of uniform concentration, then

Murphree efficiency > point efficiency.
Murphree efficiency < point efficiency.
Murphree efficiency = point efficiency.
Murphree efficiency ≠ point efficiency.

A

Murphree efficiency = point efficiency.

510
Q

In saturated gas, the

vapour is in equilibrium with the liquid at the gas temperature.
vapour is in equilibrium with the liquid at the room temperature.
partial pressure of vapour equals the vapour pressure of the liquid at room temperature.
none of these.

A

vapour is in equilibrium with the liquid at the gas temperature.

511
Q

As per Gilliland’s equation, the diffusivity is

directly proportional to ‘T^1.5’.
inversely proportional to ‘P’.
dependent on the molecular volume & molecular weight of components.
all ‘a’, ‘b’ & ‘c’.

A

all ‘a’, ‘b’ & ‘c’.

512
Q

Pick out the wrong statement.

When the concentration difference for the mass transfer becomes zero at the bottom of the gas absorption tower, then the upper end of the operating line touches the equilibrium curve.
The average distance between the operating line and equilibrium line is large, when the liquid-gas ratio is also large in case of a counter current gas absorption tower.
The operating line lies above the equilibrium curve in case of a gas desorber.
With decrease in the liquid flow rate for a fixed gas flow rate, the slope of the operating line decreases, in case of gas absorption process.

A

The operating line lies above the equilibrium curve in case of a gas desorber.

513
Q

A mixture of 10% C6H6 vapour in air at 25°C and 750 mm Hg has a dew point of 20°C. Its dew point at 30°C and 700 mm Hg will be around __________ °C.

21.7
20
27.3
18.7

A

18.7

514
Q

Which of the following is not fixed by the process requirements, in the design of absorbers ?

Flow rate of the entering gas.
Composition of the entering liquid.
Terminal concentrations of gas stream.
None of these.

A

None of these.

515
Q

If the amount of the steam used in steam distillation is increased, the temperature of distillation

increases
decreases
remains unchanged
depends on relative volatility

A

decreases

516
Q

moisture in a solid exerting an equilibrium vapour pressure equal to that of the pure liquid at the same temperature is called the __________ moisture.

unbound
critical
free
bound

A

unbound

517
Q

Inside the distillation columns, the

highest temperatures is near the feed plate.
driving force for the liquid flow is its weight.
vapors are not always at their dew points.
all (a), (b) and (c)

A

driving force for the liquid flow is its weight.

518
Q

When the psychometric ratio is __________ then the adiabatic saturation temperature and wet bulb temperature becomes equal.

1
< 1
> 1

A

1

519
Q

Desirable value of absorption factor in an absorber is

1
< 1
> 1
0.5

A

> 1

520
Q

Refractory bricks are usually dried in a __________ dryer.

tray
tunnel
conveyor
festoon

A

tunnel

521
Q

For __________ drying, the effects of velocity, temperature and humidity of the gas and the thickness of the solid are the same.

unsaturated surface
constant rate
both (a) and (b)
neither (a) nor (b).

A

both (a) and (b)

522
Q

What is the degree of freedom of an absorption process in which only one component is transferred between phases ?

3
2
4
1

A

3

523
Q

Sticky material can be dried in a __________ dryer.

tray
rotary
fluidised bed
none of these

A

tray

524
Q

Langmuir equation is associated with

leaching
adsorption
steam distillation
multicomponent absorption.

A

adsorption

525
Q

During the constant rate period of drying of a solid,

increased air humidity decreases the rate of drying.
increasing the air temperature decreases the drying rate.
surface evaporation of unbound moisture occurs.
none of these.

A

surface evaporation of unbound moisture occurs.

526
Q

At a fixed total pressure, humidity depends only on the

partial pressure of vapour in the mixture.
heat capacity of the vapour.
density of the vapour.
none of these.

A

partial pressure of vapour in the mixture.

527
Q

If moisture content of solid on dry basis is X, then the same on wet basis is

x/(x+1)
x/(1-x)
(1+x)/x
(1-x)/x

A

x/(x+1)

528
Q

Flash distillation is

same as differential distillation.
used for multicomponent systems like crude refining.
same as simple distillation.
most useful for handling binary systems.

A

used for multicomponent systems like crude refining.

529
Q

__________ developed the film theory.

Higbie
Fick
Ergun
Levenspeil

A

Higbie

530
Q

For absorbers, high pressure drop results in

increased efficiency.
decreased efficiency.
high operating cost.
better gas liquid contact.

A

high operating cost.

531
Q

Which of the following parameters remains almost constant during adiabatic saturation of unsaturated air ?

Dry bulb temperature
Dew point
Wet bulb temperature
None of these

A

Wet bulb temperature

532
Q

Coffee is prepared from coffee beans by leaching with

cold water
hot water
dilute hot caustic solution
naphtha

A

hot water

533
Q

Gaseous diffusion co-efficient increases with increase in the

pressure
temperature
both (a) & (b)
neither (a) nor (b)

A

temperature

534
Q

With increase in absolute humidity, the dew point of an unsaturated mixture of air and water vapor (at constant pressure and temperature)

increases
remains unchanged
decreases
decreases linearly

A

increases

535
Q

If xD = overhead product molal composition and RD = reflux ratio, then slope and intercept of the operating line for rectifying section are respectively

xD/ (RD+1) , RD/ (RD+1)
RD/ (RD+1) , xD/ (XD+1)
xD/ (RD+1) , (RD+1)/ RD

A

RD/ (RD+1) , xD/ (XD+1)

536
Q

Pick out the wrong statement. Raoult’s law does not apply, when the

size of component molecules are not equal.
attractive forces between like and unlike molecules in the solution are approximately equal.
component molecules are nonpolar.
chemical combination or molecular association between unlike molecules takes place in the formation of solution.

A

component molecules are nonpolar.

537
Q

Water-ethyl alcohal solution can be concentrated (in respect of alcohal concentration) by __________ distillation.

atmospheric
vacuum
high pressure
none of these

A

vacuum

538
Q

L/mGis the expression for

absorption factor
Brinkman number
slope of operating line in absorber
slope of operating line in stripper.

A

absorption factor

539
Q

Extraction of pencillin employs a __________ extraction coloumn.

centrifugal
packed
plate
None of these.

A

centrifugal

540
Q

In case of gases, the binary diffusivity is proportional to (where, P = pressure)

P
1/P
1/(P)^1/2
(P)^1/2

A

1/P

541
Q

When the gas to be dissolved in liquid is a/an __________ then normally co-current adsorber are used.

mixture of two gases
pure gas
ideal gas
sparingly soluble gas

A

pure gas

542
Q

Corresponding to Prandtl number in heat transfer, the dimensionless group in mass transfer is the __________ number.

Schmidt
Sherwood
Peclet
Stanton

A

Schmidt

543
Q

If a two phase system is in physical equilibrium; then it means that, the

escaping tendency of each component from the liquid phase to the vapor phase is exactly equal to that from vapor phase to liquid phase.
temperature of the liquid phase is equal to that of the vapor phase.
total pressure throughout the liquid phase is equal to that throughout the vapor phase.
all (a), (b) and (c).

A

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

544
Q

McCabe-Thiele method of binary distillation does not assume that the

sensible heat changes are negligible compared with latent heat changes.
molar latent heats of all components are equal.
heat of mixing is negligible.
none of these

A

none of these

545
Q

(NSh/NRe.NSc) is termed in mass transfer operation as the

Stanton number
Peclet number
thermal diffusivity
momentum diffusivity

A

Stanton number

546
Q

The Hatta number is important in

multicomponent distillation.
binary distillation.
gas absorption without chemical reaction.
gas absorption with chemical reaction.

A

gas absorption with chemical reaction.

547
Q

When a multistage tray tower uses a minimum reflux ratio, it implies

infinite trays and maximum reboiler heat load.
infinite trays and minimum reboiler heat load.
minimum trays and minimum reboiler heat load.
minimum trays and maximum reboiler heat load

A

infinite trays and minimum reboiler heat load.

548
Q

CO2 can be absorbed by

hot cupric oxide
heated charcoal
cold Ca(OH)2
alumina

A

heated charcoal

549
Q

For the same process conditions, the reflux ratio of an unlagged distillation column

decreases in winter
increases in winter
increases in summer
none of these

A

increases in winter

550
Q

An ideal tower packing should not

have low weight per unit volume.
have large surface area per unit volume.
have large free cross-section.
hold up large amount of liquid in the packing.

A

hold up large amount of liquid in the packing.

551
Q

Which of the following is a suitable absorbent for removal of H2S from natural gas ?

Vetrocoke solution
Monoethanol amine (MEA)
Dilute
Hot water

A

Monoethanol amine (MEA)

552
Q

Acetone is to be removed from air in an isothermal dilute absorber using pure water as solvent. The incoming air contains 5 mole% of acetone (yin = 0.05). The design equation to be used for obtaining the number of trays (N) of the absorber is, N+2 = 6 log (yin/yout).For 98% recovery of acetone, the number of trays required is/are

1
8
9
10

A

9

553
Q

Schimdt number and Lewis number for pure air at atmospheric conditions are respectively

< 1 and ≈ 1
1 and 0
>1 and ≈ 1
0 and ≈ 1

A

< 1 and ≈ 1

554
Q

Below is given an equilibrium moisture curve of a substance. State which regions represent free moisture and unbound moisture respectively.
(insert graph here S12P1)

II, III
II, IV
IV, III
IV, II

A

II, III

555
Q

Molecular diffusion is caused by the

transfer of molecules from low concentration to high concentration region.
thermal energy of the molecules.
activation energy of the molecules.
potential energy of the molecules.

A

thermal energy of the molecules.

556
Q

At __________ reflux, theoretical number of plates in a distillation coloumn is calculated using Fenske-Underwood equation.

operating
total
minimum
maximum permissible

A

total

557
Q

Separation of a mixture of two gases by absorption in the liquid solvent depends upon the difference in their

viscosity
density
solubility
relative volatility

A

solubility

558
Q

Components, having widely different boiling point in a binary mixture, can be separated using __________ distillation.

molecular
extractive
steam
simple

A

simple

559
Q

Which of the following equipments is not used in liquid-liquid extraction ?

Pachuka tank
Agitated vessels
Centrifugal extractors
Packed towers

A

Pachuka tank

560
Q

Pick out the wrong statement.

Packed towers are preferred for vacuum operation, because the pressure drop through the packing is less and they (packings) also lessen the possibility of tower wall collapse.
Packed towers are preferred over plate towers for handling corrosive and foamy liquids.
Diameter of randomly packed tower is normally more than 1.2 metres.
Due to uneven supply and improper distribution of liquid, problem of channeling, loading & flooding is generally encountered in packed towers.

A

Diameter of randomly packed tower is normally more than 1.2 metres.

561
Q

Equilibrium-moisture curves of different solids

are different
are same
depend on the humidity of the gas
none of these

A

are differenT

562
Q

Azeotropism for ethyl alcohol-water system disappears by

increasing temperature
decreasing pressure
increasing pressure
no means

A

decreasing pressure

563
Q

Degree of freedom for leaching and solvent extraction process is

1
3
0
2

A

3

564
Q

Diffusion co-efficient generally depends upon the temperature, pressure & the nature of the components of the system. Its dimension is not the same as that of the

mass transfer co-efficient.
thermal diffusivity.
kinematic viscosity.
volumetric diffusivity.

A

mass transfer co-efficient.

565
Q

Equilibrium moisture of a solid is equal to the total moisture minus free moisture. Which of the following substances will have maxi-mum equilibrium moisture ?

Anthracite coal
Rag paper
Bamboo
Inorganic solids

A

Bamboo

566
Q

In the absorption of ammonia in water, the main resistance to absorption is by the __________ phase.

liquid
gas
both (a) & (b)
neither (a) nor (b)

A

both (a) & (b)

567
Q

Drying of refractory is normally carried out in a __________ dryer.

open pan
tray
rotary vacuum
truck/tunnel.

A

truck/tunnel.

568
Q

The expression, ln(F/W) = ∫dx/(y*-x) from xW to xF is

differential distillation equation
for NtoG in absorption for dilute mixture
slope of q-line in McCabe-Thiele method
for relative volatility

A

differential distillation equation

569
Q

Heat sensitive materials with very high latent heat of vaporisation may be economically separated using

liquid extraction
distillation
evaporation
absorption

A

liquid extraction

570
Q

When the solvent dissolves very little of solute, then

solvent of low latent heat of vaporisation should be used.
solvent of low freezing point should be used.
large quantity of solvent is required to extract the solute.
very small quantity of solvent is required.

A

large quantity of solvent is required to extract the solute.

571
Q

An alkaline solution is used to reduce the concentration of carbon dioxide in a stream from 10% to 0.1% by absorption with irreversible chemical reaction. The overall number of transfer units based on gas phase is

9.21
4.605
100
0.001

A

4.605

572
Q

HETP is numerically equal to HTU, only when the operating line

lies below the equilibrium line.
lies above the equilibrium line.
and equilibrium lines are parallel.
is far from the equilibrium line.

A

and equilibrium lines are parallel.

573
Q

In a distillation operation, what is the effect of the temperature of the reflux stream (given below) on the condenser and reboiler loads ?
Reflux conditions:
(i) Reflux stream is completely liquid and is at its bubble point.
(ii) Reflux stream is below its bubble point.

Condenser and reboiler loads are the same in both the cases.
Reboiler load is the same in both the cases but condenser load is higher in case (ii).
Condenser load is the same in both the cases but reboiler load is higher in case (ii).
Both condensor and reboiler loads are higher in case (ii) as compared to case (i).

A

Both condensor and reboiler loads are higher in case (ii) as compared to case (i).

574
Q

Steady state equimolal counter diffusion occurs in case of

leaching
absorption
binary phase distillation
liquid-liquid extraction

A

binary phase distillation

575
Q

JD factor for mass transfer is a function of Reynolds number. Mass transfer by molecular diffusion from a single drop to surrounding still air is given by

Nsh = 2
Nst = 2
Nsc = 2
none of these

A

Nsh = 2

576
Q

The relative saturation of an unsaturated mixture of gas and vapor is independent of the

nature of the vapor.
temperature of the mixture.
composition of the mixture.
none of these.

A

none of these.

577
Q

The adiabatic saturation curve for a vapour-gas mixture is

straight line.
slightly concave upward.
slightly concave downward.
none of these.

A

slightly concave upward.

578
Q

Pick out the wrong statement.

Cellulose acetate membranes are used in dialysis process.
Elutriation process refers to when the soluble material is largely concentrated on the surface of an insoluble solid and is simply washed off by the solvent.
‘Cascade’ means a group of stages interconnected so that various streams flow from one to another.
Zirconia probe is used for the humidity measurement.

A

Zirconia probe is used for the humidity measurement.

579
Q

The value of NA/(NA + NB), for steady state equimolal counter diffusion of two gases ‘A’ and ‘B’ is

1

0.5
2

A

580
Q

Drift in a cooling tower is

the water entrained by the circulating air.
dependent on the water lost by evaporation.
desirable.
all (a), (b) & (c).

A

the water entrained by the circulating air.

581
Q

With increase in the concentration of the adsorbate, the integral heat of adsorption

increases.
decreases.
remains unchanged.
may increase or decrease ; depends on the type of adsorbate.

A

decreases.

582
Q

Small dia distillation column can be a

packed column
sieve tray
bubble cap
any of these

A

packed column

583
Q

If mass diffusivity in a mixture is equal to the thermal diffusivity, then the Lewis number is

0
1
< 1
> 1

A

1

584
Q

An air-water vapour mixture has a dry bulb temperature of 60°C and a dew point temperature of 40°C. The total pressure is 101.3 kPa and the vapour pressure of water at 40°C and 60°C are 7.30 kPa and 19.91 kPa respectively.The humidity of air sample expressed as kg of water vapour/kg of dry air is

0.048
0.079
0.122
0.152

A

0.152

585
Q

__________ column is used in gas absorption process.

Wetted wall
Seive/perforated tray
Bubble cap
Packed

A

Packed

586
Q

Nitrobenzene (boiling point = 210.6°C) is steam distilled at 1 atm pressure.Nitrobenzene will distill off __________ °C.

at < 100
at > 210.6
between 100 and 210
none of these

A

at < 100

587
Q

Pick out the wrong statement.

With decrease in feed temperature, the number of plates required for binary distillation decreases for a given L/V ratio.
The extraction per unit of total height for a short packed column is more effective than for a tall column, in case of liquid-liquid extraction.
Natural draft cooling towers are made of ferro-concrete and its cross-section is wider at the bottom.
Vanderwall adsorption is also called chemisorption.

A

Vanderwall adsorption is also called chemisorption.

588
Q

At what value of reflux ratio, number of theoretical plates in a distillation column is minimum ?

0
1

< 1

A

589
Q

Batch tray dryers suffers from the disadvantage of

high maintenance cost.
non-uniform & low production rate.
high labour cost & low heat economy.
all ‘a’, ‘b’ & ‘c’.

A

high labour cost & low heat economy.

590
Q

In a moderately sized packed absorption tower, channeling (which is most severe with stacked packings) can be minimised by taking the ratio of tower diameter to packing diameter

> 4:1
<8:1
8:1
<6:1

A

> 8:1

591
Q

__________ column is preferred to be used, when a high liquid hold up is required in a reactor for gas-liquid reaction.

Packed
Bubble
Spray
Tray

A

Bubble

592
Q

The ‘shanks system’ of leaching (i.e., counter-current multiple contact leaching) is used for

recovery of tannis from the tree barks and woods.
leaching sodium nitrate from Chilean nitrate bearing rock.
both (a) and (b).
neither (a) nor (b).

A

both (a) and (b).

593
Q

Penetration model (theory) for mass transfer was enunciated by

Danckwerts
Toor and Marchello
Higbie
Kissinevskii

A

Higbie

594
Q

Surface renewal model of mass transfer was enunciated by

Toor and Marchello
Fick
Danckwerts
Stefan

A

Danckwerts

595
Q

When the __________ the relative humidity of air decreases, despite an increase in the absolute humidity.

temperature rises
pressure rises
temperature falls
pressure falls

A

temperature rises

596
Q

For turbulent mass transfer in pipes, the Sherwood number depends on the Reynolds number as

Re^0.33
Re^0.53
Re^0.83
Re

A

Re^0.83

597
Q

The relative humidity of air decreases in-spite of an increase in the absolute humidity, when the

temperature rises.
pressure rises.
temperature falls.
pressure falls.

A

temperature rises.

598
Q

Unit of molal diffusivity is

cm%2/sec gm . mole
gm moles/cm^2 . sec
gm moles/cm. sec
gm moles/cm^2. sec

A

gm moles/cm. sec

599
Q

The term “approach” in a cooling tower refers to the difference in the temperature of the

cold water leaving the tower and the wet bulb temperature of the surrounding air.
hot water entering the tower and the wet bulb temperature of the surrounding air.
hot water entering and the cooled water leaving the cooling tower.
none of these

A

cold water leaving the tower and the wet bulb temperature of the surrounding air.

600
Q

Binary distillation involves the mass transfer by __________ at the gas-liquid interface.

unidirectional diffusion from liquid to gas phase
unidirectional diffusion from gas to liquid phase
either ‘a’ or ‘b’
a counter diffusion at an almost equal molar rate

A

a counter diffusion at an almost equal molar rate

601
Q

In a gas-liquid absorption coloumn, for obtaining the maximum absorption efficiency

liquid stream should be distributed uniformly.
gas stream should be distributed uniformly.
both gas as well as liquid streams should be distributed uniformly.
by passing should be completely avoided.

A

both gas as well as liquid streams should be distributed uniformly.

602
Q

Reverse osmosis is also called

dialysis
electrodilysis
diffusion
ultrafiltration.

A

ultrafiltration.

603
Q

Which of the following is not a batch drier?

Truck drier
Agitated pan drier
Fluidised bed drier
Vacuum shelf drier

A

Fluidised bed drier

604
Q

Steam distillation is not recommended to be used, if the

azeotropic mixture is to be separated and the final product is miscible with water.
liquids decompose, if distilled directly at atmospheric pressure.
material can not be distilled by indirect heating even under low pressure, because of the high boiling temperature.
material to be distilled is thermally unstable or has the tendency to react with other components associated with it, at the boiling temperature.

A

azeotropic mixture is to be separated and the final product is miscible with water.

605
Q

Rayleigh equation applies to __________ distillation.

differential
flash
equilibrium
molecular

A

differential

606
Q

Mass transfer co-efficient ‘K’ according to penetration theory varies with mass dif-fusivity as

D^0.5
D
1/D
D^1.5

A

D^0.5

607
Q

Most important factor to be considered in the selection of packings for absorbers is the __________ of packing.

size
durability
porosity
cost

A

porosity

608
Q

__________ is the separation technique used for desalination of sea water.

Thermal diffusion
Reverse osmosis
Adsorption
absorption

A

Reverse osmosis

609
Q

The relative saturation of a partially saturated mixture of vapour and gas can be increased by __________ of the mixture.

reducing the total pressure
increasing the total pressure
reducing the temperature
both (b) and (c)

A

both (b) and (c)

610
Q

Danckwerts developed the __________ theory.

penetration
surface renewal
film
none of these

A

surface renewal

611
Q

Molecular distillation is

high temperature distillation
for heat-sensitive materials
very low pressure distillation
both (b) and (c)

A

both (b) and (c)

612
Q

Drying of a wet solid under constant drying conditions means the exposure of the wet solid to the air of constant

humidity
velocity
temperature
all (a), (b) & (c)

A

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

613
Q

Which of the following provides maximum contact surface for a liquid-vapour system?

Packed tower
Bubble-cap plate column
Seive-plate column
Wetted wall column

A

Packed tower

614
Q

For experimental determination of mass transfer co-efficient by wetted wall tower, the mass transfer area is

calculated
unknown
known
not required

A

known

615
Q

In stripping section of continuous distillation column, the

liquid is stripped of high boiler.
liquid is enriched with high boiler.
vapour is stripped of low boiler.
none of these.

A

liquid is enriched with high boiler.

616
Q

Molality is defined as the number of gm moles of solute per __________ of solvent.

litre
gm
Kg
m^3

A

Kg

617
Q

__________ is concerned with the adsorption equilibria.

Fick’s law
Gibb’s equation
Freundlich equation
none of these

A

Freundlich equation

618
Q

Which of the following is the correct ternery diagram for liquid-liquid extraction system comprising of one pair partly soluble (e.g. water-benzene-acetic acid in which A-diluent, B - solvent and C - solute)?

(insert image here S13P4)
(insert image here S13P4)
(insert image here S13P4)
(insert image here S13P4)

A

(insert image here S13P4)

619
Q

Fractional solvent extraction

employs only one solvent
employs two solvents
results in low interfacial tension
none of these

A

employs two solvents

620
Q

In the layout plan for a vacuum distillation unit, operating at 60 mm Hg, supported by a barometric condenser, the appropriate place for the location of vacuum drum for collecting the distillate will be

at ground level.
2 metres above the ground.
5 metres above ground.
10 metres above ground.

A

at ground level.

621
Q

Raschig ring made of procelain cannot be used for treating concentrated

hydrochloric acid
nitric acid
alkalis
sulphuric acid

A

alkalis

622
Q

H2S present in naphtha reformed gas is removed by absorbing with

ethanolamine
K2CO3
HCl
vacuum gas oil

A

ethanolamine

623
Q

During constant rate drying period, vaporisation rate per unit drying surface area

decreases with time.
increases with time.
does not change with time,
does not affect the moisture content of the wet solid.

A

does not change with time,

624
Q

Pick out the wrong statement.

Mass transfer co-efficient does not account for gase-liquid diffusion.
Diffusion co-efficient and mass transfer co-efficient are not same in any mass transfer operation.
Contacting cold vapor-gas mixture with hot liquid exemplifies humidification process.
Contacting cold liquid with warm vapor-gas mixture exemplifies dehumidification process.

A

Mass transfer co-efficient does not account for gase-liquid diffusion.

625
Q

In rectifying section of a continuous distillation column, the

vapour is enriched with low boilers.
vapour is enriched with high boilers.
liquid is stripped of high boilers.
none of these.

A

vapour is enriched with high boilers.

626
Q

According to Chilton-Colburn analogy for mass transfer, NSt.NSc2/3 is equal to

f
f/2
2f
1/f

A

f/2

626
Q

For a fixed number of ideal stages in a distillation column, as the reflux ratio is increased, the difference in composition between the top and bottom product streams

increases
decreases
remains unaffected
passes through a maximum

A

increases

627
Q

A pure drug is administered as a sphere and as a cube. The amount of drug is the same in the two tablets. Assuming that the shape and size do not influence the mass transfer, the ratio of rate of dissolution in water at t = 0 for the cubic to spherical tablet is

0.54
1.04
1.24
1.94

A

1.24

628
Q

Minimum reflux ratio in a distillation column results in

optimum number of trays.
minimum reboiler size.
maximum condenser size.
minimum number of trays.

A

maximum condenser size.

629
Q

Flooding in a distillation column is detected by a sharp

increase in Murphree plate efficiency.
decrease in pressure drop.
decrease in liquid hold up in the coloumn.
increase in pressure drop.

A

increase in pressure drop.

630
Q

In extraction, as the temperature increases, the area of hetrogeneity (area covered by binodal curve)

decreases
increases
remains unchanged
none of these

A

decreases

631
Q

Pick out the wrong statement.

The mass diffusivity, the thermal diffusivity and the eddy momentum diffusivity are the same for NSc = NPr = 1.
1 Nm^3 of dry air is lighter than 1Nm^3 of humid air.
The Lewis number of a mixture is unity, when the thermal diffusivity is equal to the mass diffusivity.
An azeotropic mixture of two liquids has boiling point higher than either of them, when it shows negative deviation from Raoult’s Law.

A

1 Nm^3 of dry air is lighter than 1Nm^3 of humid air.

632
Q

In case of an unsaturated mixture of gas and vapor, the percentage saturation is __________ its relative saturation.

lower than
higher than
equal to
either (a) or (b), depends on the mixture composition

A

lower than

633
Q

At constant pressure, with increase of temperature, the dew point will

increase
decrease
remain unchanged
increase/decrease ; depends on the temperature

A

increase

634
Q

For a single component absorber, the operating line is straight only when plotted in term of __________ units.

partial pressure
mole ratio
mole fraction
none of these

A

mole ratio

635
Q

In case of unsaturated air

dew point < wet bulb temperature
wet bulb temperature < dry bulb temperature
both (a) and (b)
neither (a) not (b)

A

both (a) and (b)

636
Q

For a binary mixture with low relative volatility,

use steam distillation.
use molecular distillation.
use high pressure distillation.
an azeotrope may be formed during distillation.

A

an azeotrope may be formed during distillation.

637
Q

Plate efficiency

is a function of the mass transfer between liquid and vapour.
increases due to foaming.
increases due to liquid entrainment.
increases due to weeping and dumping of liquid.

A

is a function of the mass transfer between liquid and vapour.

638
Q

Absorption accompanied by heat evolution results in

increased capacity of the absorber.
increase in equilibrium solubility.
decrease in equilibrium solubility.
none of these.

A

decrease in equilibrium solubility.

639
Q

Even though bubble cap towers are very effective for humidification operation, they are not used commonly in industries, because of the

high evaporation losses of water.
high pressure drop of the gas.
difficulty in its fabrication.
none of these.

A

high pressure drop of the gas.

640
Q

For a distillation column operating at minimum reflux, the

concentration of liquid and vapour leaving a plate will be same.
reflux ratio will be maximum.
number of plates required will be maximum.
none of these.

A

number of plates required will be maximum.

641
Q

A solid is being dried in the linear drying rate regime from moisture content Xo to XF. The drying rate is zero at X = 0 and the critical moisture content is the same as the initial moisture Xo. The drying time for M = (Ls/ARc) is (where, L = total mass of dry solid, A = total surface area for drying Rc = Constant maximum drying rate per unit area X = moisture content (in mass of water/mass of dry solids))

M(Xo - XF)
M(Xo/XF)
M ln(Xo/XF)
MXo ln(Xo/XF)

A

MXo ln(Xo/XF)

642
Q

Flash distillation is suitable for the separation of components

having very close boiling points.
which form maximum boiling azeotrope.
having very wide boiling points.
which form minimum boiling azeotrope.

A

having very wide boiling points.

643
Q

In Mcabe-Thiele method, at infinite reflux ratio

number of plates is maximum.
overhead product is maximum.
both the operating lines coincide with the diagram.
none of these.

A

both the operating lines coincide with the diagram.

644
Q

Leaching rate is independent of the

agitation
temperature
particle size
none of these

A

none of these

645
Q

Use of packed towers for distillation is generally limited to the

small sizes.
multicomponent distillation.
high pressure operation.
vacuum distillation.

A

small sizes.

646
Q

Pick out the wrong statement.

The binary diffusivity in liquids is of the order of 10^-5 cm^2 /sec.
Molecular diffusion in solid is much faster than that in liquids.
Particles movement from higher concentration to lower concentration takes place in diffusion process.
According to Poiseuille’s law, the permeability decreases with increase in temperature for flow of a gas through a given capillary.

A

Molecular diffusion in solid is much faster than that in liquids.

647
Q

Which of the following decreases during evaporative cooling process with recirculated water supply ?

Wet bulb temperature
Relative humidity
Partial pressure of vapour
None of these

A

None of these

648
Q

Laboratory determination of the dif-fusivity of vapor is done by __________ method.

wetted wall column
Gilliland’s
Winkel mann’s
Wike’s

A

Winkel mann’s

649
Q

The minimum liquid rate to be used in an absorber corresponds to an operating line

of slope = 1
of slope = 0.1
tangential to the equilibrium curve
none of these

A

tangential to the equilibrium curve

650
Q

Unsaturated air (with dry and wet bulb temperatures being 35 and 25°C respectively) is passed through water spray chamber maintained at 35°C. The air will be

cooled
humidified
both (a) & (b)
dehumidified

A

humidified

651
Q

For absorbing a sparingly soluble gas in a liquid, the

gas side co-efficient should be increased.
liquid side coefficient should be increased.
gas side co-efficient should be decreased.
liquid side co-efficient should be decreased.

A

liquid side coefficient should be increased.

652
Q

A natural draft cooling tower is filled with wooden grids, which covers about __________ percent of the tower height.

10-15
30-40
70-80
90-100

A

10-15

653
Q

The boiling points of pure components of a binary system __________ with increase in total pressure of the system.

decreases
increases
remains unchanged
may increase or decrease, depends on the system.

A

increases

654
Q

The change in enthalpy, when a unit quantity of gas is absorbed by relatively large quantity of adsorbent (on which a definite concentration of the adsorbed gas already exists) is termed as the

differential heat of adsorption.
heat of wetting.
integral heat of adsorption.
none of these.

A

differential heat of adsorption.

655
Q

Penetration theory relates the average mass transfer co-efficient (K) with diffusivity (D) as

K ∝ D
K ∝ D^1/2
K ∝ D^1.5
K ∝ D^2

A

K ∝D^1/2

656
Q

Desulphurisation of petrol is done in a

Bollman extractor
rotating disc extractor
packed extraction column
plate type extraction column

A

rotating disc extractor

657
Q

Chemisorption compared to physical absorption has

lower adsorption rate.
lower capacity of the solvent for the solute gas.
increased utilization of stagnant zones of the liquid phase.
none of these.

A

increased utilization of stagnant zones of the liquid phase.

658
Q

Rate of adsorption increases as the

temperature increases.
temperature decreases.
pressure decreases.
size of adsorbent increases.

A

temperature decreases.

659
Q

Pick out the system with maximum boiling azeotrope at 1 atm.

acetone chloroform
ethyl alcohol-water
benzene-ethyl alcohol
none of these

A

acetone chloroform

660
Q

At 750°K and 1 atm, the approximate value of Schmidt number for air is

0.01
0.1
1
10

A

0.1

661
Q

Calculation of mass transfer co-efficient is mostly/normally done using __________ theory.

surface renewal
film
penetration
none of these.

A

film

662
Q

The velocity, concentration and temperature boundary, for the boundary layer development on a flat plate during connective mass transfer will be same, if

NSc = 1
NSc = NPr = NLe
NPr = NLe
NSc = NLe

A

NSc = NPr = NLe

663
Q

For the gas absorption, the height of a transfer unit, based on the gas phase is given by (G: superficial molar gas velocity, L: superficial molar liquid velocity, FG:mass transfer co-efficient, mols/m2 , a: in-terfacial area per unit volume of tower)

G/(FGa)
FG/(G
a)
(Ga)/FG
L/(FG
G)

A

G/(FG*a)

664
Q

Which of the following is used for the concentration of rubber latex ?

Agitated film evaporator
Long tube vertical evaporator
Short tube evaporator
Calendria

A

Agitated film evaporator

665
Q

As the reflux ratio, in a continuous counter-current extraction is increased, the number of stages

increase
decrease
remain unchanged
can either increase or decrease, depends on the system

A

decrease

666
Q

In triangular co-ordinates, the ternery composition point falls __________ of the triangle.

in the corners
inside
on the sides
none of these.

A

inside

667
Q

In a single stage extraction process, 10 kg of pure solvent S (containing no solute A) is mixed with 30 kg of feed F containing A at a mass fraction xf = 0.2. The mixture splits into an extract phase E and a raf-finate phase R containing A at xB = 0.5 and xR = 0.05 respectively. The total mass of the extract phase is (in Kg)

6.89
8.89
10
8.25

A

8.89

668
Q

Penetration theory states that the mass transfer co-coefficient is equal to (where, De is diffusivity and ‘t’ is time)

(De.t)^1/2
(De/t)^1/2
(4De/πt)^1/2
(4De/t)

A

(4De/πt)^1/2

669
Q

Reboiler is considered as one theoretical plate, because

of the assumption that vapour and liquid leaving the reboiler are in equilibrium.
vapour is recycled to the column.
reboiler itself contains one plate.
none of these.

A

of the assumption that vapour and liquid leaving the reboiler are in equilibrium.