Section 1 Flashcards

1
Q

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

A

chemical properties

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2
Q

In a solution containing 0.30 Kg mole of solute and 600 kg of solvent, the molality is

A

0.50

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3
Q

Fenske equation determines the

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

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 ?

A

Centrifugal extractor

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6
Q

Total reflux in a distillation operation requires minimum

A

number of plates

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7
Q

The difference of wet bulb temperature and adiabatic saturation temperature of unsaturated mixture of any system is

A

+ve

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8
Q

Fenske’s equation for determining the minimum number of theoretical stages in distillation column holds good, when the

A

relative volatility is reasonably constant.

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9
Q

When the temperature and humidity of air is low, we usually use __________ draft cooling tower.

A

natural

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10
Q

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

A

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

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11
Q

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

A

PACKED

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12
Q

13.
Overall efficiency of the distillation column is

A

the ratio of number of ideal plates to actual plates.

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13
Q

Which is the controlling factor for a drum drier?

A

heat transfer

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14
Q

Drying operation under vacuum is carried out to

A

reduce drying temperature.

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15
Q

Air initially at 101. 3 kPa and 40°C and with a relative humidity of 50%, is cooled at constant pressure to 30°C. The cooled air has a

A

higher relative humidity

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16
Q

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

A

absorption

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17
Q

At minimum reflux ratio for a given separation

A

number of plates is infinity.

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18
Q

Relative humidity is the ratio of the

A

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

19
Q

In batch distillation with constant reflux, overhead product composition __________ with time.

A

decreases

20
Q

Psychrometry deals with the properties of gas-vapor mixture. Humidity can be determined by the measurement of the __________ of a fibre.

A

electrical resistance

21
Q

Heat in BTU necessary to increase the temperature of 1 lb of gas and its accompanying vapour by 1°F is called the

A

specific heat

22
Q

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

A

increase ‘S’ and decrease ‘G’.

23
Q

The mass diffusivity, the thermal diffusivity and the eddy momentum diffusivity are same for, NPr = NSc = __________

A

1

24
Q

Dew point of a gas-vapour mixture

A

decreases with decrease in pressure.

25
Q

Which of the following plays an important role in problems of simultaneous heat and mass transfer ?

A

Lewis number

26
Q

In case of an absorber, the operating

A

line always lies above the equilibrium curve.

27
Q

As the reflux ratio in a distillation coloumn is increased from the minimum, the

A

total cost first decreases and then increases.

28
Q

Absorption factor is defined as (where, S1 = slope of the operating line S2 = slope of the equilibrium curve)

A

S1/S2

29
Q

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

A

0

30
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)

31
Q

Which of the following quantities need not be fixed before starting the design of a co-current absorber ?

A

Flow rate of entering liquid

32
Q

Mass transfer co-efficient of liquid is

A

affected more by temperature than that for gases.

33
Q

Absorption accompanied with chemical reaction is exemplified by the absorption of

A

SO2 in alkaline solution.

34
Q

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

A

Multicomponent distillation.

35
Q

Which of the following liquid-vapor contacting devices provides maximum contact surface area for a particular duty ?

A

Wetted wall column

36
Q

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

A

spray chamber

37
Q

Chemisorption (chemical adsorption) is

A

an irreversible phenomenon.

38
Q

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

A

D. all ‘a’, ‘b’ & ‘c’.

39
Q

Raoult’s law applies to the

A

solvents.

40
Q

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

A

allowable gas and liquid velocities.

41
Q

.
In distillation, overhead product contains

A

any number of components

42
Q

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

A

DECREASES

43
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).

44
Q

Mass transfer co-efficient (K) and diffusivity (D) are related according to film theory as

A

K ∝ D