Heat Transfer Flashcards

1
Q

Crystal size in a continuous crystalliser depends upon the
a. rate of heat transfer.
b. degree of turbulence.
c. degree of supersaturation.
d. all (a), (b) and (c).

A

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

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2
Q

Air is best heated with steam in a heat exchanger of

A

double pipe type with fin on air side.

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3
Q

Black liquor generated during paper manufacture is concentrated in a

A

multiple effect evaporator.

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4
Q

When vaporisation takes place directly at the heating surface, it is called

A

nucleate boiling

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5
Q

Steam consumption in kg/hr in case of an evaporator is given by (where, C & E are capacity the economy of the evaporator respectively)

A

C/E

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6
Q

Reynold’s analogy states that

A

Nst α f

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7
Q

With increase in temperature, the thermal conductivity of non-metallic amorphous solids

A

increases

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8
Q

Fourier’s law applies to the heat transfer by

A

conduction

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9
Q

Shell side pressure drop in a shell and tube heat exchanger does not depend upon the
a. baffle spacing & shell diameter.
b. tube diameter & pitch.
c. viscosity, density & mass velocity of shell side fluid.
d. none of these.

A

none of these.

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10
Q

In the equation Q = UAΔt; Δt is

A

logarithmic mean temperature difference.

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11
Q

With increase in porosity, the thermal conductivity of a solid substance

A

decreases

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12
Q

For an ideal black body

A

absorptivity = 1

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13
Q

In Joule’s experiment, an insulated container contains 20 kg of water initially at 25°C. It is stirred by an agitator, which is made to turn by a slowly falling body weighing 40 kg through a height of 4 m. The process is repeated 500 times. The acceleration due to gravity is 9.8 ms-2. Neglecting the heat capacity of agitator, the temperature of water (in °C) is

A

34.4

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14
Q

Fouling factor

A

accounts for additional resistances to heat flow.

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15
Q

In case of vertical tube evaporator, with increase in liquor level, the overall heat transfer co-efficient

A

decreases

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16
Q

The steam ejector is used to

A

create vacuum.

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17
Q

For shell and tube heat exchanger, with increasing heat transfer area, the purchased cost per unit heat transfer area

A

passes through a maxima

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18
Q

The thermal efficiency of a reversible heat engine operating between two given thermal reservoirs is 0.4. The device is used either as a refrigerator or as a heat pump between the same reservoirs. Then the coefficient of performance as a refrigerator (COP)R and the co-efficient of performance as a heat pump (COP)HP are

A

(COP)R = 1.5; (COP)HP = 2.5

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19
Q

Hot water (0.01 m3 /min) enters the tube side of a counter current shell and tube heat exchanger at 80°C and leaves at 50°C. Cold oil (0.05 m3/min) of density 800 kg/m3 and specific heat of 2 kJ/kg.K enters at 20°C. The log mean temperature difference in °C is approximately

A

32

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20
Q

In a heat exchanger, floating head is provided to

A

relieve stresses caused by thermal expansion.

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21
Q

Leidenfrost point is a term concerned with the

A

boiling of a liquid on a hot surface.

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22
Q

A process stream of dilute aqueous solution flowing at the rate of10 Kg.s-1 is to be heated. Steam condensate at 95°C is available for heating purpose, also at a rate of 10 Kg.s-1. A 1 - 1 shell and tube heat exchanger is available. The best arrangement is

A

counter flow with process stream on shell side.

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23
Q

Heat produced when a steady state current, I passes through an electrical conductor having resistance, ‘R’ is

A

I^2R

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24
Q

Pick out the wrong statement.

A

Orifice baffles are never used in a shell and tube heat exchanger.

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25
Q

Convective heat transfer co-efficient in case of fluid flowing in tubes is not affected by the tube length/diameter ratio, if the flow is in the __________ zone.

A

highly turbulent

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26
Q

The actual temperature drop across the heating surface in an evaporator depends on the

A

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

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27
Q

Which of the following is not used as a medium for high temperature heating?

A

mercury

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28
Q

Presence of a non-condensing gas in a condensing vapour

A

none of these.

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29
Q

Kirchoff s law applies to __________ radiation.

A

both (a) & (b)

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30
Q

With the increase of temperature, the Col-burn jH factor

A

increases.

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31
Q

In case of evaporators, liquid entrainment results primarily due to

A

foaming of the solution.

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32
Q

Baffles in the shell side of a shell and tube heat exchanger

A

increase the shell side heat transfer co-efficient.

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33
Q

Air is to be heated by condensing steam. Two heat exchangers are available (i) a shell and tube heat exchanger and (ii) a finned tube heat exchanger. Tube side heat transfer area are equal in both the cases. The recommended arrangement is

A

finned tube heat exchanger with air outside and steam inside.

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34
Q

The unit of heat transfer co-efficient in SI unit is

A

W/m2°K

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35
Q

The number of kg vaporised per kg of steam fed to the evaporator is defined as

A

economy

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36
Q

Pick out the wrong statement.

A

The equivalent diameter of heat transfer for a duct of square cross-section (having each side as ‘x’) is equal to 4x.

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37
Q

Economy of a multiple effect evaporator is not influenced much by the

A

boiling point elevations

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38
Q

Increasing the liquor level in the evaporator results in the

A

decreased capacity.

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39
Q

The equivalent diameter for pressure drop is __________ that for heat transfer.

A

smaller than

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40
Q

Controlling heat transfer film co-efficient is the one, which offers __________ resistance to heat transfer.

A

the largest

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41
Q

The heat flux (from outside to inside) across an insulating wall with thermal conductivity, K= 0.04 W/m.°K and thickness 0.16m is 10 W/m2. The temperature of the inside wall is - 5°C. The outside wall temperature is

A

35°C

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42
Q

Thermal conductivity of a conducting solid material depends upon its

A

both (a) & (b)

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43
Q

Pick out the wrong statement.

A

In case of a 1 - 2 shell and tube heat exchanger, the LMTD correction factor value increases sharply, when a temperature cross occurs.

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44
Q

The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film)

A

(ΔT)^1/4

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45
Q

Bulk of the convective heat transfer resistance from a hot tube surface to the fluid flowing in it, is

A

mainly confined to a thin film of fluid near the surface.

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46
Q

Which of the following is concerned with both heat and mass transfer?

A

Lewis relationship

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47
Q

A backward feed multiple effect evaporator is better than forward feed for concentrating cold feed, because it provides

A

higher economy

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48
Q

A 10 cm dia steam pipe, carrying steam at 180°C, is covered with an insulation (conductivity = 0.6 W/m.°C). It losses heat to the surroundings at 30°C. Assume a heat transfer co-efficient of 0.8 W/m2.°C for heat transfer from surface to the surroundings. Neglect wall resistance of the pipe and film resistance of steam. If the insulation thickness is 2 cms, the rate of heat loss from this insulated pipe will be

A

less than that of the uninsulated steam pipe.

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49
Q

Which area is used in case of heat flow by conduction through a cylinder?

A

Logarithmic mean area

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50
Q

Heat transfer by conduction results due to the transfer of free electrons, kinetic energy & vibrational energy from one molecule to another. Conduction heat transfer can not take place

A

between two bodies not in physical contact with each other.

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51
Q

The dimensionless group in mass transfer that is equivalent to Prandtl number in heat transfer is

A

Schmidt number.

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52
Q

Finned tube heat exchangers

A

give larger area per tube.

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53
Q

The absorptivity of a grey body at a given temperature __________ with increasing wavelength of radiation.

A

may increase or decrease ; depends on the material

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54
Q

Which one gives the monochromatic emissive power for black body radiation?

A

Planck’s law

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55
Q

For what value of Prandtl number, St = f/2?

A

1

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56
Q

In a shell and tube heat exchanger,

A

the temperature drops in the two fluids and the wall are proportional to individual resistances.

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57
Q

Dietus-Boelter equation used for the determination of heat transfer co-efficient is valid

A

for fluids in tubulent flow.

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58
Q

The equation, Nst = (f/2)/(1+5(NPr - 1)(sqrt*f/2)), corrosponds to __________ analogy.

A

Prandtl

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59
Q

For large heat transfer area requirement, shell and tube heat exchanger is preferred, because it

A

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

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60
Q

Out of the following four assumptions used in the derivation of the equation for LMTD [LMTD = (Δt1 - Δt2)/(ln(Δt1/Δt2))], which one is subject to the largest deviation in practice ?

A

Constant rate of fluid flow.

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61
Q

Heat flux increases with temperature drop beyond the Leiden frost point in the plot of heat flux vs. temperature drop for a boiling liquid, because

A

radiation becomes important

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62
Q

Resistance to heat flow by conduction is proportional to (where, t & ρ are thickness & density of the material respectively and A = area normal to the direction of heat flow.)

A

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

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63
Q

Temperature profile in steady state heat transfer is

A

linear

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64
Q

For the same heat load and mass flow rate in the tube side of a shell and tube heat exchanger, one may use multipass on the tube side, because it

A

increases the overall heat transfer coefficient.

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65
Q

When vaporisation takes place through a blanketting film of gas, the phenomenon is termed as __________ boiling.

A

film

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66
Q

Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter)

A

0.2 D

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67
Q

Stefan-Boltzman law which describes the radiation heat transfer states that, it is proportional to (where, t = temperature in °C T = absolute temperature in ° K)

A

T^4

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68
Q

The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

A

4.36

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69
Q

What is the unit of thermal conductivity?

A

Kcal/hr.m.°C

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70
Q

The thermal radiation emitted by a body is proportional to T^n, where T is its absolute temperature. The value of ‘n’ is exactly 4 for

A

all bodies

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71
Q

It is not preferable to use superheated steam in evaporators, because of its very

A

low film co-efficient

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72
Q

It is desired to concentrate a 20% salt solution (20 kg of salt in 100 kg of solution) to a 30% salt solution in an evaporator. Consider a feed of 300 kg/min at 30°C. The boiling point of the solution is 110°C, the latent heat of vaporisation is 2100 kJ/kg and the specific heat of the solution is 4 kJ/kg.K. The rate at which the heat has to be supplied in (kJ/min) to the evaporator is

A

3.06 x 10^5

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73
Q

LMTD for counterflow and prallel flow heat exchanger will be the same, when the

A

cold fluid is heated to a certain temperature by condensing steam (isothermal fluid).

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74
Q

For flow over a flat plate, the ratio of thermal boundary layer thickness, ‘xt’ and hydrodynamic boundary layer thickness ‘x’ is equal to (where, NPr = Prandtl number)

A

NPr^1/3

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75
Q

The range of electromagnetic spectrum important in heat transfer by radiation is __________ microns.

A

0.5-50

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76
Q

Use of transverse baffles in a shell and tube heat exchanger is done to increase the

A

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

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77
Q

The actual temperature drop across the heating surface of an evaporator depends on the

A

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

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78
Q

Economy of a multiple effect evaporator depends upon the

A

heat balance consideration

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79
Q

The Graetz number is concerned with the

A

heat transfer in laminar flow.

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80
Q

Solid angle subtended by the finite surface at the radiating element is

A

called the angle of vision.

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81
Q

Pick out the wrong statement.

A

The emissivity of a surface decreases, if it gets corroded by atmospheric environment.

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82
Q

In forced convection, the heat transfer depends on

A

Re, Pr

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83
Q

With increase in temperature, the thermal conductivity of most liquids

A

decreases

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84
Q

Heat transfer by __________ may not necessarily require the presence of a medium.

A

radiation

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85
Q

Pick out the correct statement.

A

Logarithmic mean area is used for calculating the heat flow rate through a thick walled cylinder.

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86
Q

In a shell and tube type heat exchanger, the floating tube bundle heat arrangement is used

A

in high range of temperature differences.

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87
Q

Stefan-Boltzman law applies to __________ body.

A

black

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88
Q

The film co-efficient is decreased due to the presence of non-condensing gases in the vapors. The film co-efficient of superheated vapor as compared to that of saturated vapor is

A

some

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89
Q

A perfect black body is a perfect __________ of radiation.

A

both (a) & (b)

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90
Q

In case of parallel flow heat exchanger, the lowest temperature theoretically attainable by the hot fluid is __________ the outlet temperature of the cold fluid.

A

equal to

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91
Q

An equipment which converts the latent or sensible heat of one fluid into the latent heat of vaporisation of another, is called a

A

heat exchanger

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92
Q

Which of the following is directly concerned with the heat transfer?

A

Grashoff number

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93
Q

Pick out the wrong statement:

A

With change in temperature, the radiant energy emitted by a black body remains unchanged.

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94
Q

Planck’s distribution law is valid for __________ bodies.

A

coloured

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95
Q

For hot feed, forward feeding as compared to backward feeding results in __________ economy.

A

increased

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96
Q

Radiation energy is emitted by all the substances, which are above

A

0°K

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97
Q

The interchange factor for radiation heat transfer from surface ‘x’ to surface ‘y’ in case of an infinite parallel planes with emis-sivities εx & εy is given by

A

(εx + εy)/(εx + εy - εx . εy)

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98
Q

What is the steam economy in case of a single effect evaporator system?

A

<1

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99
Q

If average heat transfer co-efficient is ha and the local coefficient at the end of the plate is hl then in case of heat transfer to a fluid flowing over a flat plate, heated over its entire length

A

ha = 2hl

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100
Q

jH factor for heat transfer is not a function of the __________ number.

A

both (b) & (c)

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101
Q

The Fourier number (defined as a.t/L2) is used in the analysis of problem involving heat transfer by

A

transient conduction

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102
Q

The energy radiated from a surface Q at absolute temperature T is related as

A

Q ∝ T^4

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103
Q

Baffles are provided in heat exchangers to increase the

A

heat transfer co-efficient

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104
Q

200 kg of solids (on dry basis) is subjected to a drying process for a period of 5000 seconds. The drying occurs in the constant rate period with the drying rate as, Nc = 0.5 x 10-3 kg/m2.s. The initial moisture content of the solid is 0.2 kg moisture/kg dry solid. The interfacial area available for drying is 4 m2/1000 kg of dry solid. The moisture content at the end of the drying period is (in kg moisture/kg dry solid)

A

0.1

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105
Q

In case of a vertical tube evaporator, with increase in the liquor level, the

A

capacity of the evaporator is decreased.

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106
Q

The ratio of total radiating power to the absorptivity of the body depends upon the __________ as per Kirchoffs law.

A

temperature of the body

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107
Q

For gases, the thermal conductivity increases with temperature rise. For liquids, with increase in concentration, its thermal conductivity generally

A

decreases

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108
Q

A 2-4 heat exchanger involves

A

both counter and parallel-flow of the fluids.

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109
Q

In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always

A

< 1

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110
Q

With increase in temperature, the thermal conductivity of steel

A

decreases

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111
Q

Which of the following forced convection heat transfer equation accounts for the liquid viscosity effect for viscous liquids?

A

Sieder-Tate equation

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112
Q

The main function of baffles provided in a shell and tube heat exchanger is to

A

enhance turbulence.

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113
Q

In a single effect evaporator, the economy is

A

< 1

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114
Q

LMTD correction factor which is to be applied for a cross-flow heat exchanger increases with increase in the number of shell passes. Its value for a single pass cross flow heat exchanger is

A

<1

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115
Q

Which of the following is not concerned with the heat transfer?

A

Schmidt number

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116
Q

Latent heat absorbed by 1 lb of water at 212°F, when it is changed to steam at 212°F, may be around __________ BTU.

A

180

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117
Q

In counter flow compared to parallel flow,

A

both (a) and (b).

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118
Q

The thermal radiative flux from a surface of emissivity = 0.4 is 22.68 kW/m2. The approximate surface temperature (K) is (Stefan-Boltzman constant = 5.67xl0-8 W/m2.K4)

A

1000

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119
Q

Crystallisation of solids from a homogeneous solution is a/an __________ process.

A

exothermic

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120
Q

A multiple effect evaporator has a capacity to process 4000 kg of solid caustic soda per day, when it is concentrating from 10% to 25% solids. The water evaporated in kg per day is

A

24000

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121
Q

Value of Prandtl number for water ranges from

A

5 to 10

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122
Q

Heat transfer in the laminar sublayer in case of a liquid flowing through a pipe, is mostly by

A

conduction

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123
Q

Among liquids, water has a comparatively high value of thermal conductivity, due to its

A

partial ionisation

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124
Q

Reynold’s analogy states that (where, St = Stanton number f = friction factor)

A

St = f/2

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125
Q

For evaporation of viscous solution in a multiple effect evaporator, the prefered feeding scheme is

A

backward

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126
Q

The sum of reflectivity and absorptivity for an opaque body is equal to

A

1

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127
Q

The film thickness for laminar film condensation on vertical surface __________ from top to bottom.

A

cummulatively increases

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128
Q

In case of a multipass shell and tube heat exchanger, providing a baffle on the shell side __________ the heat transfer rate.

A

increases

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129
Q

The local surface conductance for laminar film condensation on vertical surface is (where, t = film thickness)

A

∝ 1/t

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130
Q

Heat transfer co-efficient (h1) for liquids increases with

A

increasing temperature.

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131
Q

A diathermaneous substance __________ the thermal radiation completely.

A

transmits

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132
Q

A hot body will radiate heat most rapidly, if its surface is

A

black & rough

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133
Q

Evaporation of 1kg of water from a solution in a single effect evaporator requires about __________ kg of steam.

A

1-1.3

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134
Q

A metal wire of 0.01 m dia and thermal conductivity 200 W/m.K is exposed to a fluid stream with a convective heat transfer coefficient of 100 W/m2.K. The Biot number is

A

0.025

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135
Q

Analogy between mass and heat transfer is not applicable in case of

A

both (b) and (c).

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136
Q

A __________ surface has the maximum thermal emissivity out of the following.

A

black & rough

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137
Q

Radiant energy received by a body is proportional to (where, d = the distance between the object emitting radiation and that receiving it.)

A

d^2

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138
Q

Mechanical recompression evaporation is used in the production of

A

distilled water

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139
Q

A measure of the extent to which viscous heating is important relative to the heat flow resulting from the impressed temperature difference is represented by the __________ number.

A

Brinkman

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140
Q

Out of 100 kcal/second of incident radiant energy on the surface of a thermally transparent body, 300 kcal/second is reflected back. If the transmissivity of the body is 0.25, the emissivity of the surface will be

A

0.45

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141
Q

The purpose of providing a ‘catchall’ in the vapor line of an evaporator is to

A

arrest the entrained liquid

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142
Q

What is the thermal conductivity of a perfect heat insulator?

A

zero

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143
Q

Fouling factor’ used in the design of a multipass shell and tube heat exchanger is a

A

factor of safety.

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144
Q

A fluid is flowing inside the inner tube of a double pipe heat exchanger with diameter ‘d’. For a fixed mass flow rate, the tube side heat transfer co-efficient for turbulent flow conditions is proportional to

A

d^-0.2

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145
Q

Prandtl and Reynolds analogy are same, when Prandtl number is

A

1

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146
Q

Heat transfer occurs by natural convection because change in temperature causes difference in

A

density

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147
Q

The ratio of kinematic viscosity to thermal diffusivity is called the __________ number.

A

Prandtl

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148
Q

The critical radius ‘r’ of insulation on a pipe is given by

A

r = k/h

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149
Q

As per Kirchoffs law, the ratio of the total radiating power to the absorptivity of a body depends on the

A

temperature of the body only.

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150
Q

If the baffle spacing in a shell and tube heat exchanger increases, then the Reynolds number of the shell side fluid

A

decreases.

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151
Q

The heat transfer by radiation from a mild steel surface is to be reduced by reducing the emissivity of the surface. This can be best achieved by

A

painting the surface white (with aluminium paint).

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152
Q

__________ paint has the maximum absorption coefficient.

A

Black

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153
Q

What is Nusselt number?

A

hD/k

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154
Q

Steam traps are provided in steam carrying pipelines to

A

remove condensate and inert gases.

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155
Q

The Dietus-Boelter equation for convective leat transfer
https://www.indiabix.com/_files/images/chemical-engineering/heat-transfer/245-165-1.png
cannot be used for (See picture for equation)

A

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

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156
Q

A hot liquid is kept in a big room. The logorithm of the numerical value of the temperature difference between the liquid and the room is plotted against time. The plot will be very nearly a/an

A

straight line

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157
Q

Radiation heat transfer rates does not depend upon the

A

none of these.

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158
Q

Which of the following is correct?

A

Driving force = Rate x Resistance

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159
Q

Convective heat transfer, in which heat is transferred by movement of warmed matter is described by

A

Newton’s law of cooling

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160
Q

As the difference between the wall temperature and bulk temperature increases, the boiling heat transfer co-efficient

A

goes through a minimum.

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161
Q

Heat transfer rate per unit area is called

A

heat flux

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162
Q

Log mean temperature difference (LMTD) cannot be used, if

A

none of these.

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163
Q

In a multipass shell and tube heat exchanger, tube side return pressure loss is equal to __________ the velocity head.

A

four times

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164
Q

For a given ambient air temperature with increase in the thickness of insulation of a hot cylinderical pipe, the rate of heat loss from the surface would

A

first increase and then decrease

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165
Q

In a parallel flow heat exchanger, if the outlet temperature of hot and cold fluids are the same, then the log mean temperature difference (LMTD) is

A

zero

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166
Q

For what value of Prandtl number, the Col-burn analogy is valid?

A

0.6 to 120

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167
Q

In a forward feed multiple effect, the pressure build up will be

A

least at the outlet of the last effect.

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168
Q

Film boiling is usually not desired in commercial equipments, because

A

the heat transfer rate is low in view of the large temperature drop.

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169
Q

For the same heat transfer area and the terminal conditions, the ratio of the capacities of a single effect evaporator to a triple effect evaporator is

A

1

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170
Q

The variation of thermal conductivity of a metal with temperature is often correlated using an expression of the form K = K0 + at. where, K is the thermal conductivity and T is the temperature (in °K). The units of ‘a’ in SI system will be

A

W/m.k2

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171
Q

Film condensation is promoted on a/an __________ surface.

A

clean & smooth

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172
Q

Dietus-Boelter equation cannot be used for molten metals mainly due to its very low

A

Prandtl number

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173
Q

If Prandtl number is greater than the Schmidt number, then the

A

thermal boundary layer lies inside the concentration boundary layer.

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174
Q

Which of the following accessories is provided in the vapor line of an evaporator for removing the entrained liquid?

A

Catchall

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175
Q

Rate of heat transfer by vaporisation from pools of water is affected by the

A

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

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176
Q

Multiple effect evaporators are commonly used in the manufacture of
P. Paper Q. Superphosphate
R. Sugar S. Fats

A

P and S

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177
Q

Which of the following has the highest thermal conductivity?

A

Silver

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178
Q

Which of the following is unimportant in forced convection?

A

Grashoff number

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179
Q

Steam is to be condensed in a shell and tube heat exchanger, 5 m long with a shell diameter of 1 m. Cooling water is to be used for removing the heat. Heat transfer co-efficient for the cooling water, whether on shell side or tube side is the same. The best arrangement is

A

vertical heat exchanger with steam on shell side.

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180
Q

In a multiple effect evaporator, the effect of boiling point elevation is to

A

reduce the capacity

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181
Q

The rate of heat transfer through a pipe wall is given by, https://www.indiabix.com/_files/images/chemical-engineering/heat-transfer/271-499-1.png . For cylinder of very thin wall, q can be approximated by

A

https://www.indiabix.com/_files/images/chemical-engineering/heat-transfer/271-499-5.png

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182
Q

Dropwise condensation occurs on __________ surfaces.

A

contaminated cooling

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183
Q

For specified tube outside diameter, higher BWG means higher

A

cross-sectional area

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184
Q

Pick out the wrong statement.

A

Swenson-Walker crystalliser is a batch crystalliser.

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185
Q

In case of a vertical tube evaporator, with increase in the liquor level, the __________ is increased.

A

neither (a) and (b)

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186
Q

Electromagnetic radiations propagate in vacuum with a velocity of __________ metre/second.

A

3 x l08

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187
Q

Heat flux is the time rate of heat transfer per unit

A

area

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188
Q

Film boiling occurs at __________ pressure.

A

very high

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189
Q

Heat flux through several resistances in series in analogous to the current flowing through several

A

resistances in series.

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190
Q

Extended heat transfer surface like fins are used to increase the heat transfer rate. Fin efficiency is defined as the ratio of heat transferred across the fin surface to the theoretical heat transfer across an equal area held at the

A

constant temperature equal to that of the base

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191
Q

Vacuum is generally maintained in the vapour space of an evaporator mainly to

A

get economical temperature difference by using moderate pressure steam.

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192
Q

Double pipe heat exchangers are used

A

when heat transfer area required is very low, i.e (100-200 ft2).

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193
Q

Nusselt number (for forced convection heat transfer) is a function of the __________ number.

A

both (a) & (b)

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194
Q

Pick out the wrong statement.

A

Heat transfer by radiation can not occur across an absolute volume.

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195
Q

Which type of heat exchanger is preferred for heavy heat loads ?Which type of heat exchanger is preferred for heavy heat loads?

A

Series and parallel set of shell and tube

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196
Q

Pick out the wrong statement.

A

Thermal conductance of a wall of thickness ‘L’, thermal conductivity ‘k’ and heat flow area ‘A’ is kL/A.

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197
Q

While the total emissivity of a perfect black body is unity, the same for a real body is

A

between 0 and 1

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198
Q

The Grashoff number is defined as the ratio of the

A

buoyancy to viscous forces.

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199
Q

According to Reynolds analogy, Stanton number is equal to (where, f = Fanning friction factor)

A

f/2

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200
Q

The absorptivity of a body is equal to its emissivity

A

under thermal equilibrium.

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201
Q

Absorptivity and refletivity of a perfect black body are respectively

A

1 and 0

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202
Q

In thermal radiation for a black body (where, ε is emissivity and α is absorptivity)

A

α = 1; ε = 1

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203
Q

Pick out the wrong statement.

A

S.I. unit of fouling factor is Watt/m2.°K.

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204
Q

When warm and cold liquids are mixed, the heat transfer is mainly by

A

convection

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205
Q

A cube, sphere & a thin circular plate (all having same mass and made of same material) are all heated to 300°C and allowed to cool in natural air. Which one will cool the slowest?

A

Sphere

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206
Q

Vent pipes are provided in a condenser to

A

remove non-condensable gases.

207
Q

Heat transfer by natural convection is enhanced in system with

A

high co-efficient of thermal expansion.

208
Q

In case of __________ boiling, the bubbles formed on a submerged hot surface get absorbed in the mass of the liquid.

A

pool

209
Q

A body cools down from 75°C to 70°C in 10 minutes. It will cool down from 70° C to 65° C in __________ minutes.

A

> 10

210
Q

In forced convection, the Nusselt number is a function of

A

Re and Pr

211
Q

At what value of Prandtl number, the hydrodynamic and thermal boundary layers are identical?

A

1

212
Q

A dilute aqueous solution is to be concentrated in an evaporator system. High pressure steam is available. Multiple effect evaporator system is employed, because

A

total amount of vapor produced per Kg of feed steam in a multiple effect system is much higher than in a single effect.

213
Q

Heat transfer efficiency leading of energy conservation in a heat exchanger can be achieved by

A

keeping the heat transfer surface clean.

214
Q

Trap is used to remove __________ from steam pipe lines.

A

condensate

215
Q

A composite flat wall of a furnace is made of two materials ‘A’ and ‘B’. The thermal conductivity of ‘A’ is twice of that of material ‘B’, while the thickness of layer of ‘A’ is half that of B. If the temperature at the two sides of the wall are 400 and 1200°K, then the temperature drop (in °K) across the layer of material ‘A’ is

A

160

216
Q

Tube pitch is the __________ of tube diameters and the clearances.

A

sum

217
Q

With increase in the distance between the heat source and the object receiving the heat, the radiation heat transfer

A

decreases

218
Q

The equivalent diameter for the annulus of a double pipe heat exchanger, whose inner pipe has fins on the outside is __________ compared to the same size pipes without fins.

A

less

219
Q

Natural convection is characterised by

A

Grashoff number

220
Q

Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is

A

4.364

221
Q

Thickness of thermal boundary layer is more compared to that of hydrodynamic boundary layer, when the value of Prandtl number is

A

< 1

222
Q

The critical radius of insulation for cylindrical pipe is (where, hi = heat transfer coefficient at inside of the pipe)

A

K/h0

223
Q

The heat flux in the nucleate boiling regimes is proportional to (where, ΔT = excess temperature)

A

(ΔT)^3

224
Q

A body is called grey if the monochromatic emissivity of the body is

A

same for all wavelengths

225
Q

In an extended surface heat exchanger, fluid having lower co-efficient

A

flows outside the tubes.

226
Q

In a shell and tube heat exchanger, the tube side heat transfer co-efficient just at the entrance of the tube is

A

infinity.

227
Q

Grashoff number, which is defined as g . β(Ts - T∞) ρ2. L3/μ2, is proportional to the ratio of buoyancy force to __________ force.

A

viscous

228
Q

Pick out the wrong statement.

A

Film boiling is desirable in commercial equipments due to high heat transfer rate at low temperature drop.

229
Q

Graetz number is given by

A

mCp/kL

230
Q

For a cold dilute feed to produce thick viscous liquor, backward feeding as compared to forward feeding results in

A

increased economy

231
Q

Economy of an evaporator is influenced by the

A

both(b) & (c)

232
Q

If the thermal conductivity of a wall material is independent of temperature, the steady state temperature distribution in the very large thin plane wall having steady, uniform surface temperature follows __________ law.

A

linear

233
Q

In regenerative air preheater (as practised in heating of coke ovens), the heat is transferred

A

by heating an intermediate material (like chequor bricks) and then heating the air from this hot material.

234
Q

__________ equation relates the thermal conductivity of a solid to its temperature.

A

Lee’s

235
Q

For small temperature difference, the heat transfer rate as per Newton’s law of cooling is proportional to (where, Δt = excess temperature)

A

Δt

236
Q

Pick out the wrong statement.

A

Overall heat transfer co-efficient in a heat exchanger is controlled by the value of the film co-efficient, which is higher.

237
Q

Viscous & heat sensitive liquids are concentrated in __________ evaporators.

A

agitated film

238
Q

1 BTU/hr.ft.°F is equal to __________ kcal/hr. m.°C.

A

1.49

239
Q

Heat transfer by radiation between two bodies at T1 & T2 and in an ambient temperature of Ta°C depends on

A

none of these

240
Q

The ratio of momentum diffusivity to thermal diffusivity is the __________ number.

A

Prandtl

241
Q

For a perfectly transparent surface (like gases), the

A

transmissivity = 1

242
Q

For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are

A

different

243
Q

During crystallisation, formation of crystal can occur in __________ solution only.

A

supersaturated

244
Q

An evaporator while concentrating an aqueous solution from 10 to 40% solids evaporates 30000 kg of water. The amount of solids handled by the system in kg is

A

4000

245
Q

An insulator should have

A

low thermal conductivity.

246
Q

In a backward feed multiple effect evaporator

A

feed flows from low pressure to high pressure.

247
Q

1

A

Nu = (Re) (Pr) (St)

248
Q

3

A

parabolic

249
Q

4

A

logarithmic

250
Q

5

A

there is no risk of contamination.

251
Q

6

A

abundance & high heat capacity

252
Q

8

A

Steel

253
Q

9

A

turbulent

254
Q

10

A

local

255
Q

12

A

approach

256
Q

14

A

a higher capacity

257
Q

15

A

81.25

258
Q

16

A

U1 = U2

259
Q

17

A

Watt/m.°K

260
Q

18

A

boiling point (at the same pressure)

261
Q

20

A

> 0.6

262
Q

21

A

R2/(R1+R2)

263
Q

22

A

0.794 h1

264
Q

23

A

heat transfer area.

265
Q

24

A

4.88 kcal/hr. m.2°C.

266
Q

25

A

Molten sodium (a coolant used in fast breeder reactor)

267
Q

26

A

m2°K/W

268
Q

28

A

flexibility possible in the baffle arrangement.

269
Q

29

A

wall or skin friction

270
Q

30

A

0.5 to 50

271
Q

32

A

thickness

272
Q

34

A

solution has an elevation of boiling point.

273
Q

35

A

Pe = Re.Pr

274
Q

36

A

heat flux at the wall to that across the entire pipe.

275
Q

37

A

momentum diffusivity to thermal diffusivity.

276
Q

39

A

Agitated film evaporator

277
Q

40

A

Kirchoffs

278
Q

42

A

higher tube side heat transfer co-efficient.

279
Q

43

A

< 1

280
Q

46

A

U-tube

281
Q

47

A

Forced convection is relatively more effective in increasing the rate of mass transfer, if Schmidt number is larger.

282
Q

48

A

viscous

283
Q

50

A

parabolic

284
Q

Intermittant tube cleaning is possible to be done in case of a __________ evaporator.

A

basket type

285
Q

Harmonic mean temperature difference is given by

A

(2. ΔT1. ΔT2)/(ΔT1 + ΔT2)

286
Q

Arithmetic mean area can be used in heat transfer problem to calculate the heat flow by conduction through a cylinder which is

A

thin walled having the value of Ao Ai/< 2.

287
Q

Three solid objects of the same material and of equal mass-a sphere, a cylinder (length = diameter) and a cube are at 500°C initially. These are dropped in a quenching bath containing a large volume of cooling oil each attaining the bath temperature eventually. The time required for 90% change in temperature is the smallest for

A

cube

288
Q

Overall heat transfer co-efficient for cooling of hydrocarbons by water is about

A

50 -100 BTU/hr. ft.2°F

289
Q

Absorptivity of a perfect black body is unity. Which of the following has maximum absorptivity?

A

coke breeze

290
Q

Thermal diffusivity is given by

A

k/p.Cp

291
Q

At what value of Prandtl number, the hydrodynamic and thermal boundary layers of a fluid flowing over a heated plate will be identical?

A

1

292
Q

Fourier’s law of heat conduction applies to __________ surfaces.

A

both (a) and (b)

293
Q

__________ chart is known as transient heat conduction chart.

A

Dirhing’s

294
Q

Choose the most important factor on which the heat conducted through a wall in a unit time will depend on?

A

Temperature difference between the two surfaces of the wall.

295
Q

Which of the following has the minimum thermal conductivity?

A

Nitrogen

296
Q

In a heat exchanger, one transfer unit means

A

a section of the exchanger in which change in temperature of one stream equals the average driving force in the section.

297
Q

For condensation of pure vapors, if the heat transfer co-efficients in filmwise and drop-wise condensation are respectively hf and hd, then

A

hf < hd

298
Q

Pick out the wrong statement:

A

Heat sensitive materials should be concentrated in high pressure evaporators.

299
Q

For concentrating an aqueous solution of a material like anhydrous Na2SO4, whose solubility decreases with rise in temperature, the most suitable evaporator is a __________ evaporator.

A

vacuum

300
Q

Circulation pump is located below the evaporater to

A

create more suction head.

301
Q

The statement that “maximum wavelength of radiation is inversly proportional to the temperature” is __________ law.

A

Wien’s displacement

302
Q

Steam condensate is recovered by steam traps and recycled for use as boiler feed water, because of its low

A

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

303
Q

At steady state the temperature variation in a plane wall, made of two different solids I & II is shown below :

The thermal conductivity of material I

A

is smaller than that of II.

304
Q

Duhring rule is important in solving problems on

A

evaporation

305
Q

In a shell and tube heat exchanger, the height of 25 percent cut baffles is equal to (where, D = inside diameter of shell)

A

0.75 D

306
Q

Multiple effect evaporation is generally recommended, when the

A

large scale evaporation of liquor is needed

307
Q

The inside heat transfer co-efficient in case of turbulent flow of liquid in the tube side in a 1-2 shell and tube heat exchanger is increased by __________ times, when the number of tube passes is increased to 8.

A

4^0.8

308
Q

__________ heat exchanger is the most suitable, when the temperature of shell side fluid is much higher than that of tube side.

A

U-tube

309
Q

In which mode of heat transfer, the Biot number is important?

A

Transient heat conduction

310
Q

_________ paint has the minimum absorption co-efficient.

A

White lead

311
Q

Asymptotic conditions is reached, when for a fluid flowing in laminar flow through a long tube

A

exit fluid temperature = wall temperature.

312
Q

1000 kg of wet solids are to be dried from 60% to 20% moisture (by weight). The mass of moisture removed in kg is

A

400

313
Q

Which is the most suitable for the con-certration of highly concentrated solution?

A

Open pan evaporation

314
Q

Unsteady state heat conduction occurs, when

A

temperature distribution is dependent on time.

315
Q

What is the absorptivity of a black body?

A

1

316
Q

Mode of heat transfer in which the fluid moves under the influence of changes in fluid pressure produced by external work is called

A

forced convection

317
Q

Baffle spacing

A

should be less than the inside diameter of the shell.

318
Q

Boiling point elevation of a solution of NaOH

A

both (b) and (c).

319
Q

The advantage of backward feed multiple effect evaporators over forward feed units is that

A

most concentrated liquid is at highest temperature.

320
Q

Which of the following is the most controlling factor for the rate of bubble detachment from the hot solid surface?

A

Interfacial tension

321
Q

Which characteristic of a fluid is not important in deciding its route in a shell and tube heat exchanger?

A

None of these

322
Q

Thermal conductivities of most of the liquids __________ with rise in temperature.

A

decreases

323
Q

A metal ball of radius 0.1 m at a uniform temperature of 90°C is left in air at 30°C. The density and the specific heat of the metal are 3000 kg/m3 and 0.4 kJ/kg.K respectively. The heat transfer co-efficient is 50 W/m2.K Neglecting the temperature gradients inside the ball, the time taken (in hours) for the ball to cool to 60°C is

A

0.15

324
Q

The purpose of floating head in a heat exchanger is to

A

avoid buckling of tubes.

325
Q

1000 Kg of liquid at 30°C in a well stirred vessel has to be heated to 120°C, using immersed coils carrying condensing steam at 150°C. The area of the steam coils is 1.2 m2 and the overall heat transfer co-efficient to the liquid is 1500 W/m2.°C. Assuming negligible heat loss to the surrounding and specific heat capacity of the liquid to be 4 kJ/kg.°C, the time taken for the liquid to reach desired temperature will be

A

51 min

326
Q

Overall thermal resistance for conductive heat transfer through a series of flat resistances is equal to the

A

sum of all resistances.

327
Q

Double pipe heat exchangers are preferably useful, when

A

requirement of heat transfer area is low.

328
Q

Removal of __________ heat is involved in the condensation of a vapor under saturated conditions.

A

latent

329
Q

The rate of heat transfer from a vertical plate by natural convection depends upon the temperature differences (ΔT) between wall and outside bulk. The proportionality is given as

A

(ΔT)^3/4

330
Q

If air (a non-condensing gas) is present in a condensing vapor stream, it will __________ the condensation rate of vapor.

A

decrease

331
Q

Prandtl and Reynold’s analogies are identical for Prandtl number value of

A

1

332
Q

The outlet temperature of cooling water in a heat exchanger is generally not allowed to exceed above 50°C in industrial practice mainly to avoid

A

excessive corrosion

333
Q

In evaporators, lowering the feed temperature

A

both (a) and (b).

334
Q

The type of liquor circulation system to be ‘ employed in evaporators (viz. natural or forced circulation) is determined mainly by the __________ of the liquid.

A

viscosity

335
Q

In case of surface condensers, a straight line is obtained on plotting __________ on an ordinary graph paper.

A

1/ ¯v^-0.8

336
Q

Thermal diffusivity is the most important in heat transfer by

A

conduction

337
Q

(NGr x NPr) is called the __________ number.

A

Reyleigh

338
Q

A dephlegmator is a

A

partial condenser

339
Q

A tank painted with which of the following coloured paints, would heat up maximum by radiation from sun?

A

Black paint

340
Q

The separation of liquid droplets from the vapor is done by a/an __________ , in the evaporators.

A

entrainment separator

341
Q

Fouling factor for a heat exchanger is given by (where, U1 = heat transfer co-efficient of dirty surface U2 = heat transfer co-efficient of clean surface)

A

1/U1 - 1/U2

342
Q

If a single tube pass heat exchanger is converted to two pass, then for the same flow rate, the pressure drop per unit length in tube side will

A

increase by 2^16

343
Q

A steel sphere of radius 0.1 m at 400°K is immersed in an oil at 300°K. If the centre of the sphere reaches 350°K in 20 minutes, how long will it take for a 0.05 m radius steel sphere to reach the same temperature (at the centre) under identical conditions ? Assume that the conductive heat transfer co-efficient is infinitely large.

A

5 minutes

344
Q

Fluid motion in the natural convection heat transfer between a solid surface and a fluid in contact with it, results from the

A

none of these.

345
Q

Evaporator tubes are generally

A

vertical

346
Q

For a counter current heat exchanger with Tih = 80°C, T°c = 60°C, T°h = 50°C and Tic = 30°C, and the temperature difference between the two streams being the same everywhere along Z, the direction of flow of hot fluid. The temperature profile should satisfy

A

d^2T/dZ^2 = 0

347
Q

In a boiling curve, the peak heat flux is called the __________ point.

A

burnout

348
Q

Pick out the wrong statement.

A

Filmwise condensation takes place on non-wettable surfaces.

349
Q

h.D/K is called the __________ number.

A

Nusselt

350
Q

Prandtl number is the ratio of

A

momentum diffusivity to thermal diffusivity

351
Q

Conductance is given by(where, x = thickness, A = heat flow area, K = thermal conductivity.)

A

KA/x

352
Q

Heat flux, as defined in heat flow is analogous to __________ in electricity flow.

A

current

353
Q

The wavelength at which the maximum monochromatic emissive power occurs for a black body, is (where, T = absolute temperature of the black body)

A

α 1/T

354
Q

In a shell and tube heat exchanger, putting a longitudinal baffle across the shell, forces the shell side fluid to pass __________ through the heat exchanger.

A

twice

355
Q

When the ratio of the Grashoff number and to the square of Reynolds number is one, the dominant mechanism of heat transfer is

A

mixed convection (both free and forced)

356
Q

The purpose of providing bleed points in the evaporator is to

A

facilitate removal of non-condensable gases

357
Q

Water always boils when its

A

saturated vapour pressure equals the external pressure on its surface.

358
Q

A multiple effect evaporator as compared to a single effect evaporator of the same capacity has

A

higher steam economy

359
Q

Which is the most suitable for cold viscous feed?

A

Backward feed

360
Q

Dropwise condensation is promoted on a/an __________ surface.

A

oily

361
Q

At Pr > 1, conduction in an ordinary fluid flowing through a heated pipe is limited to the

A

viscous sub-layer

362
Q

In a single evaporator system, the steam economy __________ by creating vacuum in the evaporator.

A

increases

363
Q

(NRe.NPr)(D/L)is called the __________ number

A

Graetz

364
Q

Nucleate boiling is promoted

A

on rough surfaces

365
Q

In forced circulation, the heating element is injected

A

internally

366
Q

If all the conditions and dimensions are same, then the ratio of velocity through the tubes of a double pass heat exchanger to that through the single pass heat exchanger is

A

2

367
Q

The equation, Nst = f/2, is the __________ analogy.

A

Reynolds

368
Q

Boiling point elevation for a strong and concentrated solution is found by Duhring’s rule, which states that at the same pressure, the boiling point of a solution is a linear function of the __________ of pure water.

A

boiling point

369
Q

Rate of crystallisation does not depend upon the

A

none of these.

370
Q

Stefen’s block body radiation law can also be derived from __________ law.

A

Planck’s

371
Q

Multipass heat exchangers are used

A

to obtain higher heat transfer co-efficient and shorter tube.

372
Q

A hollow sphere and a solid sphere of the same material and equal radii are heated to the same temperature. In this case,

A

both(b) & (c).

373
Q

Condensing film co-efficient for steam on horizontal tubes ranges from 5000 to 15000 Kcal/hr.m2 .°C. Condensation of vapor is carried out inside the tube in a shell and tube heat exchanger, when the

A

condensate is corrosive in nature.

374
Q

When does the heat generated by fluid friction becomes appreciable compared to the heat transferred between the fluids?

A

At high fluid velocity

375
Q

The Sieder-Tate correlation for heat transfer in turbulent flow in pipe gives Nu α Re^0.8, where, Nu is the Nusselt number and Re is the Reynolds number for the flow. Assuming that this relation is valid, the heat transfer co-efficient varies with the pipe diameter (D) as

A

(D)^-0.2

376
Q

A long iron rod initially at a temperature of 20°C has one end dipped in boiling water (100°C) at time, t = 0. The curved surface of the rod is insulated so that heat conduction is one dimensional in the axial direction. The temperature at a distance 100 mm from the dipped end becomes 40°C at time, t = 200 s. The same temperature is achieved at a distance of 200 mm from the dipped end at time

A

t = 800 s

377
Q

LMTD for evaporators & condensers for a given terminal parameters & set of conditions for counterflow is equal to that for parallel flow. In such heat exchangers, with one of the fluids condensing or evaporating, the surface area required is the least in the __________ flow.

A

same in either ‘a’, b’ or ‘c’

378
Q

Thermal diffusivity of a material

A

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

379
Q

Viscosity of gases __________ with increase in temperature.

A

increase slowly

380
Q

What is the emissivity of a black body?

A

1

381
Q

Steam is routed through the tube in case of a __________ evaporator.

A

horizontal tube

382
Q

Dropwise condensation of steam on cooling surface is promoted

A

an oily surface.

383
Q

Conduction occurs in the buffer zone for a fluid flowing through a heated pipe, only when Prandtl number is

A

0.1

384
Q

In a heat exchanger, the rate of heat transfer from the hot fluid to the cold fluid

A

varies directly as the area and the LMTD.

385
Q

With increase in temperature, the total emissivity of conductors

A

increases

386
Q

Loss of heat from untagged steam pipe to the ambient air is by

A

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

387
Q

Fruit juice (a heat sensitive material) can be concentrated in a __________ evaporator.

A

falling film

388
Q

Tubes are held between top and bottom tube sheets in Calenderia type evaporator by keeping

A

both the tube sheets fixed.

389
Q

A single pass air heater is connected to a two pass unit. For the air flow rate and other conditions remaining the same, the film heat transfer co-efficient for air will vary in the ratio of

A

2^0.8

390
Q

Heat sensitive materials can be concentrated in an evaporator employing

A

vacuum

391
Q

A concentric double pipe heat exchanger as compared to the shell and tube heat exchanger for the same heat load requires

A

more space.

392
Q

In a shell and tube heat exchanger, floating head is used for

A

large temperature differentials.

393
Q

Steam trap is used to

A

remove water resulting from partial condensation of steam.

394
Q

The average heat transfer co-efficient over the entire length of the plate (ha) and the local heat transfer co-efficient (hL), in case of heat transfer over a flat plate in lminar zone is related as

A

ha = 2hL

395
Q

What is the logarithmic mean of r1 and r2 ?

A

(r1-r2/ln(r1/r2))

396
Q

Maximum heat transfer rate is achieved in __________ flow.

A

turbulent

397
Q

Wavelength corresponding to the maximum energy is inversely proportional to the absolute temperature. This is __________ law.

A

Wien’s

398
Q

Three material A, B and C of equal thick-nes and of thermal conductivity of 20, 40 & 60 kcal/hr. m. °C respectively are joined together. The temperature outside of A and C are 30°C and 100°C respectively. The interface between B and C will be at a temperature of __________ °C.

A

70

399
Q

Which of the following parameters of the fluid is not very important, while deciding its route in a shell and tube heat exchanger?

A

density

400
Q

Corrosiveness of steam condensate is due to the presence of

A

both (a) & (b)

401
Q

The equation, (NSt x N2/3Pr) = f/2, is the __________ analogy.

A

Colburn

402
Q

The driving potential for the crystal growth during crystallisation is the __________ of the solution.

A

super-saturation

403
Q

jH factor for heat transfer depends upon the __________ number.

A

Reynolds

404
Q

Kg of liquid evaporated per hour in an evaporator is defined as its

A

capacity

405
Q

Pick out the correct statement.

A

In steady state heat conduction, the only property of the substance which determines the temperature distribution, is the thermal conductivity.

406
Q

Open pan evaporators are preferred to be used, when the solution to be concentrated is

A

highly viscous

407
Q

Cp.μ/K is termed as the __________ number.

A

Prandtl

408
Q

The maximum heat transfer co-efficient from steam heating will be attained when the steam is

A

saturated

409
Q

Kirchoff’s law is applicable to

A

both (a) and (b)

410
Q

In a forward feed multiple effect evaporator, the pressure is

A

lowest in last effect

411
Q

In a co-current double pipe heat exchanger used for condensing saturated steam over the inner tube, if the entrance and exit conditions of the coolant are interchanged, then the rate of condensation will

A

remain unchanged

412
Q

Which of the following situations can be approximated to a steady state heat transfer system?

A

10 kg of dry saturated steam at 8 kgf/cm2 flowing through a short length of stainless steel pipe exposed to atmospheric air at 35°C.

413
Q

Sensible heat absorbed by 1 lb of water when it is heated from 32 to 212°F may be around __________ BTU.

A

180

414
Q

The unit of conductance in SI unit is

A

W/°K

415
Q

In a shell and tube heat exchanger, square pitch compared to triangular pitch

A

gives a higher shell side pressure drop.

416
Q

Which of the following has maximum thermal conductivity?

A

Iron

417
Q

A wall has two layers of materials A and B; each made of a different material. Both the layers have the same thickness. The thermal conductivity of materialA is twice that of B. Under the equilibrium, the temperature difference across the wall is 36°C. The temperature difference across the layer A is __________ °C.

A

12

418
Q

The film co-efficient between condensing vapour and metal wall increases with

A

increasing temperature of the vapour.

419
Q

Critical value of the __________ number governs the transition from laminar to turbulent flow in free convection heat transfer.

A

Prandtl & Grashoff

420
Q

The thermal boundary layer at NPr > 1

A

is thinner than hydrodynamic boundary layer.

421
Q

In the free convection regime of pool boiling, the heat flux is proportional to

A

Δt^5/4

422
Q

With increase in temperature, the thermal conductivity of fresh lubricating oil

A

decreases

423
Q

Fresh orange juice contains 12% (by weight) solids and the rest water 90% of the fresh juice is sent to an evaporator to remove water and subsequently mixed with the remaining 10% of fresh juice. The resultant product contains 40% solids. The kg of water removed from 1 kg fresh juice is

A

0.7

424
Q

Nusselt number is the ratio of the temperature gradient at the wall to

A

that across the entire pipe

425
Q

The Stefan-Boltzman constant depends on the

A

none of these

426
Q

The units of resistance to heat transfer is

A

W-1m2K

427
Q

Thermal conductivity of a gas at low density, __________ with increase in temperature.

A

increases

428
Q

Nusselt number is a function of Prandtl number and __________ number of fluid in natural convection heat transfer.

A

Grashoff

429
Q

__________ heat exchanger is used for chilling oil to be dewaxed.

A

Double pipe

430
Q

It is not recommended to use a 1-2 shell and tube heat exchanger for a particular heat duty, whenever the LMTD correction factor is

A

< 0.75

431
Q

Pick out the wrong statement.

A

Two identical cubes of iron and copper will have the same heat content under the same conditions of temperature.

432
Q

In sub-cooled boiling,

A

temperature of the heating surface is more than the boiling point of the liquid.

433
Q

With increase in temperature, the thermal conductivity of a gas

A

increases.

434
Q

A __________ evaporator employs an annular downtake.

A

basket type

435
Q

Radiation heat losses from satisfactorily insulated high pressure boilar may be about __________ percent.

A

7

436
Q

In natural convection heat transfer, the correlating parameter is the

A

Grashoff number

437
Q

Boiling of milk in an open vessel is an example of __________ boiling.

A

film

438
Q

Pick out the wrong statement.

A

The maximum is the emissive power of a surface at a temperature T1 occurs at a wavelength of λ1. If the surface temperature is halved, the maximum in the emissive power would occur at a wavelength of 0.5 λ1.

439
Q

Mode of heat transfer involved in the cooling of air cooled internal combustion engine is

A

natural convection

440
Q

Steady state one dimensional heat flow by conduction as given by Fourier’s low does not assume that

A

material is anisotropic.

441
Q

The left face of a one dimensional slab of thickness 0.2 m is maintained at 80°C and the right face is exposed to air at 30°C. The thermal conductivity of the slab is 1.2 W/m.K and the heat transfer co-efficient from the right face is 10 W/m2.K. At steady state, the temperature of the right face in °C is

A

48.7

442
Q

In a shell and tube heat exchanger, the shell side fluid velocity can not be changed by changing the

A

tube diameter

443
Q

To reduce the tube side pressure drop for the same flow rate, the heat exchanger recomended is

A

1-1 heat exchanger

444
Q

Heat transfer co-efficient (h) for a fluid flowing inside a clean pipe is given by
This is valid for the value of NRe equal to

A

> 10000

445
Q

Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m2°C.

A

1588776

446
Q

Correction is applied to LMTD for __________ flow.

A

cross

447
Q

If h1 = inner film co-efficient and /h2 = outer film co-efficient, then the overall heat transfer co-efficient is

A

always between h1 and h2

448
Q

One kilogram of water at 0°C is changed to superheated steam of one atm pressure and 300° C. The major heat consumption in the process will be to

A

evaporate the water.

449
Q

For __________ Prandtl number values, the heat conduction will be negligible in the buffer zone.

A

high

450
Q

The radiation heat flux from a heating element at a temperature of 800°C, in a furnace maintained at 300°C is 8 kW/m2. The flux, when the element temperature is increased to 1000°C for the same furnace temperature is

A

16.5 kW/m2

451
Q

Heat exchangers operating, when the asymptotic range is reached,

A

results in making part of the heating surface inactive.

452
Q

In case of a shell and tube heat exchanger, the minimum and maximum baffle spacing is respectively (where, D = inside diameter of the shell)

A

D/5 and D

453
Q

In case of heat transfer by conduction in a hollow cylinder, __________ mean area is used to calculate the heat transfer rate.

A

logarithmic

454
Q

In a gas-liquid shell and tube heat exchanger, the

A

all ‘a’, ‘b’ & ‘c’

455
Q

Which is the most suitable for the concentration of foamy & frothy liquors?

A

Long tube vertical evaporator

456
Q

Boiling point elevation of an ideal solution

A

increases rapidly with temperature rise.

457
Q

The rate of heat transfer is a product of overall heat transfer co-efficient, the difference in temperature and the

A

heat transfer area

458
Q

Which of the following has the lowest overall heat transfer co-efficient?

A

Air

459
Q

Which of the following has the minimum absorptivity?

A

Aluminum foil

460
Q

A black body when hot, emits heat radiation of __________ wavelengths.

A

all

461
Q

A composite wall consists of two plates A and B placed in series normal to the flow of heat. The thermal conductivities are kA and kB and the specific heat capacities are CPA and CPB for plates A and B respectively. Plate B has twice the thickness of plate A. At steady state, the temperature difference across plate A is greater than that across plate B, when

A

kA < 0.5kB

462
Q

Vibrations in the tubes of a shell and tube heat exchanger is induced due to the

A

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

463
Q

Heat transfer by conduction in the turbulent core of a fluid flowing through a heated pipe is negligible, if the value of Prandtl number is

A

0.6

464
Q

The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is

A

3.66

465
Q

Sensible heat of hot industrial flue gases can not be recovered by a/an

A

none of these

466
Q

The critical radius of insulation for a spherical shell is (where, K = thermal conductivity of insulating material h0 = heat transfer coefficient at the outer surface)

A

2K/h0

467
Q

Radiator of an automobile engine is a __________ type of heat exchanger.

A

direct contact

468
Q

In pipe flow, heat is transferred from hot wall to the liquid by

A

forced convection and conduction

469
Q

The value of Stefan-Boltazman constant in SI unit is

A

5.6697 x 10-8W/m2.°K4

470
Q

The unit of heat transfer co-efficient is

A

BTU/hr. ft2°F

471
Q

For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus-Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of

A

6.1

472
Q

The inner wall of a furnace is at a temperature of 700°C. The composite wall is made of two substances, 10 and 20 cm thick with thermal conductivities of 0.05 and 0.1 W.m-1.°C-1 respectively. The ambient air is at 30°C and the heat transfer co-efficient between the outer surface of wall and air is 20 W.m-2.°C-1. The rate of heat loss from the outer surface in W.m-2is

A

165.4

473
Q

Value of Nusselt number [Nu = (hD/k)] for the heat transfer by conduction from a droplet or a spherical particle to a surrounding stagnant film is

A

2

474
Q

Low thermal conductivity of heat insulating materials is due to its

A

high proportion of air space

475
Q

The most conducive surface for dropwise condensation to occur is the __________ surface.

A

oily

476
Q

In an interphase heat transfer process, the equilibrium state corresponds to equality of temperature in the two phases, while the condition for equilibrium in an interphase mass transfer process is equality of

A

concentrations

477
Q

Calburn analogy is applicable for the value of Prandtl number from

A

0.6 to 120

478
Q

Pick out the correct equation.

A

jH = (St)(Pr)^2/3 = f/2

479
Q

Multiple effect evaporators ar used to

A

increase the steam economy & the capacity.

480
Q

Prandtl number is given by

A

(Cp · μ)/k

481
Q

Small scale evaporation is done in a

A

steam jacketed kettle

482
Q

Heat exchanger tubes are never made of

A

lead

483
Q

At constant temperature, the thermal conductivities of gases __________ with rise in pressure.

A

decrease

484
Q

Reason for operating an evaporator in multiple effect is to secure

A

both (a) and (b).

485
Q

In a cooling tower, water becomes cool by

A

loosing sensible heat.

486
Q

In Fourier’s law, the proportionality constant is called the

A

thermal conductivity

487
Q

The heat transfer co-efficient in film type condensation is __________ that for dropwise condensation.

A

lower than

488
Q

Pick out the wrong statement.

A

Thermal conductivity of a dry material is more than that of the damp material.

489
Q

Duhring’s plot’ is of use in

A

evaporation

490
Q

Which has the lowest Prandtl number?

A

Liquid metal

491
Q

Pick out the wrong statement.

A

Duhring’s plot is used for calculating the concentration of solution.

492
Q

Prandtl number for most of dry gases is about

A

0.72

493
Q

Prandtl number is the reciprocal of

A

Thermal diffusivity/Momentum diffusivity

494
Q

In a heat exchanger with steam outside the tubes, a liquid gets heated to 45°C, when its flow velocity in the tubes is 2 m/s. If the flow velocity is reduced to 1 m/s, other things remaining the same, the temperature of the exit liquid will be

A

more than 45°C

495
Q

For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is

A

Nu = 2/pi x Gz

496
Q

Multiple effect evaporation accounts for

A

steam economy

497
Q

In case of a supercooled solution, which is on the verge of crystallisation, the free energy of the solution as compared to that of the solid is

A

more

498
Q

Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

A

1

499
Q

In Biot number, the characteristic length used is the ratio of the __________ of the solid.

A

volume to surface area

500
Q

Which of the following is the most widely used heat insulating material for pipelines carrying steam?

A

85% magnesia cement and glass wool.

501
Q

Heat transfer co-efficient equation for forced convection, Nu = 0.023 Re^0.8 . Pr^n, is not valid, if the value of

A

Reynolds number for the flow involved is < 2100.

502
Q

Which is the best tube arrangement (in a shell and tube heat exchanger) if the fluids are clean and non-fouling?

A

Triangular pitch

503
Q

In case of a multipass shell and tube heat exchanger, the temperature drop in the fluid

A

and the wall are proportional to individual resistances.

504
Q

The purpose of providing expansion bellows in the shell of tubular exchanger is to

A

account for the uneven expansion of shell and tube bundles.

505
Q

A graph between __________ is called Wilson plot.

A

1/U Vs. 1/V^0.8

506
Q

Grashhoff number is given by

A

gD^3.β.Δtρ2/μ^2

507
Q

The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is

A

333W/m2.K

508
Q

In a laboratory test run, the rate of drying was found to be 0.5 x 10-3 kg/m2.s, when the moisture content reduced from 0.4 to 0.1 on dry basis. The critical moisture content of the material is 0.08 on a dry basis. A tray dryer is used to dry 100 kg (dry basis) of the same material under identical conditions. The surface area of the material is 0.04 m2/kg of dry solid. The time required (in seconds) to reduce the moisture content of the solids from 0.3 to 0.2 (dry basis) is

A

5000

509
Q

Pick out the wrong statement.

A

Heat transfer co-efficient during nucleate boiling is not influenced by the agitation imparted.

510
Q

What is the geometric mean of two heat transfer areas A1 and A2?

A

sqrt*(A1 . A2)

511
Q

Evaporation by thermocompression results in the

A

both (a) and (b).

512
Q

Forced circulation evaporators are normally used for concentrating liquids having

A

both(a) & (b)

513
Q

Steam economy in case of a triple effect evaporator will be

A

> 1