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Chemical Engineering Reviewer > Heat Transfer (Set 4) > Flashcards

Heat Transfer (Set 4) Flashcards

As one of the transport phenomena, the concepts in heat transfer are crucial for design, operation, and maintenance of heat transfer equipment such as heat exchangers and insulation.

1
Q

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

A

basket type

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2
Q

Harmonic mean temperature difference is given by

A

(2. ΔT1. ΔT2)/(ΔT1 + ΔT2)

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3
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.

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4
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

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5
Q

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

A

50 -100 BTU/hr. ft.2°F

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6
Q

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

A

coke breeze

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7
Q

Thermal diffusivity is given by

A

k/p.Cp

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8
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

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9
Q

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

a. isothermal
b. non-isothermal

A

both (a) and (b)

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10
Q

____ chart is known as transient heat conduction chart.

A

Dirhing’s

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11
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.

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12
Q

Which of the following has the minimum thermal conductivity?

A

Nitrogen

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13
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.

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14
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

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15
Q

Pick out the wrong statement:

A

Heat sensitive materials should be concentrated in high pressure evaporators.

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16
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

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17
Q

Circulation pump is located below the evaporater to

A

create more suction head.

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18
Q

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

A

Wien’s displacement

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19
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)

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20
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.

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21
Q

Duhring rule is important in solving problems on

A

evaporation

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22
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

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23
Q

Multiple effect evaporation is generally recommended, when the

A

large scale evaporation of liquor is needed

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24
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

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25
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

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26
Q

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

A

Transient heat conduction

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27
Q

_________ paint has the minimum absorption co-efficient.

A

White lead

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28
Q

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

A

exit fluid temperature = wall temperature.

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29
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

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30
Q

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

A

Open pan evaporation

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31
Q

Unsteady state heat conduction occurs, when

A

temperature distribution is dependent on time.

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32
Q

What is the absorptivity of a black body?

A

1

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33
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

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34
Q

Baffle spacing

A

should be less than the inside diameter of the shell.

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35
Q

Boiling point elevation of a solution of NaOH
a. increases rapidly with temperature rise.
b. is almost independent of temperature.
c. is almost independent of pressure.

A

both (b) and (c).

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36
Q

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

A

most concentrated liquid is at highest temperature.

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37
Q

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

A

Interfacial tension

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38
Q

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

A

None of these

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39
Q

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

A

decreases

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40
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

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41
Q

The purpose of floating head in a heat exchanger is to

A

avoid buckling of tubes.

42
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

43
Q

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

A

sum of all resistances.

44
Q

Double pipe heat exchangers are preferably useful, when

A

requirement of heat transfer area is low.

45
Q

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

A

latent

46
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

47
Q

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

A

decrease

48
Q

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

A

1

49
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

50
Q

In evaporators, lowering the feed temperature

A

both (a) and (b).

51
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

52
Q

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

A

1/ ¯v^-0.8

53
Q

Thermal diffusivity is the most important in heat transfer by

A

conduction

54
Q

(NGr x NPr) is called the ____ number.

A

Reyleigh

55
Q

A dephlegmator is a

A

partial condenser

56
Q

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

A

Black paint

57
Q

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

A

entrainment separator

58
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

59
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

60
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

61
Q

Fluid motion in the natural convection heat transfer between a solid surface and a fluid in contact with it, results from the
a. existence of thermal boundary layer.
b. temperature gradient produced due to density difference
c. buoyancy of the bubbles produced at active nucleation site.

A

none of these.

62
Q

Evaporator tubes are generally

A

vertical

63
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

64
Q

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

A

burnout

65
Q

Pick out the wrong statement.

A

Filmwise condensation takes place on non-wettable surfaces.

66
Q

h.D/K is called the ____ number.

A

Nusselt

67
Q

Prandtl number is the ratio of

A

momentum diffusivity to thermal diffusivity

68
Q

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

A

KA/x

69
Q

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

A

current

70
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

71
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

72
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)

73
Q

The purpose of providing bleed points in the evaporator is to

A

facilitate removal of non-condensable gases

74
Q

Water always boils when its

A

saturated vapour pressure equals the external pressure on its surface.

75
Q

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

A

higher steam economy

76
Q

Which is the most suitable for cold viscous feed?

A

Backward feed

77
Q

Dropwise condensation is promoted on a/an ____ surface.

A

oily

78
Q

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

A

viscous sub-layer

79
Q

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

A

increases

80
Q

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

A

Graetz

81
Q

Nucleate boiling is promoted

A

on rough surfaces

82
Q

In forced circulation, the heating element is injected

A

internally

83
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

84
Q

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

A

Reynolds

85
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

86
Q

Rate of crystallisation does not depend upon the

A

none of these.

87
Q

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

A

Planck’s

88
Q

Multipass heat exchangers are used

A

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

89
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).

90
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.

91
Q

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

A

At high fluid velocity

92
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

93
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

94
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. parallel
b. mixed
c. counterflow

A

same in either ‘a’, b’ or ‘c’

95
Q

Thermal diffusivity of a material

A

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

96
Q

Viscosity of gases ____ with increase in temperature.

A

increase slowly

97
Q

What is the emissivity of a black body?

A

1

98
Q

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

A

horizontal tube

99
Q

Dropwise condensation of steam on cooling surface is promoted

A

an oily surface.

100
Q

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

A

0.1

Chemical Engineering Reviewer (44 decks)

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