Heat Transfer (2) Flashcards

1
Q

Black liquor generated during paper manufacture is concentrated in a

A

multiple effect evaporator.

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2
Q

Reynold’s analogy states that

A

Nst α f

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3
Q

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

A

nucleate boiling

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4
Q

Shell side pressure drop in a shell and tube heat exchanger does not depend upon the

A

none of these.

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5
Q

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

A

decreases

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6
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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7
Q

Fouling factor

A

accounts for additional resistances to heat flow.

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8
Q

The steam ejector is used to

A

create vacuum.

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9
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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10
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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11
Q

Presence of a non-condensing gas in a condensing vapour

A

none of these.

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12
Q

In case of evaporators, liquid entrainment results primarily due to

A

foaming of the solution.

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13
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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14
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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15
Q

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

A

boiling point elevations

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16
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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17
Q

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

A

the largest

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18
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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19
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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20
Q

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

A

Schmidt number.

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21
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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22
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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23
Q

Out of the following four assumptions used in the derivation of the equation for LMTD , which one is subject to the largest deviation in practice ?

A

Constant rate of fluid flow.

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24
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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25
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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26
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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27
Q

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

A

low film co-efficient

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28
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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29
Q

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

A

0.5-50

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30
Q

Economy of a multiple effect evaporator depends upon the

A

heat balance consideration

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31
Q

The Graetz number is concerned with the

A

heat transfer in laminar flow.

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32
Q

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

A

called the angle of vision.

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33
Q

Pick out the wrong statement.

A

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

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34
Q

With increase in temperature, the thermal conductivity of most liquids

A

decreases

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35
Q

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

A

radiation

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36
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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37
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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38
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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39
Q

Planck’s distribution law is valid for __________ bodies.

A

coloured

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40
Q

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

A

increased

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41
Q

Baffles are provided in heat exchangers to increase the

A

heat transfer co-efficient

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42
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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43
Q

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

A

Schmidt number

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44
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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45
Q

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

A

partial ionisation

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46
Q

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

A

cummulatively increases

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47
Q

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

A

∝ 1/t

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48
Q

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

A

increasing temperature.

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49
Q

A diathermaneous substance __________ the thermal radiation completely.

A

transmits

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50
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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51
Q

Mechanical recompression evaporation is used in the production of

A

distilled water

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52
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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53
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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54
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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55
Q

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

A

density

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56
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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57
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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58
Q

Which of the following is correct ?

A

Driving force = Rate x Resistance

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59
Q

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

A

none of these.

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60
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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61
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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62
Q

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

A

0.6 to 120

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63
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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64
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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65
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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66
Q

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

A

Prandtl number

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67
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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68
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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69
Q

Which of the following is unimportant in forced convection ?

A

Grashhoff number

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70
Q

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

A

reduce the capacity

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71
Q

Dropwise condensation occurs on __________ surfaces.

A

contaminated cooling

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72
Q

For specified tube outside diameter, higher BWG means higher

A

cross-sectional area

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73
Q

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

A

3 x l0^8

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74
Q

Film boiling occurs at __________ pressure.

A

very high

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75
Q

Pick out the wrong statement.

A

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

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76
Q

The Grashoff number is defined as the ratio of the

A

buoyancy to viscous forces.

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77
Q

The absorptivity of a body is equal to its emissivity

A

under thermal equilibrium.

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78
Q

Pick out the wrong statement.

A

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

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79
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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80
Q

Vent pipes are provided in a condenser to

A

remove non-condensable gases.

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81
Q

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

A

pool

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82
Q

Trap is used to remove __________ from steam pipe lines.

A

condensate

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83
Q

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

A

sum

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84
Q

Natural convection is characterised by

A

Grashhoff number

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85
Q

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

A

< 1

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86
Q

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

A

K/h0

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87
Q

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

A

r = k/h

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88
Q

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

A

(ΔT)^3

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89
Q

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

A

same for all wavelengths

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90
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

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91
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

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92
Q

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

A

Lee’s

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93
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

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94
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.

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95
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

96
Q

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

A

Prandtl

97
Q

For a perfectly transparent surface (like gases), the

A

transmissivity = 1

98
Q

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

A

different

99
Q

Choose the correct equation.

A

Nu = (Re) (Pr) (St)

100
Q

In a forward feed multiple effect evaporator unit

A

none of these.

101
Q

In case of __________ boiling, the liquid temperature is below the saturation temperature and the boiling takes place in the vicinity of the heated surface.

A

local

102
Q

The ratio of velocity head to tube side return loss in case of a multipass shell and tube heat exchanger is

A

1/4

103
Q

Terminal point temperature differences between fluids in case of a heat exchanger is termed as

A

approach

104
Q

Overall heat transfer co-efficient of a particular tube is U1. If the same tube with some dirt deposited on either side has coefficient U2, then

A

U1 = U2

105
Q

Boiling point of a solution according to Duhring’s rule is a linear function of the __________ of water.

A

boiling point (at the same pressure)

106
Q

In SI units, thermal conductivity is expressed in

A

Watt/m.°K

107
Q

In SI units, fouling factor is expressed in

A

m2°K/W

108
Q

An ejector is used to

A

none of these

109
Q

Extremely large or small volumes of fluids are generally best routed through the shell side of a shell and tube heat exchanger, because of the

A

flexibility possible in the baffle arrangement.

110
Q

All analogy equations connecting friction factor and heat transfer co-efficient apply only to

A

wall or skin friction

111
Q

Electro-magnetic spectrum range, which is important for radiation varies from __________ microns.

A

0.5 to 50

112
Q

The characteristic dimensionless groups for heat transfer to a fluid flowing through a pipe in laminar flow are

A

Nu, Gz

113
Q

The capacity of double-effect evaporator is less than half of the capacity of two single effects, each of which is operating over same terminal temperature difference, when the

A

solution has an elevation of boiling point.

114
Q

Peclet number (Pe) is given by

A

Pe = Re.Pr

115
Q

Nusselt number is the ratio of the

A

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

116
Q

The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is

A

higher tube side heat transfer co-efficient.

117
Q

If heat transfer rate varies with the time, it is termed as

A

none of these

118
Q

Pick out the wrong statement.

A

The Colbum jH factor for heat transfer is given by Nst Npr.

119
Q

Pick out the wrong statement.

A

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

120
Q

Agitated film evaporator is suitable for concentrating __________ liquids.

A

viscous

121
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 tempeature follows __________ law.

A

parabolic

122
Q

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

A

basket type

123
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.

124
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

125
Q

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

A

coke breeze

126
Q

__________ chart is known as transient heat conduction chart.

A

Dirhing’s

127
Q

Which of the following has the minimum thermal conductivity ?

A

Nitrogen

128
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.

129
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

130
Q

Pick out the wrong statement:

A

Heat sensitive materials should be concentrated in high pressure evaporators.

131
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

132
Q

Circulation pump is located below the evaporater to

A

create more suction head.

133
Q

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

A

Wien’s displacement

134
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

135
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

136
Q

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

A

exit fluid temperature = wall temperature.

137
Q

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

A

Open pan evaporation

138
Q

Unsteady state heat conduction occurs, when

A

temperature distribution is dependent on time.

139
Q

Baffle spacing

A

should be less than the inside diameter of the shell.

140
Q

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

A

most concentrated liquid is at highest temperature.

141
Q

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

A

None of these

142
Q

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

A

decreases

143
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

144
Q

The purpose of floating head in a heat exchanger is to

A

avoid buckling of tubes.

145
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

146
Q

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

A

latent

147
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

148
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

149
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

150
Q

Thermal diffusivity is the most important in heat transfer by

A

conduction

151
Q

(NGr x NPr) is called the __________ number.

A

Reyleigh

152
Q

A dephlegmator is a

A

partial condenser

153
Q

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

A

Black paint

154
Q

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

A

entrainment separator

155
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

156
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

157
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.

158
Q

Evaporator tubes are generally

A

vertical

159
Q

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

A

burnout

160
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

161
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)

162
Q

Water always boils when its

A

saturated vapour pressure equals the external pressure on its surface.

163
Q

Dropwise condensation is promoted on a/an __________ surface.

A

oily

164
Q

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

A

viscous sub-layer

165
Q

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

A

increases

166
Q

Nucleate boiling is promoted

A

on rough surfaces

167
Q

In forced circulation, the heating element is injected

A

internally

168
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

169
Q

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

A

Planck’s

170
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.

171
Q

The Sieder-Tate correlation for heat transfer in turbulent flow in pipe gives Nu α Re0.8, 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

172
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

173
Q

Viscosity of gases __________ with increase in temperature.

A

increase slowly

174
Q

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

A

horizontal tube

175
Q

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

A

0.1

176
Q

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

A

both the tube sheets fixed.

177
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.

178
Q

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

A

large temperature differentials.

179
Q

Steam trap is used to

A

remove water resulting from partial condensation of steam.

180
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

181
Q

Maximum heat transfer rate is achieved in __________ flow.

A

turbulent

182
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

183
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

184
Q

jH factor for heat transfer depends upon the __________ number.

A

Reynolds

185
Q

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

A

capacity

186
Q

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

A

highly viscous

187
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

188
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.

189
Q

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

A

increasing temperature of the vapour.

190
Q

The thermal boundary layer at NPr > 1

A

is thinner than hydrodynamic boundary layer.

191
Q

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

A

Δt^5/4

192
Q

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

A

decreases

193
Q

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

A

increases

194
Q

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

A

Grashoff

195
Q

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

A

Double pipe

196
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.

197
Q

In sub-cooled boiling,

A

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

198
Q

In natural convection heat transfer, the correlating parameter is the

A

Grashoff number

199
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.

200
Q

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

A

material is anisotropic.

201
Q

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

A

tube diameter

202
Q

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

A

1-1 heat exchanger

203
Q

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

A

5000-15000

204
Q

Correction is applied to LMTD for __________ flow.

A

cross

205
Q

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

A

high

206
Q

Heat exchangers operating, when the asymptotic range is reached,

A

results in making part of the heating surface inactive.

207
Q

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

A

Long tube vertical evaporator

208
Q

Boiling point elevation of an ideal solution

A

increases rapidly with temperature rise.

209
Q

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

A

Air

210
Q

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

A

all

211
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

212
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

213
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

214
Q

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

A

none of these

215
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

216
Q

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

A

direct contact

217
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

218
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

219
Q

Calburn analogy is applicable for the value of Prandtl number from

A

0.6 to 120

220
Q

Multiple effect evaporators ar used to

A

increase the steam economy & the capacity.

221
Q

Small scale evaporation is done in a

A

steam jacketed kettle

222
Q

Heat exchanger tubes are never made of

A

lead

223
Q

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

A

decrease

224
Q

In a cooling tower, water becomes cool by

A

loosing sensible heat.

225
Q

Pick out the wrong statement.

A

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

226
Q

Which has the lowest Prandtl number ?

A

Liquid metal

227
Q

Prandtl number for most of dry gases is about

A

0.72

228
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 Gz

229
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

230
Q

Multiple effect evaporation accounts for

A

steam economy

231
Q

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

A

1

232
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.

233
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

234
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

235
Q

Pick out the wrong statement.

A

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