Deck 7: Heat Transfer and Heat Exchangers: Part B
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Deck 7: Heat Transfer and Heat Exchangers: Part B
1
Heat waves
A)Cannot pass through vacuum
B)Travel in straight line
C)Can be reflected by a mirror
D)Both (B) and (C)
A)Cannot pass through vacuum
B)Travel in straight line
C)Can be reflected by a mirror
D)Both (B) and (C)
Both (B) and (C)
2
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)0.35
B)0.45
C)0.55
D)0.85
A)0.35
B)0.45
C)0.55
D)0.85
0.45
3
If air (a non-condensing gas) is present in a condensing vapor stream, it will __________ the condensation rate of vapor.
A)Increase
B)Decrease
C)Not affect
D)Increase the condensing film co-efficient as well as
A)Increase
B)Decrease
C)Not affect
D)Increase the condensing film co-efficient as well as
Decrease
4
The most conducive surface for dropwise condensation to occur is the __________ surface.
A)Coated
B)Oily
C)Glazed & polished
D)Smooth
A)Coated
B)Oily
C)Glazed & polished
D)Smooth
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5
For a perfectly transparent surface (like gases), the
A)Absorptivity = 0
B)Transmissivity = 1
C)Reflectivity = 0
D)All (A), (B) & (C)
A)Absorptivity = 0
B)Transmissivity = 1
C)Reflectivity = 0
D)All (A), (B) & (C)
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6
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)Baffle spacing & shell diameter
B)Tube diameter & pitch
C)Viscosity, density & mass velocity of shell side fluid
D)None of these
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7
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)d0.8
B)d-0.2
C)d-1
D)d-1.8
A)d0.8
B)d-0.2
C)d-1
D)d-1.8
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8
In evaporators, lowering the feed temperature
A)Increases the heating area required
B)Reduces the economy
C)Both (A) and (B)
D)Decreases the heating area required
A)Increases the heating area required
B)Reduces the economy
C)Both (A) and (B)
D)Decreases the heating area required
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9
Heat transfer co-efficient (h) for a fluid flowing inside a clean pipe is given by h = 0.023 (K/D) (DV?/µ) 0.8 (CP.µ/k) 0.4. This is valid for the value of NRe equal to
A)< 2100
B)2100-4000
C)> 4000
D)> 10000
A)< 2100
B)2100-4000
C)> 4000
D)> 10000
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10
In case of vertical tube evaporator, with increase in liquor level, the overall heat transfer co-efficient
A)Increases
B)Decreases
C)Is not affected
D)May increase or decrease; depends on the feed
A)Increases
B)Decreases
C)Is not affected
D)May increase or decrease; depends on the feed
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11
The ratio of kinematic viscosity to thermal diffusivity is called the __________ number.
A)Peclet
B)Prandtl
C)Stanton
D)Nusselt
A)Peclet
B)Prandtl
C)Stanton
D)Nusselt
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12
Intermittent tube cleaning is possible to be done in case of a __________ evaporator.
A)Basket type
B)Horizontal tube
C)Calandria
D)None of these
A)Basket type
B)Horizontal tube
C)Calandria
D)None of these
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13
Vibrations in the tubes of a shell and tube heat exchanger is induced due to the
A)Flow of fluid on the tube and shell sides
B)Oscillations in the flow of shell/tube sides fluid
C)Vibrations transmitted through piping and/or supports due to external reasons
D)All (A), (B) and (C)
A)Flow of fluid on the tube and shell sides
B)Oscillations in the flow of shell/tube sides fluid
C)Vibrations transmitted through piping and/or supports due to external reasons
D)All (A), (B) and (C)
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14
Pick out the wrong statement.
A)Orifice baffles are never used in a shell and tube heat exchanger
B)Pressure drop on the shell side of a heat exchanger depends upon tube pitch also
C)In a horizontal tube evaporator, surface blanketing by air is avoided
D)Split ring type and pull through type floating heads are two commonly used floating heads is heat exchangers
A)Orifice baffles are never used in a shell and tube heat exchanger
B)Pressure drop on the shell side of a heat exchanger depends upon tube pitch also
C)In a horizontal tube evaporator, surface blanketing by air is avoided
D)Split ring type and pull through type floating heads are two commonly used floating heads is heat exchangers
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15
What is the steam economy in case of a single effect evaporator system?
A)1
B)> 1
C)< 1
D)0.1
A)1
B)> 1
C)< 1
D)0.1
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16
Overall heat transfer co-efficient for cooling of hydrocarbons by water is about
A)50 -100 Kcal/hr.m2.°C
B)50 -100 W/m2.°K
C)50 -100 BTU/hr. ft.2°F
D)1000 - 1500 BTU/hr. ft.2°F
A)50 -100 Kcal/hr.m2.°C
B)50 -100 W/m2.°K
C)50 -100 BTU/hr. ft.2°F
D)1000 - 1500 BTU/hr. ft.2°F
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17
For turbulent flow in a tube, the heat transfer co-efficient is obtained from the DittusBoelter 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)1
B)1.74
C)6.1
D)37
A)1
B)1.74
C)6.1
D)37
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18
For small temperature difference, the heat transfer rate as per Newton's law of cooling is proportional to (where, ?t = excess temperature)
A)?t
B)?t2
C)?t3
D)?(?t)
A)?t
B)?t2
C)?t3
D)?(?t)
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19
Baffles in the shell side of a shell and tube heat exchanger
A)Increase the cross-section of the shell side liquid
B)Force the liquid to flow parallel to the bank
C)Increase the shell side heat transfer co-efficient
D)Decrease the shell side heat transfer co-efficient
A)Increase the cross-section of the shell side liquid
B)Force the liquid to flow parallel to the bank
C)Increase the shell side heat transfer co-efficient
D)Decrease the shell side heat transfer co-efficient
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20
The ratio of total radiating power to the absorptivity of the body depends upon the __________ as per Kirchoff?s law.
A)Wavelength of radiation
B)Nature of the body
C)Temperature of the body
D)None of these
A)Wavelength of radiation
B)Nature of the body
C)Temperature of the body
D)None of these
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21
__________ chart is known as transient heat conduction chart.
A)Dirhing's
B)Heisler's
C)Mollier's
D)Cox
A)Dirhing's
B)Heisler's
C)Mollier's
D)Cox
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22
Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m2 °C.
A)10-50
B)100-500
C)1000-1500
D)5000-15000
A)10-50
B)100-500
C)1000-1500
D)5000-15000
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23
Controlling heat transfer film co-efficient is the one, which offers __________ resistance to heat transfer.
A)No
B)The least
C)The largest
D)Lower
A)No
B)The least
C)The largest
D)Lower
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24
The main function of baffles provided in a shell and tube heat exchanger is to
A)Facilitate the cleaning of outer tube surface
B)Enhance turbulence
C)Hold the tubes in position
D)All 'a', 'b' & 'c'
A)Facilitate the cleaning of outer tube surface
B)Enhance turbulence
C)Hold the tubes in position
D)All 'a', 'b' & 'c'
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25
Pick out the wrong statement:
A)The capacity of an evaporator is reduced by the boiling point elevation
B)Corrosive liquid is normally passed through the tubes in a shell and tube heat exchanger
C)Steam jet ejector is used for vapor compression in a thermal recompression evaporator
D)Heat sensitive materials should be concentrated in high pressure evaporators
A)The capacity of an evaporator is reduced by the boiling point elevation
B)Corrosive liquid is normally passed through the tubes in a shell and tube heat exchanger
C)Steam jet ejector is used for vapor compression in a thermal recompression evaporator
D)Heat sensitive materials should be concentrated in high pressure evaporators
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26
Boiling point elevation of an ideal solution
A)Increases rapidly with temperature rise
B)Decreases rapidly with temperature rise
C)In independent of pressure
D)Both (B) and (C)
A)Increases rapidly with temperature rise
B)Decreases rapidly with temperature rise
C)In independent of pressure
D)Both (B) and (C)
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27
Which of the following is concerned with both heat and mass transfer?
A)Lewis relationship
B)Nusselt number
C)Kutateladze number
D)Froude number
A)Lewis relationship
B)Nusselt number
C)Kutateladze number
D)Froude number
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28
The thermal radiative flux from a surface of emissivity = 0.4 is 22.68 kW/m2 . The approximate surface temperature (K) is (Stefan-Boltzmann constant = 5.67 × 10-8 W/m2 .K4 )
A)1000
B)727
C)800
D)1200
A)1000
B)727
C)800
D)1200
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29
Duhring?s rule is important in solving problems on
A)Distillation
B)Crystallisation
C)Evaporation
D)Humidification
A)Distillation
B)Crystallisation
C)Evaporation
D)Humidification
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30
Which is the most suitable for the concentration of foamy & frothy liquors?
A)Agitated film evaporator
B)Long tube vertical evaporator
C)Open pan evaporator
D)None of these
A)Agitated film evaporator
B)Long tube vertical evaporator
C)Open pan evaporator
D)None of these
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31
Heat transfer by radiation between two bodies at T1 & T2 and in an ambient temperature of Ta°C depends on
A)T1 - T2
B)T1 - Ta
C)T2 - Ta
D)None of these
A)T1 - T2
B)T1 - Ta
C)T2 - Ta
D)None of these
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32
Air is best heated with steam in a heat exchanger of
A)Plate type
B)Double pipe type with fin on steam side
C)Double pipe type with fin on air side
D)Shell and tube type
A)Plate type
B)Double pipe type with fin on steam side
C)Double pipe type with fin on air side
D)Shell and tube type
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33
The film thickness for laminar film condensation on vertical surface __________ from top to bottom.
A)Cumulatively increases
B)Cumulatively decreases
C)Remain constant
D)And the surface conductance increase
A)Cumulatively increases
B)Cumulatively decreases
C)Remain constant
D)And the surface conductance increase
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34
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)5.6
B)0.025
C)3.5
D)0.0035
A)5.6
B)0.025
C)3.5
D)0.0035
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35
__________ paint has the minimum absorption co-efficient.
A)Black
B)White lead
C)Grey
D)Light cream
A)Black
B)White lead
C)Grey
D)Light cream
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36
The value of Stefan-Boltzmann constant in SI unit is
A)5.6697 × 10-8W/m2.°K4
B)0.1714 × 10-8W/m2.°K4
C)5.6697 × 10-8kcal/m2. °K4
D)0.1714 × 10-8kcal/m2. °K4
A)5.6697 × 10-8W/m2.°K4
B)0.1714 × 10-8W/m2.°K4
C)5.6697 × 10-8kcal/m2. °K4
D)0.1714 × 10-8kcal/m2. °K4
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37
For shell and tube heat exchanger, with increasing heat transfer area, the purchased cost per unit heat transfer area
A)Increases
B)Decreases
C)Remain constant
D)Passes through a maxima
A)Increases
B)Decreases
C)Remain constant
D)Passes through a maxima
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38
What is the thermal conductivity of a perfect heat insulator?
A)Zero
B)One
C)?
D)Between 0 and ?
A)Zero
B)One
C)?
D)Between 0 and ?
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39
Mode of heat transfer in which the fluid moves under the influence of changes in fluid pressure produced by external work is called
A)Radiation
B)Natural convection
C)Forced convection
D)Conduction
A)Radiation
B)Natural convection
C)Forced convection
D)Conduction
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40
The ratio of momentum diffusivity to thermal diffusivity is the __________ number.
A)Prandtl
B)Nusselt
C)Stanton
D)Grashoff
A)Prandtl
B)Nusselt
C)Stanton
D)Grashoff
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41
Steam traps are provided in steam carrying pipelines to
A)Condense steam
B)Release excess steam pressure by bleeding steam
C)Remove condensate and inert gases
D)None of these
A)Condense steam
B)Release excess steam pressure by bleeding steam
C)Remove condensate and inert gases
D)None of these
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42
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)555
B)55.5
C)0.55
D)0.15
A)555
B)55.5
C)0.55
D)0.15
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43
Kirchoff?s law applies to __________ radiation.
A)Total
B)Monochromatic
C)Both (A) & (B)
D)Neither (A) nor (B)
A)Total
B)Monochromatic
C)Both (A) & (B)
D)Neither (A) nor (B)
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44
Heat transfer occurs by natural convection because change in temperature causes difference in
A)Viscosity
B)Density
C)Thermal conductivity
D)Heat capacity
A)Viscosity
B)Density
C)Thermal conductivity
D)Heat capacity
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45
Log mean temperature difference (LMTD) cannot be used, if
A)Heat transfer co-efficient over the entire heat exchanger is not constant
B)There exists an unsteady state
C)The heat capacity is not constant and there is a phase change
D)None of these
A)Heat transfer co-efficient over the entire heat exchanger is not constant
B)There exists an unsteady state
C)The heat capacity is not constant and there is a phase change
D)None of these
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46
The rate of heat transfer from a vertical plate by natural convection depends upon the temperature differences (?T) between wall and outside bulk. The proportionality is given as
A)(?T) 1/4
B)(?T) 1/2
C)(?T) 5/4
D)(?T) 3/4
A)(?T) 1/4
B)(?T) 1/2
C)(?T) 5/4
D)(?T) 3/4
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47
Pick out the wrong statement.
A)In case of heat transfer by purely forced convection, GR/Re 2 ? 1
B)The equivalent diameter of heat transfer for a duct of square cross-section (having each side as'x') is equal to 4x
C)Distillation process is not the same as evaporation
D)The effectiveness of nucleate boiling depends basically on the ease with which the bubbles are formed and detached from the heating surface
A)In case of heat transfer by purely forced convection, GR/Re 2 ? 1
B)The equivalent diameter of heat transfer for a duct of square cross-section (having each side as'x') is equal to 4x
C)Distillation process is not the same as evaporation
D)The effectiveness of nucleate boiling depends basically on the ease with which the bubbles are formed and detached from the heating surface
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48
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 = hl
B)ha = 2hl
C)ha = 0.5 hl
D)ha = 0.75 hl
A)ha = hl
B)ha = 2hl
C)ha = 0.5 hl
D)ha = 0.75 hl
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49
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)Minimum
B)Maximum
C)Zero
D)Infinity
A)Minimum
B)Maximum
C)Zero
D)Infinity
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50
Harmonic mean temperature difference is given by
A)?(?T1 . ?T2)
B)2 (?T1 . ?T2)/(?T1 + ?T2)
C)2 (?T1 . ?T2)/(?T1 - ?T2)
D)(?T1 - ?T2)/(?T1 . ?T2)
A)?(?T1 . ?T2)
B)2 (?T1 . ?T2)/(?T1 + ?T2)
C)2 (?T1 . ?T2)/(?T1 - ?T2)
D)(?T1 - ?T2)/(?T1 . ?T2)
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