Deck 5: Heat Transfer and Evaporator
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Deck 5: Heat Transfer and Evaporator
1
The actual temperature drop across the heating surface of an evaporator depends on the
A)Liquid depth over the heating surface
B)Solution being evaporated
C)Pressure difference between the steam chest and the vapor space above the boiling liquid
D)All (A), (B) and (C)
A)Liquid depth over the heating surface
B)Solution being evaporated
C)Pressure difference between the steam chest and the vapor space above the boiling liquid
D)All (A), (B) and (C)
All (A), (B) and (C)
2
In SI units, thermal conductivity is expressed in
A)Watt/m.°K
B)Watt/m2. °K
C)Watt/m2. °K.
D)Watt/m4. °K.
A)Watt/m.°K
B)Watt/m2. °K
C)Watt/m2. °K.
D)Watt/m4. °K.
Watt/m.°K
3
jH factor for heat transfer depends upon the __________ number.
A)Biot
B)Nusselt
C)Reynolds
D)Prandtl
A)Biot
B)Nusselt
C)Reynolds
D)Prandtl
Reynolds
4
In pipe flow, heat is transferred from hot wall to the liquid by
A)Conduction only
B)Forced convection only
C)Forced convection and conduction
D)Free and forced convection
A)Conduction only
B)Forced convection only
C)Forced convection and conduction
D)Free and forced convection
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5
A perfect black body is a perfect __________ of radiation.
A)Absorber
B)Emitter
C)Both (A) & (B)
D)Neither (A) nor (B)
A)Absorber
B)Emitter
C)Both (A) & (B)
D)Neither (A) nor (B)
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6
Heat transfer rate described by Fourier's law will decrease, if the __________ increases.
A)Thermal conductivity
B)Thickness
C)Temperature difference
D)Heat transfer area
A)Thermal conductivity
B)Thickness
C)Temperature difference
D)Heat transfer area
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7
The absorptivity of a body is equal to its emissivity
A)At a particular temperature
B)For circular bodies
C)Under thermal equilibrium
D)None of these
A)At a particular temperature
B)For circular bodies
C)Under thermal equilibrium
D)None of these
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8
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)Increase
B)Decrease
C)Remain unchanged
D)Either increase or decrease; depends on the coolant flow rate
A)Increase
B)Decrease
C)Remain unchanged
D)Either increase or decrease; depends on the coolant flow rate
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9
The inner wall of a furnace is at a temperature of 700°C. The composite wall is made of two substances, 10 and 2 0 cm thick with thermal conductivities of 0.05 and 0.1 W.m-1 .°C1 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 -2 is
A)165.4
B)167.5
C)172.5
D)175
A)165.4
B)167.5
C)172.5
D)175
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10
Which one gives the monochromatic emissive power for black body radiation?
A)Planck's law
B)Kirchhoff's law
C)Wien's law
D)Stefan-Boltzmann law
A)Planck's law
B)Kirchhoff's law
C)Wien's law
D)Stefan-Boltzmann law
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11
If heat transfer rate varies with the time, it is termed as
A)Forced convection
B)Steady state conduction
C)Monochromatic radiation
D)None of these
A)Forced convection
B)Steady state conduction
C)Monochromatic radiation
D)None of these
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12
Absorptivity and reflectivity of a perfect black body are respectively
A)1 and 0
B)0 and 1
C)1 and ?
D)0 and 0.5
A)1 and 0
B)0 and 1
C)1 and ?
D)0 and 0.5
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13
__________ heat exchanger is used for chilling oil to be dewaxed.
A)U-tube
B)Double pipe
C)Fixed tube
D)Floating head
A)U-tube
B)Double pipe
C)Fixed tube
D)Floating head
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14
Pick out the correct equation.
A)jH = (St)(Pr) 2/3 = f/2
B)jH = (St)(Pr) 1/3 = f/2
C)jH = (St) 2/3(Pr) = f/2
D)jH = (St) 1/3(Pr) = f/2
A)jH = (St)(Pr) 2/3 = f/2
B)jH = (St)(Pr) 1/3 = f/2
C)jH = (St) 2/3(Pr) = f/2
D)jH = (St) 1/3(Pr) = f/2
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15
It is not preferable to use superheated steam in evaporators, because of its very
A)High temperature
B)High pressure
C)Low film co-efficient
D)None of these
A)High temperature
B)High pressure
C)Low film co-efficient
D)None of these
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16
Water is normally used as a coolant in the heat exchange equipments mainly because of its
A)Abundance & high heat capacity
B)Low density
C)Low viscosity
D)High fluidity
A)Abundance & high heat capacity
B)Low density
C)Low viscosity
D)High fluidity
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17
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
B)2 0.8
C)2 0.2
D)2 0.5
A)2
B)2 0.8
C)2 0.2
D)2 0.5
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18
At constant temperature, the thermal conductivities of gases __________ with rise in pressure.
A)Decrease
B)Increase
C)Remain unchanged
D)May increase or decrease; depends on the pressure
A)Decrease
B)Increase
C)Remain unchanged
D)May increase or decrease; depends on the pressure
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19
Stefan-Boltzmann law applies to __________ body.
A)Black
B)White
C)Grey
D)Any colour
A)Black
B)White
C)Grey
D)Any colour
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20
When warm and cold liquids are mixed, the heat transfer is mainly by
A)Conduction
B)Convection
C)Radiation
D)Both (A) & (C)
A)Conduction
B)Convection
C)Radiation
D)Both (A) & (C)
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21
A BTU/hr.ft.2 °F is equal to
A)1 kcal/hr. m2 °C
B)4.88 kcal/hr. m.2 °C
C)1 kcal/hr. m2 .°K
D)None of these
A)1 kcal/hr. m2 °C
B)4.88 kcal/hr. m.2 °C
C)1 kcal/hr. m2 .°K
D)None of these
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22
Open pan evaporators are preferred to be used, when the solution to be concentrated is
A)Scaling
B)Highly viscous
C)Corrosive
D)Salty
A)Scaling
B)Highly viscous
C)Corrosive
D)Salty
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23
A __________ evaporator employs an annular downtake.
A)Basket type
B)Horizontal
C)Long tube vertical
D)None of these
A)Basket type
B)Horizontal
C)Long tube vertical
D)None of these
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24
The equation, Nst = (f/2)/[1 + 5 (NPr - 1) ?(f/2)], corresponds to __________ analogy.
A)Von-Karman
B)Reynolds
C)Colburn
D)Prandtl
A)Von-Karman
B)Reynolds
C)Colburn
D)Prandtl
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25
The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is
A)Lower tube side pressure drop
B)Lower shell side pressure drop
C)Higher tube side heat transfer co-efficient
D)Higher shell side heat transfer co-efficient
A)Lower tube side pressure drop
B)Lower shell side pressure drop
C)Higher tube side heat transfer co-efficient
D)Higher shell side heat transfer co-efficient
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