htn 1 Flashcards
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).
D
Heat waves
A. can not pass through vacuum.
B. travel in straight line.
C. can be reflected by a mirror.
D. both (b) and (c).
D
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.
C
Which of the following is generally considered as opaque
surface towards radiations?
A. Gases
B. Solids
C. Liquids
D. Both (b) and (c)
D
Black liquor generated during paper manufacture is
concentrated in a
A. single effect evaporator.
B. single effect evaporator followed by a crystalliser.
C. multiple effect evaporator.
D. multiple effect evaporators followed by a crystalliser.
C
When vaporisation takes place directly at the heating surface, it
is called
A. film boiling
B. nucleate boiling
C. vapour binding
D. none of these
B
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
B. E/C
C. CE
D. 1/CE
A
Reynold’s analogy states that
A. Nst α f
B. Nst α NRe
C. NNu α f
D. NRe α f
A
With increase in temperature, the thermal conductivity of non-
metallic amorphous solids
A. decreases
B. increases
C. remains constant
D. first decreases up to certain temp. & then increases
B
Fourier’s law applies to the heat transfer by
A. convection
B. radiation
C. conduction
D. all (a), (b) & (c)
C
For an ideal black body
A. absorptivity = 1
B. reflectivity = 1
C. emissivity = 0
D. transmissivity = 1
A
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.
D
In the equation Q = UAΔt; Δt
A. geometric mean temperature difference.
B. arithmetic mean temperature difference.
C. logarithmic mean temperature difference.
D. the difference of average bulk temperatures of hot
and cold fluids.
C
With increase in porosity, the thermal conductivity of a solid
substance
A. increases
B. decreases
C. remains unchanged
D. may increase or decrease; depends on the solid
B
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. 40.5
B. 34.4
C. 26.8
D. 25
B
Fouling factor
A. is a dimensionless quantity.
B. does not provide a safety factor for design.
C. accounts for additional resistances to heat flow.
D. none of these.
C
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
B
The steam ejector is used to
A. remove condensate from the steam pipelines.
B. create vacuum.
C. superheat the steam.
D. none of these.
B
For shell and tube heat exchanger, with increasing heat transfer
area, the purchased cost per unit heat transfer area
A. increases
B. decreases
C. remains constant
D. passes through a maxima
D
Presence of a non-condensing gas in a condensing vapour
A. increases the rate of condensation.
B. decreases thermal resistance.
C. is desirable to increase the film co-efficient.
D. none of these.
D
Kirchoff s law applies to __________ radiation.
A. total
B. monochromatic
C. both (a) & (b)
D. neither (a) nor (b)
C
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 = (COP)HP = 0.6
B. (COP)R = 2.5; (COP)HP = 1.5
C. (COP)R = 1.5; (COP)HP = 2.5
D. (COP)R = (COP)HP = 2.5
C
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
B. 37
C. 45
D. 50
A
In a heat exchanger, floating head is provided to
A. facilitate cleaning of the exchanger.
B. increase the heat transfer area.
C. relieve stresses caused by thermal expansion.
D. increase log mean temperature gradient.
C
Leidenfrost point is a term concerned with the
A. condensation of the saturated vapor on a cold
surface.
B. concentration of a corrosive solution by
evaporation.
C. heat transfer between two highly viscous liquids.
D. boiling of a liquid on a hot surface.
D
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.
B. counter flow with process stream on tube side.
C. parallel flow with process stream on shell side.
D. parallel flow with process stream on tube side.
A
Heat produced when a steady state current, I passes through an
electrical conductor having resistance, ‘R’ is
A. IR
B. I^2R
C. IR^2
D. I^2R^2
B
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
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. laminar
B. transition
C. both ‘a’ & ‘b’
D. highly turbulent
D
The actual temperature drop across the heating surface in an
evaporator depends on the
A. feed.
B. depth of liquid over heating surface.
C. pressure difference between steam chest and
vapour space.
D. all (a), (b) and (c).
D
Which of the following is not used as a medium for high
temperature heating?
A. Dowtherm
B. mercury
C. liquid metal (e.g. molten sodium)
D. fused salts (e.g., an eutectic mixture of 53% KNO3,
40% NaNO2and 7% NaNO3)
B
With the increase of temperature, the Col-burn jH factor
A. increases.
B. decreases.
C. remains unchanged.
D. may increase or decrease ; depending on
temperature.
A
In case of evaporators, liquid entrainment results primarily due
to
A. high vacuum in the evaporator.
B. high evaporation rate.
C. foaming of the solution.
D. high heat transfer rate.
C
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.
C
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 inside and
steam outside.
B. finned tube heat exchanger with air outside and
steam inside.
C. shell and tube heat exchanger with air inside tubes
and steam on shell side.
D. shell and tube heat exchanger with air on shell side
and steam inside tubes.
B
The unit of heat transfer co-efficient in SI unit is
A. J/M2°K
B. W/m2°K
C. W/m°K
D. J/m°K
B
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.
B
Increasing the liquor level in the evaporator results in the
A. decreased capacity.
B. increase in liquor film co-efficient.
C. decreased effect of hydrostatic head.
D. increased true temperature drop.
A
Economy of a multiple effect evaporator is not influenced much
by the
A. boiling point elevations
B. temperature of the feed
C. rate of heat transfer
D. ratio of the weight of the thin liquor to thick liquor
A
The number of kg vaporised per kg of steam fed to the
evaporator is defined as
A. capacity
B. rate of evaporation
C. economy
D. rate of vaporisation
C
The equivalent diameter for pressure drop is __________ that
for heat transfer.
A. smaller than
B. greater than
C. equal to
D. not related with
A
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
C
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. 25°C
B. 30°C
C. 35°C
D. 40°C
C
Thermal conductivity of a conducting solid material depends
upon its
A. temperature
B. porosity
C. both (a) & (b)
D. neither (a) nor (b)
C
Pick out the wrong statement.
A. The controlling resistance in case of heating of air
by condensing steam is in the air film.
B. The log mean temperature difference (LMTD) for
counter flow and parallel flow can be theoretically
same when any one of the fluids (hot or cold fluid)
passes through the heat exchanger at constant
temperature.
C. In case of a 1 - 2 shell and tube heat exchanger, the
LMTD correction factor value increases sharply,
when a temperature cross occurs.
D. Phase change in case of a pure fluid at a given
pressure from liquid to vapor or vice-versa occurs at
saturation temperature.
C
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 in physical contact with each
other.
B. between two bodies not in physical contact with
each other.
C. from one part of a body to the another part of the
same body.
D. both ‘b’ & ‘c’
B
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)
2
B. √��
C. (ΔT)
1/4
D. (ΔT)
3/2
C
Bulk of the convective heat transfer resistance from a hot tube
surface to the fluid flowing in it, is
A. in the central core of the fluid.
B. uniformly distributed throughout the fluid.
C. mainly confined to a thin film of fluid near the
surface.
D. none of these.
C
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
A backward feed multiple effect evaporator is better than forward
feed for concentrating cold feed, because it provides
A. higher economy
B. lower capacity
C. both (a) & (b)
D. lower economy
A
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. greater than that for uninsulated steam pipe.
B. less than that of the uninsulated steam pipe.
C. equal to that of the uninsulated steam pipe.
D. less than the steam pipe with 5 cms insulation.
B
Which area is used in case of heat flow by conduction through a
cylinder?
A. Logarithmic mean area
B. Arithmetic mean area
C. Geometric mean area
D. None of these
A
The dimensionless group in mass transfer that is equivalent to
Prandtl number in heat transfer is
A. Nusselt number.
B. Sherwood number.
C. Schmidt number.
D. Stanton number.
C
Finned tube heat exchangers
A. give larger area per tube.
B. use metal fins of low thermal conductivity.
C. facilitate very large temperature drop through tube
wall.
D. are used for smaller heat load.
A
The absorptivity of a grey body at a given temperature
__________ with increasing wavelength of radiation.
A. increases
B. decreases
C. remains constant
D. may increase or decrease ; depends on the material
D
Which one gives the monochromatic emissive power for black
body radiation?
A. Planck’s law
B. Kirchhoffs law
C. Wien’s law
D. Stefan-Boltzman law
A
For what value of Prandtl number, St = f/2?
A. 1.5
B. 1
C. > 1
D. < 1
B
In a shell and tube heat exchanger,
A. the temperature drops in the two fluids and the wall
are proportional to individual resistances.
B. the temperature drop is inversely proportional to the
resistance across which the drop occurs.
C. there is no relationship between temperature drop
and resistance.
D. the relationship is not generalised.
A
Dietus-Boelter equation used for the determination of heat
transfer co-efficient is valid
A. for fluids in laminar flow.
B. for fluids in tubulent flow.
C. when Grashhoff number is very important.
D. for liquid metals.
B
The equation, nst=f/2/ 1+5(Npr-1)..
, corresponds to __ analogy.
A. Von-Karmann
B. Reynolds
C. Colburn
D. Prandtl
D
For large heat transfer area requirement, shell and tube heat
exchanger is preferred, because it
A. occupies smaller space.
B. is more economical.
C. is easy to operate and maintain.
D. all (a), (b) and (c).
D
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 overall heat transfer co-efficient.
B. Constant rate of fluid flow.
C. Constant specific heat.
D. No partial phase change in the system.
B
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. convection becomes important
B. conduction becomes important
C. radiation becomes important
D. sub-cooled boiling occurs
C
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 l05
B. 6.12 x 105
C. 7.24 x 105
D. 9.08 x 105
A
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. t
B. 1/ρ
C. 1/A
D. all (a), (b) & (c)
D
Temperature profile in steady state heat transfer is
A. asymptotic
B. hyperbolic
C. parabolic
D. linear.
D
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. decreases the pressure drop.
B. decreases the outlet temperature of cooling
medium.
C. increases the overall heat transfer coefficient.
D. none of these.
C
When vaporisation takes place through a blanketting film of gas,
the phenomenon is termed as __________ boiling.
A. pool
B. nucleate
C. transition
D. film
D
Minimum recommended baffle spacing in a shell and tube heat
exchanger is about (where, D = shell diameter)
A. 0.2 D
B. 0.5 D
C. 0.66 D
D. 0.80 D
A
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
B. T4
C. 1/t
4
D. 1/T4
B
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. 2.36
B. 4.36
C. 120.36
D. dependent on NRe only
B
What is the unit of thermal conductivity?
A. Kcal/hr. m2 °C
B. Kcal/hr.m.°C
C. Kcal/hr.m
D. Kcal/hr. °C
B
The thermal radiation emitted by a body is proportional to Tn,
where T is its absolute temperature. The value of ‘n’ is exactly 4
for
A. black painted bodies only
B. all bodies
C. polished bodies only
D. a black body
B
In forced convection, the heat transfer depends on
A. Re, Pr
B. Re, Gr
C. mainly Gr
D. Re only
A
In forced convection, the heat transfer depends on
A. Re, Pr
B. Re, Gr
C. mainly Gr
D. Re only
C
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).
B. outlent temperature of both the hot and cold fluid are
same.
C. outlet temperature of hot fluid is less than the outlet
temperature of the cold fluid.
D. none of these.
A
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
B. NPr1/3
C. NPr-1
D. NPr-1/3
B
The range of electromagnetic spectrum important in heat
transfer by radiation is __________ microns.
A. 0.38-0.78
B. 0.5-50
C. 100-1000
D. 5-50
B
Use of transverse baffles in a shell and tube heat exchanger is
done to increase the
A. rate of heat transfer.
B. flow velocity.
C. turbulence of shell side fluid.
D. all (a), (b) and (c).
D
Use of transverse baffles in a shell and tube heat exchanger is
done to increase the
A. rate of heat transfer.
B. flow velocity.
C. turbulence of shell side fluid.
D. all (a), (b) and (c).
D
Economy of a multiple effect evaporator depends upon the
A. heat balance consideration
B. rate of heat transfer
C. both (a) and (b)
D. neither (a) nor (b)
A
Economy of a multiple effect evaporator depends upon the
A. heat balance consideration
B. rate of heat transfer
C. both (a) and (b)
D. neither (a) nor (b)
A
Economy of a multiple effect evaporator depends upon the
A. heat balance consideration
B. rate of heat transfer
C. both (a) and (b)
D. neither (a) nor (b)
A
Solid angle subtended by the finite surface at the radiating
element is
A. called the view factor.
B. called the angle of vision.
C. proportional to the square of the distance between
surfaces.
D. expressed in terms of radians.
B
Pick out the wrong statement.
A. The emissivity of a surface decreases, if it gets
corroded by atmospheric environment.
B. The emissivity of a surface increases with increase in
surface roughness.
C. The emissivity of a polished surface is quite low.
D. The emissivity of a non-metallic surface decreases
with increase in the temperature.
A
With increase in temperature, the thermal conductivity of most
liquids
A. increases
B. decreases
C. remains same
D. first increases upto a certain temperature and then
becomes constant
B
Heat transfer by __________ may not necessarily require the
presence of a medium.
A. conduction
B. natural convection
C. forced convection
D. radiation
D
Pick out the correct statement.
A. Higher is the temperature of the radiating body, higher
is the wavelength of radiation.
B. Logarithmic mean area is used for calculating the heat
flow rate through a thick walled cylinder.
C. The wavelength corresponding to maximum mono-
chromatic emissive power increases with rise in
temperature.
D. Solid angle subtended by the finite surface at the
radiating element is called the angle of incidence.
B
In a shell and tube type heat exchanger, the floating tube bundle
heat arrangement is used
A. in low range of temperature differences.
B. in high range of temperature differences.
C. because of its low cost.
D. to prevent corrosion of the tube bundles.
B
Stefan-Boltzman law applies to __________ body.
A. black
B. white
C. grey
D. any colour
A
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. more
B. less
C. some
D. either more or less ; depends on the nature of
vapo
C
A perfect black body is a perfect __________ of radiation.
A. absorber
B. emitter
C. both (a) & (b)
D. neither (a) nor (b)
C
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
B. more than
C. less than
D. either more or less than (depending upon the fluid)
A
An equipment which converts the latent or sensible heat of one
fluid into the latent heat of vaporisation of another, is called a
A. boiler
B. heat exchanger
C. recuperator
D. regenerator
B
Which of the following is directly concerned with the heat
transfer?
A. Strouhal number
B. Sherwood number
C. Euler number
D. Grashoff number
D
Pick out the wrong statement:
A. With change in temperature, the radiant energy emitted
by a black body remains unchanged.
B. Absorptivity of a body approaches unity in case of
diffuse reflection.
C. Absorptivity of a perfectly black body is unity.
D. Value of Stefan-Boltzman constant is 4.876 x 10
8KCal/m2.hr.°K4
A
Planck’s distribution law is valid for __________ bodies.
A. black
B. white
C. coloured
D. all (a), (b) & (c)
D
For hot feed, forward feeding as compared to backward feeding
results in __________ economy.
A. increased
B. decreased
C. no effect on
D. none of these
A
Radiation energy is emitted by all the substances, which are
above
A. 0°K
B. 0°C
C. 100°C
D. room temperature
A
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
B. εx . εy
C. 1/EX+ 1/EY
D.EX+EY/EX+EY - EX*EY
∙
D
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
B
What is the steam economy in case of a single effect evaporator
system?
A. 1
B. >1
C. < 1
D. 0.1
C
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
B
jH factor for heat transfer is not a function of the __________
number.
A. Reynolds
B. Nusselt
C. Grashoff
D. both (b) & (c)
D
The Fourier number (defined as a.t/L2) is used in the analysis of
problem involving heat transfer by
A. forced convection
B. natural convection
C. transient conduction
D. steady state conduction
C
The energy radiated from a surface Q at absolute
temperature T is related as
A. Q ∝ T2
B. Q ∝ T4
C. Q ∝ T3
D. none of these
B
Baffles are provided in heat exchangers to increase the
A. fouling factor
B. heat transfer area
C. heat transfer co-efficient
D. heat transfer rate
C
In case of a vertical tube evaporator, with increase in the liquor
level, the
A. capacity of the evaporator is decreased.
B. capacity of the evaporator is increased.
C. true temperature drop increases.
D. both (b) and (c).
A
The ratio of total radiating power to the absorptivity of the body
depends upon the __________ as per Kirchoffs law.
A. wavelength of radiation
B. nature of the body
C. temperature of the body
D. none of these
C
For gases, the thermal conductivity increases with temperature
rise. For liquids, with increase in concentration, its thermal
conductivity generally
A. decreases
B. increases
C. remains unchanged
D. increases exponentially
A
A 2-4 heat exchanger involves
A. only counter-flow of fluids.
B. only parallel-flow of fluids.
C. both counter and parallel-flow of the fluids.
D. smaller pressure drop compared to 1-2 exchanger.
C
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
B. > 1
C. 1
D. ∞
A
With increase in temperature, the thermal conductivity of steel
A. increases
B. decreases
C. remains unchanged
D. increases exponentially
B
Which of the following forced convection heat transfer equation
accounts for the liquid viscosity effect for viscous liquids?
A. Dittus-Boeltier equation
B. Sieder-Tate equation
C. Nusselt equation
D. None of these
B
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’.
B
In a single effect evaporator, the economy is
A. 1
B. < 1
C. > 1
D. none of these
B
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. 0
B. 1
C. >1
D. <1
D
Which of the following is not concerned with the heat transfer?
A. Brinkman number
B. Stanton number
C. Schmidt number
D. Peclet number
C
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
B. 970
C. 3.97
D. none of these
A
In counter flow compared to parallel flow,
A. LMTD is greater.
B. less surface area is required for a given heat transfer
rate.
C. both (a) and (b).
D. more surface area is required for a given heat
transfer rate.
C
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
B. 727
C. 800
D. 1200
A
Crystallisation of solids from a homogeneous solution is a/an
__________ process.
A. exothermic
B. mildly endothermic
C. highly endothermic
D. none of these
A
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. 6000
B. 24000
C. 60000
D. 48000
B
Value of Prandtl number for water ranges from
A. l to 2
B. 5 to 10
C. 100 to 500
D. 1000 to 2000
B
Heat transfer in the laminar sublayer in case of a liquid flowing
through a pipe, is mostly by
A. eddies current
B. conduction
C. convection
D. none of these
B
Among liquids, water has a comparatively high value of thermal
conductivity, due to its
A. low density
B. high viscosity
C. partial ionisation
D. dense structure
C
Reynold’s analogy states that (where, St = Stanton number f =
friction factor)
A. St = f/2
B. St = f/4
C. St = 4f
D. St = f^1/2
A
For evaporation of viscous solution in a multiple effect
evaporator, the prefered feeding scheme is
A. forward
B. backward
C. parallel
D. none of these
B
The sum of reflectivity and absorptivity for an opaque body is
equal to
A. 0.5
B. 1
C. 0
D. 2
B
The film thickness for laminar film condensation on vertical
surface __________ from top to bottom.
A. cummulatively increases
B. cummulatively decreases
C. remains constant
D. and the surface conductance increase
A
In case of a multipass shell and tube heat exchanger, providing
a baffle on the shell side __________ the heat transfer rate.
A. increases
B. decreases
C. does not affect
D. may increase or decrease, depends on the type of
baffle
A
The local surface conductance for laminar film condensation on
vertical surface is (where, t = film thickness)
A. ∝ t
B. ∝ 1/t
C. ∝ √𝑡
D. independent of ‘t’
B
Heat transfer co-efficient (h1) for liquids increases with
A. increasing temperature.
B. decreasing temperature.
C. decreasing Reynolds number.
D. none of these.
A
A diathermaneous substance __________ the thermal radiation
completely.
A. absorbs
B. reflects
C. transmits
D. none of these
C
A hot body will radiate heat most rapidly, if its surface is
A. white & rough
B. black & rough
C. white & polished
D. black & polished
B
Evaporation of 1kg of water from a solution in a single effect
evaporator requires about __________ kg of steam.
A. 0.4 - 0.6
B. 1-1.3
C. 1.8-2
D. 2 - 2.4
B
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
B
Analogy between mass and heat transfer is not applicable in
case of
A. same velocity profile or equal eddy diffusivities.
B. thermal or pressure mass diffusion.
C. viscous heating or chemical reaction.
D. both (b) and (c).
D
A __________ surface has the maximum thermal emissivity out
of the following.
A. black & smooth
B. black & rough
C. white & smooth
D. white & rough
B
Radiant energy received by a body is proportional to (where, d =
the distance between the object emitting radiation and that
receiving it.)
A. √𝑑
B. d
C. d^2
D. d^1.5
C
Mechanical recompression evaporation is used in the production
of
A. alcohol
B. distilled water
C. salt
D. fruits jam
B
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. Condensation
B. Grashoff
C. Stantan
D. Brinkman
D
The purpose of providing a ‘catchall’ in the vapor line of an
evaporator is to
A. create vacuum
B. regulate the vapor flow
C. vent the non-condensible gases
D. arrest the entrained liquid
D
What is the thermal conductivity of a perfect heat insulator?
A. zero
B. one
C. ∞
D. between 0 and ∞
A
‘Fouling factor’ used in the design of a multipass shell and tube
heat exchanger is a
A. non-dimensional factor.
B. factor of safety.
C. conversion factor for individual film heat transfer co
efficient to overall heat transfer co-efficient.
D. none of these.
B
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^0.8
B. d^-0.2
C. d^-1
D. d^-1.8
B
Prandtl and Reynolds analogy are same, when Prandtl number
is
A. 0.5
B. 1
C. > 2
D. 1.5
B
Heat transfer occurs by natural convection because change in
temperature causes difference in
A. viscosity
B. density
C. thermal conductivity
D. heat capacity
B
The ratio of kinematic viscosity to thermal diffusivity is called the
__________ number.
A. Peclet
B. Prandtl
C. Stanton
D. Nusselt
B
The critical radius ‘r’ of insulation on a pipe is given by
A. r = 2k/h
B. r = k/h
C. r = k/2h
D. r = h/k
B
________ paint has the maximum absorption coefficient.
A. Black
B. Yellow
C. White
D. Grey
A
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.
B. wavelength of monochromatic radiation.
C. both (a) and (b).
D. nature of material of body.
A
If the baffle spacing in a shell and tube heat exchanger
increases, then the Reynolds number of the shell side fluid
A. remains unchanged.
B. increases.
C. increases or decreases depending on number of shell
passes.
D. decreases.
D
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 black.
B. painting the surface white (with aluminium paint).
C. giving the surface a mirror finish.
D. roughening the surface.
B
What is Nusselt number?
A. Cp u/ k
B. hD/k
C. h Cp/ u
D. Cp u /h
B
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.
C
The Dietus-Boelter equation for convective heat transfer (i.e.,
ℎ=0.023 K/D 𝑅𝑒^0.8𝑃𝑟^0.4 ) cannot be used for
A. low Reynold’s number
B. very low Grashoff number
C. molten metals
D. all (a), (b) and (c)
D
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. ellipse
B. straight line
C. parabola
D. circular arc
B
Radiation heat transfer rates does not depend upon the
A. type of absorbing surface.
B. distance between the heat source and the object
receiving the heat.
C. surface area and temperature of the heat source.
D. none of these
D
Which of the following is correct?
A. Rate = Driving force x Resistance
B. Driving force = Rate x Resistance
C. Resistance = Driving force x Rate
D. Rate = Resistance/Driving force
B
Film condensation is promoted on a/an __________ surface.
A. oily
B. coated
C. clean & smooth
D. dirty
C
Convective heat transfer, in which heat is transferred by
movement of warmed matter is described by
A. Fourier’s law
B. Newton’s law of cooling
C. Fick’s law
D. none of these
B
As the difference between the wall temperature and bulk
temperature increases, the boiling heat transfer co-efficient
A. continues to increase.
B. continues to decrease.
C. goes through a minimum.
D. goes through a maximum.
C
Heat transfer rate per unit area is called
A. thermal conductivity
B. heat flux
C. heat transfer co-efficient
D. thermal diffusivity
B
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.
D
In a multipass shell and tube heat exchanger, tube side return
pressure loss is equal to __________ the velocity head.
A. twice
B. four times
C. square root of
D. square of
B