Heat Transfer 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) all (a), (b) and (c).
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) both (b) and (c).
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) double pipe type with fin on air side.
Which of the following is generally considered as opaque surface towards radiations?
a) Gases
b) Solids
c) Liquids
d) Both (b) and (c)
d) Both (b) and (c)
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) multiple effect evaporator.
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) nucleate boiling
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) C/E
Reynold’s analogy states that
a) Nst α f
b) Nst α NRe
c) NNu α f
d) NRe α f
a) Nst α f
With increase in temperature, the thermal conductivity of non-metallic amorphous solids
a) decreases
b) increases
c) remains constant
d) first decreases upto certain temperature and then increases
b) increases
Fourier’s law applies to the heat transfer by
a) convection
b) radiation
c) conduction
d) all (a), (b) & (c)
c) conduction
Shell side pressure drop in a shell and tube heat exchanger does not depend upon the
baffle spacing & shell diameter.
a) tube diameter & pitch.
b) viscosity, density & mass
c) velocity of shell side fluid.
d) none of these.
d) none of these.
In the equation Q = UAΔt; Δt is
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) logarithmic mean temperature difference.
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) decreases
For an ideal black body
a) absorptivity = 1
b) reflectivity = 1
c) emissivity = 0
d) transmissivity = 1
a) absorptivity = 1
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) accounts for additional resistances to heat flow.
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) decreases
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) create vacuum.
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) passes through a maxima
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) relieve stresses caused by thermal expansion.
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) boiling of a liquid on a hot surface.
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) counter flow with process stream on shell side.
Heat produced when a steady state current, I passes through an electrical conductor having resistance, ‘R’ is
a) IR
b) (I^2)R
c) IR^2
d) (I^2)(R^2)
b) (I^2)R
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.
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) highly turbulent
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) all (a), (b) and (c).
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) mercury
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) none of these.
Kirchoff s law applies to __________ radiation.
a) total
b) monochromatic
c) both (a) & (b)
d) neither (a) nor (b)
c) both (a) & (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) increases.
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) foaming of the solution.
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) increase the shell side heat transfer co-efficient.
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) finned tube heat exchanger with air outside and steam inside.
The unit of heat transfer co-efficient in SI unit is
a) J/M^2°K
b) W/m^2°K
c) W/m°K
d) J/m°K
b) W/m^2°K
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) economy
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) The equivalent diameter of heat transfer for a duct of square cross-section (having each side as ‘x’) is equal to 4x.
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) boiling point elevations
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) decreased capacity.
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) smaller than
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 largest
Thermal conductivity of a conducting solid material depends upon its
a) temperature
b) porosity
c) both (a) & (b)
d) neither (a) nor (b)
c) both (a) & (b)
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) In case of a 1 - 2 shell and tube heat exchanger, the LMTD correction factor value increases sharply, when a temperature cross occurs.
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) √ΔT
c) (ΔT)^(1/4)
d) (ΔT)^(3/2)
c) (ΔT)^(1/4)
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) mainly confined to a thin film of fluid near the surface.
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
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) higher economy
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) Logarithmic mean area
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) between two bodies not in physical contact with each other.
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) Schmidt number.
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) give larger area per tube.
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) may increase or decrease ; depends on the material
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) Planck’s law
For what value of Prandtl number, St = f/2?
a) 1.5
b) 1
c) > 1
d) < 1
b) 1
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) the temperature drops in the two fluids and the wall are proportional to individual resistances.
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) for fluids in tubulent flow.
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) all (a), (b) and (c).
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) Constant rate of fluid flow.