Heat Transfer Flashcards
(140 cards)
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