Q.1

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 arekg/m3 and 0.4 kJ/kg.K respectively. The heat transfer co-efficient isW/m2.K Neglecting the temperature gradients inside the ball, the time taken (in hours) for the ball to cool to 60°C is

  • 555
  • 55.5
  • 0.55
  • 0.15
Q.2

What is the unit of thermal conductivity ?

  • Kcal/hr. m2 °C
  • Kcal/hr.m.°C
  • Kcal/hr.m
  • Kcal/hr. °C
Q.3

Heat transfer by __________ may not necessarily require the presence of a medium.

  • conduction
  • natural convection
  • forced convection
  • radiation
Q.4

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)

  • NPr
  • NPr1/3
  • NPr-1
  • NPr-1/3
Q.5

A perfect black body is a perfect __________ of radiation.

  • absorber
  • emitter
  • both (a) & (b)
  • neither (a) nor (b)
Q.6

Which one gives the monochromatic emissive power for black body radiation ?

  • Planck's law
  • Kirchhoffs law
  • Wien's law
  • Stefan-Boltzman law
Q.7

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

  • decreases the pressure drop.
  • decreases the outlet temperature of cooling medium.
  • increases the overall heat transfer coefficient.
  • none of these.
Q.8

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

  • black painted bodies only
  • all bodies
  • polished bodies only
  • a black body
Q.9

Which of the following is unimportant in forced convection ?

  • Reynolds number
  • Prandtl number
  • Grashhoff number
  • none of these
Q.10

__________ chart is known as transient heat conduction chart.

  • Dirhing's
  • Heisler's
  • Mollier's
  • Cox
Q.11

Pick out the correct statement.

  • Higher is the temperature of the radiating body, higher is the wavelength of radiation.
  • Logarithmic mean area is used for calculating the heat flow rate through a thick walled cylinder.
  • The wavelength corresponding to maximum mono-chromatic emissive power increases with rise in temperature.
  • Solid angle subtended by the finite surface at the radiating element is called the angle of incidence.
Q.12

In a shell and tube type heat exchanger, the floating tube bundle heat arrangement is used

  • in low range of temperature differences.
  • in high range of temperature differences.
  • because of its low cost.
  • to prevent corrosion of the tube bundles.
Q.13

The range of electromagnetic spectrum important in heat transfer by radiation is __________ microns.

  • 0.38-0.78
  • 0.5-50
  • 100-1000
  • 5-50
Q.14

In case of parallel flow heat exchanger, the lowest temperature theoretically attainable by the hot fluid is __________ the outlet temperature of the cold fluid.

  • equal to
  • more than
  • less than
  • either more or less than (depending upon the fluid)
Q.15

An equipment which converts the latent or sensible heat of one fluid into the latent heat of vaporisation of another, is called a

  • boiler
  • heat exchanger
  • recuperator
  • regenerator
Q.16

For what value of Prandtl number, St = f/2?

  • 1.5
  • 1
  • > 1
  • < 1
Q.17

When vaporisation takes place through a blanketting film of gas, the phenomenon is termed as __________ boiling.

  • pool
  • nucleate
  • transition
  • film
Q.18

Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter)

  • 0.2 D
  • 0.5 D
  • 0.66 D
  • 0.80 D
Q.19

It is not preferable to use superheated steam in evaporators, because of its very

  • high temperature
  • high pressure
  • low film co-efficient
  • none of these
Q.20

Steam is to be condensed in a shell and tube heat exchanger, 5 m long with a shell diameter of 1 m. Cooling water is to be used for removing the heat. Heat transfer co-efficient for the cooling water, whether on shell side or tube side is the same. The best arrangement is

  • vertical heat exchanger with steam on tube side.
  • vertical heat exchanger with steam on shell side.
  • horizontal heat exchanger with steam on tube side.
  • horizontal heat exchanger with steam on shell side.
Q.21

Film boiling occurs at __________ pressure.

  • atmospheric
  • sub-atmospheric
  • negative
  • very high
Q.22

Which of the following is correct ?

  • Rate = Driving force x Resistance
  • Driving force = Rate x Resistance
  • Resistance = Driving force x Rate
  • Rate = Resistance/Driving force
Q.23

In a multipass shell and tube heat exchanger, tube side return pressure loss is equal to __________ the velocity head.

  • twice
  • four times
  • square root of
  • square of
Q.24

Nusselt number (for forced convection heat transfer) is a function of the __________ number.

  • Prandtl
  • Reynolds
  • both (a) & (b)
  • neither (a) nor (b)
Q.25

Stefan-Boltzman law applies to __________ body.

  • black
  • white
  • grey
  • any colour
Q.26

Use of transverse baffles in a shell and tube heat exchanger is done to increase the

  • rate of heat transfer.
  • flow velocity.
  • turbulence of shell side fluid.
  • all (a), (b) and (c).
Q.27

Which of the following is directly concerned with the heat transfer ?

  • Strouhal number
  • Sherwood number
  • Euler number
  • Grashoff number
Q.28

In a shell and tube heat exchanger,

  • the temperature drops in the two fluids and the wall are proportional to individual resistances.
  • the temperature drop is inversely proportional to the resistance across which the drop occurs.
  • there is no relationship between temperature drop and resistance.
  • the relationship is not generalised.
Q.29

Dietus-Boelter equation used for the determination of heat transfer co-efficient is valid

  • for fluids in laminar flow.
  • for fluids in tubulent flow.
  • when Grashhoff number is very important.
  • for liquid metals.
Q.30

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 )

  • t4
  • T4
  • 1/t4
  • 1/T4
Q.31

The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

  • 2.36
  • 4.36
  • 120.36
  • dependent on NRe only
Q.32

It is desired to concentrate asalt solution (kg of salt inkg of solution) to asalt solution in an evaporator. Consider a feed ofkg/min at 30°C. The boiling point of the solution is 110°C, the latent heat of vaporisation iskJ/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

  • 3.06 x l05
  • 6.12 x 105
  • 7.24 x 105
  • 9.08 x 105
Q.33

LMTD for counterflow and prallel flow heat exchanger will be the same, when the

  • cold fluid is heated to a certain temperature by condensing steam (isothermal fluid).
  • outlent temperature of both the hot and cold fluid are same.
  • outlet temperature of hot fluid is less than the outlet temperature of the cold fluid.
  • none of these.
Q.34

In a multiple effect evaporator, the effect of boiling point elevation is to

  • reduce the capacity
  • reduce the economy
  • increase the economy
  • none of these
Q.35

Steam traps are provided in steam carrying pipelines to

  • condense steam.
  • release excess steam pressure by bleeding steam.
  • remove condensate and inert gases.
  • none of these.
Q.36

Heat flux through several resistances in series in analogous to the current flowing through several

  • resistances in parallel.
  • capacitors in series.
  • resistances in series.
  • none of these.
Q.37

Convective heat transfer, in which heat is transferred by movement of warmed matter is described by

  • Fourier's law
  • Newton's law of cooling
  • Fick's law
  • none of these
Q.38

As the difference between the wall temperature and bulk temperature increases, the boiling heat transfer co-efficient

  • continues to increase.
  • continues to decrease.
  • goes through a minimum.
  • goes through a maximum.
Q.39

For a given ambient air temperature with increase in the thickness of insulation of a hot cylinderical pipe, the rate of heat loss from the surface would

  • decrease
  • increase
  • first decrease and then increase
  • first increase and then decrease
Q.40

Pick out the wrong statement.

  • Heat transfer by radiation can not occur across an absolute volume.
  • In case of a shell and tube heat exchanger, the pressure drop through the shell is proportional to the number of times the fluid crosses the bundle between baffles.
  • Propagation velocity for travel of heat radiation through vacuum is equal to the velocity of the light.
  • The amount of heat involved in the condensation or vaporisation of 1 kg of a fluid is the same.
Q.41

Which type of heat exchanger is preferred for heavy heat loads ?

  • Double pipe
  • Plate fine
  • Series and parallel set of shell and tube
  • None of these
Q.42

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

  • more
  • less
  • some
  • either more or less ; depends on the nature of vapor
Q.43

For specified tube outside diameter, higher BWG means higher

  • tube thickness
  • cross-sectional area
  • weight per unit length
  • none of these
Q.44

The actual temperature drop across the heating surface of an evaporator depends on the

  • liquid depth over the heating surface.
  • solution being evaporated.
  • pressure difference between the steam chest and the vapor space above the boiling liquid.
  • all (a), (b) and (c)
Q.45

Economy of a multiple effect evaporator depends upon the

  • heat balance consideration
  • rate of heat transfer
  • both (a) and (b)
  • neither (a) nor (b)
Q.46

If Prandtl number is greater than the Schmidt number, then the

  • thermal boundary layer lies inside the concentration boundary layer.
  • concentration boundary layer lies inside the thermal boundary layer.
  • thermal & concentration boundary layers are of equal thickness.
  • hydrodynamic(i.e., momentum)boundary layer is thicker than the other two.
Q.47

Pick out the wrong statement:

  • With change in temperature, the radiant energy emitted by a black body remains unchanged.
  • Absorptivity of a body approaches unity in case of diffuse reflection.
  • Absorptivity of a perfectly black body is unity.
  • Value of Stefan-Boltzman constant is 4.876 x 10-8 KCal/m2.hr.°K4.
Q.48

Extended heat transfer surface like fins are used to increase the heat transfer rate. Fin efficiency is defined as the ratio of heat transferred across the fin surface to the theoretical heat transfer across an equal area held at the

  • surrounding temperature.
  • average temperature of the fin.
  • temperature of the fin end.
  • constant temperature equal to that of the base
Q.49

Vacuum is generally maintained in the vapour space of an evaporator mainly to

  • get economical temperature difference by using moderate pressure steam.
  • facilitate forward feeding in multiple effect evaporation.
  • concentrate heat sensitive materials.
  • achieve very high concentration of the final product.
Q.50

Heat transfer efficiency leading of energy conservation in a heat exchanger can be achieved by

  • keeping the heat transfer surface clean.
  • enhancing the fluid pumping rate.
  • increasing the tube length.
  • none of these.
0 h : 0 m : 1 s