Q.1

Value of Nusselt number [Nu = (hD/k)] for the heat transfer by conduction from a droplet or a spherical particle to a surrounding stagnant film is

  • 0.5
  • 2
  • 10
  • 100
Q.2

At constant temperature, the thermal conductivities of gases __________ with rise in pressure.

  • decrease
  • increase
  • remain unchanged
  • may increase or decrease; depends on the pressure
Q.3

Mode of heat transfer involved in the cooling of air cooled internal combustion engine is

  • conduction
  • natural convection
  • forced convection
  • none of these
Q.4

For __________ Prandtl number values, the heat conduction will be negligible in the buffer zone.

  • extremely low
  • low
  • high
  • no
Q.5

A __________ evaporator employs an annular downtake.

  • basket type
  • horizontal
  • long tube vertical
  • none of these
Q.6

In Biot number, the characteristic length used is the ratio of the __________ of the solid.

  • volume to surface area
  • perimeter to surface area
  • surface area to volume
  • surface area to perimeter
Q.7

At constant temperature, the thermal conductivities of gases __________ with rise in pressure.

  • decrease
  • increase
  • remain unchanged
  • may increase or decrease; depends on the pressure
Q.8

In a heat exchanger with steam outside the tubes, a liquid gets heated to 45°C, when its flow velocity in the tubes is 2 m/s. If the flow velocity is reduced to 1 m/s, other things remaining the same, the temperature of the exit liquid will be

  • less than 45°C
  • more than 45°C
  • equal to 45°C
  • initially decreases and remains constant thereafter.
Q.9

The purpose of providing expansion bellows in the shell of tubular exchanger is to

  • increase the heating load.
  • impart structural strength.
  • account for the uneven expansion of shell and tube bundles.
  • facilitate increase of shell length, if needed.
Q.10

Pick out the wrong statement.

  • 'Solvates' are chemical compounds formed by solute with their solvents. When water is the solvent, then it is called a 'hydrate'.
  • In heat exchanger calculations (Δt)weighted is used in place of Δt, when it involves more than one sequence of heating or cooling i.e., desuperheating & condensation or condensation & sub-cooling.
  • Heat transfer co-efficient during nucleate boiling is not influenced by the agitation imparted.
  • In case of short tube vertical evaporators, area of central downtake is about 50 to 100% of the total tube cross-sectional area.
Q.11

Steady state one dimensional heat flow by conduction as given by Fourier's low does not assume that

  • there is no internal heat generation.
  • boundary surfaces are isothermal.
  • material is anisotropic.
  • constant temperature gradient exists.
Q.12

The radiation heat flux from a heating element at a temperature of 800°C, in a furnace maintained at 300°C is 8 kW/m2. The flux, when the element temperature is increased to 1000°C for the same furnace temperature is

  • 11.2 kW/m2
  • 12.0 kW/m2
  • 14.6 kW/m2
  • 16.5 kW/m2
Q.13

Radiation heat losses from satisfactorily insulated high pressure boilar may be about __________ percent.

  • 1
  • 7
  • 18
  • 26
Q.14

Which of the following is the most widely used heat insulating material for pipelines carrying steam ?

  • Tar dolomite bricks followed by asbestos.
  • Fireclay refractory followed by aluminium sheet.
  • Cotton followed by aluminium foil.
  • 85% magnesia cement and glass wool.
Q.15

'Duhring's plot' is of use in

  • extractive distillation
  • evaporation
  • leaching
  • absorption
Q.16

The left face of a one dimensional slab of thickness 0.2 m is maintained at 80°C and the right face is exposed to air at 30°C. The thermal conductivity of the slab is 1.2 W/m.K and the heat transfer co-efficient from the right face isW/m2.K. At steady state, the temperature of the right face in °C is

  • 77.2
  • 71.2
  • 63.8
  • 48.7
Q.17

Heat exchangers operating, when the asymptotic range is reached,

  • provide very large heat transfer co-efficient.
  • results in making part of the heating surface inactive.
  • results in abruptly increased velocity.
  • none of these.
Q.18

In natural convection heat transfer, the correlating parameter is the

  • Graetz number
  • Eckert number
  • Grashoff number
  • Bond number
Q.19

Heat transfer co-efficient equation for forced convection, Nu = 0.Re0.8 . Prn, is not valid, if the value of

  • n = 0.4 is used for heating.
  • n = 0.3 is used for cooling.
  • Reynolds number for the flow involved is > 10000.
  • Reynolds number for the flow involved is < 2100.
Q.20

Reason for operating an evaporator in multiple effect is to secure

  • increased steam economy.
  • decreased steam consumption.
  • both (a) and (b).
  • increased capacity.
Q.21

Which has the lowest Prandtl number ?

  • Liquid metal
  • Aqueous solution
  • Water
  • Lube oil
Q.22

Multiple effect evaporation accounts for

  • steam economy
  • lower operating costs
  • investment economy
  • none of these
Q.23

In case of a supercooled solution, which is on the verge of crystallisation, the free energy of the solution as compared to that of the solid is

  • more
  • less
  • same
  • more or less; depends on the nature of solution
Q.24

Grashhoff number is given by

  • gD3.β.Δtρ22
  • gD2βΔtρ/μ2
  • gD2βΔtP2μ
  • gD3βΔtP2
Q.25

Evaporation by thermocompression results in the

  • saving of steam.
  • realisation of multiple effect economy in a single effect.
  • both (a) and (b).
  • none of these.
Q.26

In a shell and tube heat exchanger, the shell side fluid velocity can not be changed by changing the

  • tube layout
  • tube diameter
  • tube pitch
  • no. of baffles
Q.27

In case of a shell and tube heat exchanger, the minimum and maximum baffle spacing is respectively (where, D = inside diameter of the shell)

  • D/5 and D
  • D/2 and 2 D
  • D/4 and 2 D
  • D and 2 D
Q.28

Boiling of milk in an open vessel is an example of __________ boiling.

  • film
  • sub-cooled
  • saturated nucleate
  • none of these
Q.29

Which is the best tube arrangement (in a shell and tube heat exchanger) if the fluids are clean and non-fouling ?

  • Square pitch
  • Triangular pitch
  • Diagonal square pitch
  • None of these
Q.30

Evaporation by thermocompression results in the

  • saving of steam.
  • realisation of multiple effect economy in a single effect.
  • both (a) and (b).
  • none of these.
Q.31

In a cooling tower, water becomes cool by

  • loosing sensible heat.
  • heat transfer to surroundings.
  • vaporisation due to heat loss to air.
  • loosing latent heat.
Q.32

Pick out the wrong statement.

  • The value of hydrostatic head increases with increase in vacuum in the effect in a multiple effect evaporator system.
  • Entering velocity of the liquid in the tubes of natural circulation evaporators is in the range of 0.3 to 0.9 metre/second.
  • Duhring's plot is used for calculating the concentration of solution.
  • In a multiple effect evaporation system, the number of effects is limited by the total boiling point rise.
Q.33

Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

  • 1
  • 10
  • 20
  • 30
Q.34

The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 =W/m2.K. The fouling factor after one year of operation is found to be hd0 =W/m2.K. The overall heat transfer co-efficient at this time is

  • 1200W/m2.K
  • 894W/m2.K
  • 333W/m2.K
  • 287 W/m2.K
Q.35

Forced circulation evaporators are normally used for concentrating liquids having

  • scaling characteristics
  • high viscosity
  • both(a) & (b)
  • neither (a) nor (b)
Q.36

To reduce the tube side pressure drop for the same flow rate, the heat exchanger recomended is

  • 1-2 heat exchanger
  • 1-1 heat exchanger
  • 3-2 heat exchanger
  • 2-4 heat exchanger
Q.37

In case of heat transfer by conduction in a hollow cylinder, __________ mean area is used to calculate the heat transfer rate.

  • geometric
  • arithmetic
  • logarithmic
  • either (a), (b) or (c)
Q.38

Pick out the wrong statement.

  • In process heat exchangers, saturated steam is preferred over the superheated steam.
  • The maximum is the emissive power of a surface at a temperature T1 occurs at a wavelength of λ1. If the surface temperature is halved, the maximum in the emissive power would occur at a wavelength of 0.5 λ1.
  • When a vertical plate is heated in infinite air environmental under natural convection conditions, the velocity profile in air, normal to the plate, exhibits a maximum.
  • A body at 925 K emits an energy of 1.42 x 1011σW/m2 (σ is the Stefan-Boltzman constant) in the wavelength band between 3 μm to 4 μm. The fraction of this energy in the total energy emitted over the entire wavelength range is equal to emissivity.
Q.39

In case of a multipass shell and tube heat exchanger, the temperature drop in the fluid

  • is inversely proportional to the resistance across which the drop occurs.
  • and the wall are proportional to individual resistances.
  • and the wall is not related.
  • none of these.
Q.40

In Fourier's law, the proportionality constant is called the

  • heat transfer co-efficient
  • thermal diffusivity
  • thermal conductivity
  • Stefan-Boltzman constant
Q.41

Prandtl number for most of dry gases is about

  • 0.001
  • 0.72
  • 70
  • 150
Q.42

In a laboratory test run, the rate of drying was found to be 0.5 x 10-3 kg/m2.s, when the moisture content reduced from 0.4 to 0.1 on dry basis. The critical moisture content of the material is 0.on a dry basis. A tray dryer is used to drykg (dry basis) of the same material under identical conditions. The surface area of the material is 0.m2/kg of dry solid. The time required (in seconds) to reduce the moisture content of the solids from 0.3 to 0.2 (dry basis) is

  • 2000
  • 4000
  • 5000
  • 6000
Q.43

Steam economy in case of a triple effect evaporator will be

  • 1
  • < 1
  • > 1
  • between 0 and 1
Q.44

The heat transfer co-efficient in film type condensation is __________ that for dropwise condensation.

  • greater than
  • lower than
  • is same as
  • half
Q.45

Prandtl number is the reciprocal of

  • Thermal diffusivity/Momentum diffusivity
  • thermal diffusivity x Momentum
  • Thermal diffusivity x Mass diffusivity
  • Mass diffusivity x Momentum diffusivity
Q.46

Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

  • 1
  • 10
  • 20
  • 30
Q.47

Pick out the wrong statement.

  • Bubble size increases with the dynamic viscosity of the liquid in case of nucleate pool boiling.
  • Thermal conductivity of a dry material is more than that of the damp material.
  • Ratio of its capacity to economy equals the steam consumption in kg/hr in an evaporator.
  • Vaporisation of organic substances in evaporator mostly causes foam formation.
Q.48

In a laboratory test run, the rate of drying was found to be 0.5 x 10-3 kg/m2.s, when the moisture content reduced from 0.4 to 0.1 on dry basis. The critical moisture content of the material is 0.on a dry basis. A tray dryer is used to drykg (dry basis) of the same material under identical conditions. The surface area of the material is 0.m2/kg of dry solid. The time required (in seconds) to reduce the moisture content of the solids from 0.3 to 0.2 (dry basis) is

  • 2000
  • 4000
  • 5000
  • 6000
Q.49

In a heat exchanger, the rate of heat transfer from the hot fluid to the cold fluid

  • varies directly as the area and the LMTD.
  • directly proportional to LMTD and inversely proportional to the area.
  • varies as square of the area.
  • none of these.
Q.50

Intermittant tube cleaning is possible to be done in case of a __________ evaporator.

  • basket type
  • horizontal tube
  • calendria
  • none of these
0 h : 0 m : 1 s