Q.1

The type of liquor circulation system to be ' employed in evaporators (viz. natural or forced circulation) is determined mainly by the __________ of the liquid.

  • viscosity
  • density
  • thermal conductivity
  • corrosive nature
Q.2

The rate of heat transfer from a vertical plate by natural convection depends upon the temperature differences (ΔT) between wall and outside bulk. The proportionality is given as

  • (ΔT)1/4
  • ΔT1/2
  • (ΔT)5/4
  • (ΔT)3/4
Q.3

With increase in temperature, the total emissivity of conductors

  • increases
  • decreases
  • remains same
  • decreases linearly
Q.4

In a forward feed multiple effect evaporator unit

  • viscosity of liquid is highest in first effect.
  • transfer from effect to effect is done by pumps.
  • no pump is required to withdraw the product from the last effect.
  • none of these.
Q.5

If air (a non-condensing gas) is present in a condensing vapor stream, it will __________ the condensation rate of vapor.

  • increase
  • decrease
  • not affect
  • increase the condensing film co-efficient as well as
Q.6

Loss of heat from untagged steam pipe to the ambient air is by

  • conduction
  • convection
  • radiation
  • all (a), (b) & (c)
Q.7

View factor is important in heat transfer by

  • steady state conduction
  • natural convection
  • forced convection
  • radiation
Q.8

Arithmetic mean area can be used in heat transfer problem to calculate the heat flow by conduction through a cylinder which is

  • thin walled having the value of Ao Ai/< 2.
  • thick walled.
  • having the value of Ao/Ai > 2.
  • both (b) and (c).
Q.9

In case of heat flow by conduction for a cylindrical body with an internal heat source, the nature of temperature distribution is

  • linear
  • hyperbolic
  • parabolic
  • none of these
Q.10

In SI units, fouling factor is expressed in

  • m2°K/W
  • W/m2°K
  • m2°K
  • m°K/W
Q.11

Film boiling is usually not desired in commercial equipments, because

  • the heat transfer rate is low in view of the large temperature drop.
  • it is difficult to maintain.
  • it is not economic.
  • none of these.
Q.12

A sphere of radius 'R1' is enclosed in a sphere of radius 'R2'. The view (or shape) factor for radiative heat transfer of the outer sphere with respect to the inner sphere is

  • 0
  • R2/(R1+R2)
  • 1
  • (R1/R2)2
Q.13

Thermal diffusivity is the most important in heat transfer by

  • conduction
  • radiation
  • condensation
  • natural convection
Q.14

Overall heat transfer co-efficient of a particular tube is U1. If the same tube with some dirt deposited on either side has coefficient U2, then

  • U1 = U2
  • U2 > U1
  • U1 > U2
  • U1 = dirt factor - U2
Q.15

The characteristic dimensionless groups for heat transfer to a fluid flowing through a pipe in laminar flow are

  • Re.Gz
  • Nu, Pr
  • Nu, Pr, Re
  • Nu, Gz
Q.16

Prandtl and Reynold's analogies are identical for Prandtl number value of

  • 0
  • 0.5
  • 1
  • 5
Q.17

Fruit juice (a heat sensitive material) can be concentrated in a __________ evaporator.

  • long tube
  • falling film
  • high pressure
  • none of these
Q.18

Tubes are held between top and bottom tube sheets in Calenderia type evaporator by keeping

  • both the tube sheets fixed.
  • both the tube sheets floating.
  • the top tube sheet floating and bottom tube sheet fixed.
  • the top tube sheet fixed and the bottom tube-sheet floating.
Q.19

The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is

  • lower tube side pressure drop.
  • lower shell side pressure drop.
  • higher tube side heat transfer co-efficient.
  • higher shell side heat transfer co-efficient.
Q.20

Three solid objects of the same material and of equal mass-a sphere, a cylinder (length = diameter) and a cube are at 500°C initially. These are dropped in a quenching bath containing a large volume of cooling oil each attaining the bath temperature eventually. The time required forchange in temperature is the smallest for

  • cube
  • cylinder
  • sphere
  • equal for all the three
Q.21

For heat flow through very thick walled cylinder, use____mean radius.

  • arithmetic
  • logarithmic
  • geometric
  • either (a) or (c)
Q.22

An ejector is used to

  • increase pressure
  • increase temperature
  • remove condensate
  • none of these
Q.23

For the same heat transfer area and the terminal conditions, the ratio of the capacities of a single effect evaporator to a triple effect evaporator is

  • 3
  • 0.33
  • 1
  • 1.33
Q.24

For a laminar flow of fluid in a circular tube, 'h1' is the convective heat transfer co-efficient at velocity 'V1'. If the velocity is reduced by half and assuming the fluid properties are constant, the new convective heat transfer co-efficient is

  • 1.26 h1
  • 0.794 h1
  • 0.574 h1
  • 1.741 h1
Q.25

(NGr x NPr) is called the __________ number.

  • Graetz
  • Reyleigh
  • Nusselt
  • Stanton
Q.26

In SI units, thermal conductivity is expressed in

  • Watt/m.°K
  • Watt/m2. °K
  • Watt/m2. °K
  • Watt/m4. °K
Q.27

The critical radius 'r' of insulation on a pipe is given by

  • r = 2k/h
  • r = k/h
  • r = k/2h
  • r = h/k
Q.28

Heat transfer rate described by Fourier's law will decrease, if the __________ increases.

  • thermal conductivity
  • thickness
  • temperature difference
  • heat transfer area
Q.29

Nusselt number is the ratio of the

  • temperature gradient of the wall to that across the entire pipe.
  • temperature difference to the temperature gradient at the wall.
  • heat flux at the wall to that across the entire pipe.
  • none of these
Q.30

The outlet temperature of cooling water in a heat exchanger is generally not allowed to exceed above 50°C in industrial practice mainly to avoid

  • its evaporation loss
  • excessive corrosion
  • uneconomic LMTD
  • decrease in heat exchanger efficiency
Q.31

Tube expansion allowances exist in __________ heat exchanger.

  • multipass fixed tube sheet
  • U-tube
  • single pass fixed tube sheet
  • none of these
Q.32

For a multipass shell and tube heat exchanger, the LMTD correction factor is always

  • 1
  • > 1
  • < 1
  • between 1 & 2
Q.33

Overall heat transfer co-efficient for cooling of hydrocarbons by water is about

  • 50 -100 Kcal/hr.m2.°C
  • 50 -100 W/m2 . °K
  • 50 -100 BTU/hr. ft.2°F
  • 1000 - 1500 BTU/hr. ft.2°F
Q.34

The ratio of velocity head to tube side return loss in case of a multipass shell and tube heat exchanger is

  • 2
  • 1/2
  • 4
  • 1/4
Q.35

Water is normally used as a coolant in the heat exchange equipments mainly because ofits

  • abundance & high heat capacity
  • low density
  • low viscosity
  • high fluidity
Q.36

Indirect contact heat exchangers are preferred over direct contact heat exchangers, because

  • heat transfer co-efficient are high.
  • there is no risk of contamination.
  • there is no mist formation.
  • cost of equipment is lower.
Q.37

The Grashoff number is defined as the ratio of the

  • buoyancy to inertial forces.
  • buoyancy to viscous forces.
  • inertial to viscous forces.
  • buoyancy to surface tension forces.
Q.38

Absorptivity of a perfect black body is unity. Which of the following has maximum absorptivity ?

  • aluminium foil
  • refractory bricks
  • iron plate
  • coke breeze
Q.39

Which of the following is the most controlling factor for the rate of bubble detachment from the hot solid surface ?

  • Liquid density
  • Liquid viscosity
  • Hot surface temperature
  • Interfacial tension
Q.40

Extremely large or small volumes of fluids are generally best routed through the shell side of a shell and tube heat exchanger, because of the

  • less corrosion problems.
  • flexibility possible in the baffle arrangement.
  • low pressure drop.
  • high heat transfer co-efficient.
Q.41

In which mode of heat transfer, the Biot number is important ?

  • Transient heat conduction
  • Natural convection
  • Forced convection
  • Radiation
Q.42

The variation of thermal conductivity of a metal with temperature is often correlated using an expression of the form K = K0 + at. where, K is the thermal conductivity and T is the temperature (in °K). The units of 'a' in SI system will be

  • W/m.k
  • W/m
  • W/m.k2
  • none, 'a' is just a number
Q.43

The main purpose of providing fins on heat transfer surface is to increase the

  • temperature gradient.
  • mechanical strength of the equipment.
  • heat transfer area.
  • heat transfer co-efficient.
Q.44

A dephlegmator is a

  • total condenser
  • vacuum evaporator
  • partial condenser
  • double pipe heat exchanger
Q.45

Boiling point of a solution according to Duhring's rule is a linear function of the __________ of water.

  • boiling point (at the same pressure)
  • viscosity
  • density
  • thermal conductivity
Q.46

As per Kirchoffs law, the ratio of the total radiating power to the absorptivity of a body depends on the

  • temperature of the body only.
  • wavelength of monochromatic radiation.
  • both (a) and (b).
  • nature of material of body.
Q.47

A black body does not __________ radiation.

  • absorb or emit
  • refract
  • reflect
  • both(b) & (c)
Q.48

Prandtl number is the ratio of

  • momentum diffusivity to mass diffusivity.
  • momentum diffusivity to thermal diffusivity.
  • thermal diffusivity to mass diffusivity.
  • thermal diffusivity to momentum diffusivity.
Q.49

Which of the following parameters is increased by use of finned tube in a multipass shell and tube heat exchanger ?

  • Tube side pressure drop and the heat transfer rate.
  • Convective heat transfer co-efficient.
  • Effective tube surface area for convective heat transfer.
  • All (a) (b) and (c).
Q.50

In evaporators, lowering the feed temperature

  • increases the heating area required.
  • reduces the economy.
  • both (a) and (b).
  • decreases the heating area required.
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