Heat Transfer 2 Flashcards

1
Q

In natural convection heat transfer, the correlating parameter is the

A

Grashoff number

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
2
Q

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

A

film

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
3
Q

Pick out the wrong statement.

A

The maximum is the emissive power of a surface at a temperature T1 occurs at a wavelength of ?1. If the surface temperature is halved, the maximum in the emissive power would occur at a wavelength of 0.5 ?1.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
4
Q

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

A

natural convection

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
5
Q

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

A

material is anisotropic.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
6
Q

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 is 10 W/m2.K. At steady state, the temperature of the right face in �C is

A

48.7

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
7
Q

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

A

tube diameter

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
8
Q

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

A

1-1 heat exchanger

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
9
Q

Heat transfer co-efficient (h) for a fluid flowing inside a clean pipe is given by
This is valid for the value of NRe equal to

A

> 10000

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
10
Q

Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m2�C.

A

5000-15000

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
11
Q

Correction is applied to LMTD for __________ flow.

A

cross

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
12
Q

If h1 = inner film co-efficient and /h2 = outer film co-efficient, then the overall heat transfer co-efficient is

A

always between h1 and h2

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
13
Q

One kilogram of water at 0�C is changed to superheated steam of one atm pressure and 300� C. The major heat consumption in the process will be to

A

evaporate the water.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
14
Q

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

A

high

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
15
Q

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

A

16.5 kW/m2

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
16
Q

Heat exchangers operating, when the asymptotic range is reached,

A

results in making part of the heating surface inactive.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
17
Q

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

A

D/5 and D

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
18
Q

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

A

logarithmic

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
19
Q

In a gas-liquid shell and tube heat exchanger, the

A

all ‘a’, ‘b’ & ‘c’

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
20
Q

Which is the most suitable for the concentration of foamy & frothy liquors?

A

Long tube vertical evaporator

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
21
Q

Boiling point elevation of an ideal solution

A

increases rapidly with temperature rise.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
22
Q

The rate of heat transfer is a product of overall heat transfer co-efficient, the difference in temperature and the

A

heat transfer area

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
23
Q

Which of the following has the lowest overall heat transfer co-efficient?

A

Air

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
24
Q

Which of the following has the minimum absorptivity?

A

Aluminum foil

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
25
Q

A black body when hot, emits heat radiation of __________ wavelengths.

A

all

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
26
Q

A composite wall consists of two plates A and B placed in series normal to the flow of heat. The thermal conductivities are kA and kB and the specific heat capacities are CPA and CPB for plates A and B respectively. Plate B has twice the thickness of plate A. At steady state, the temperature difference across plate A is greater than that across plate B, when

A

kA < 0.5kB

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
27
Q

Vibrations in the tubes of a shell and tube heat exchanger is induced due to the

A

all (a), (b) and (c)

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
28
Q

Heat transfer by conduction in the turbulent core of a fluid flowing through a heated pipe is negligible, if the value of Prandtl number is

A

0.6

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
29
Q

The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is

A

3.66

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
30
Q

Sensible heat of hot industrial flue gases can not be recovered by a/an

A

none of these

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
31
Q

The critical radius of insulation for a spherical shell is (where, K = thermal conductivity of insulating material h0 = heat transfer coefficient at the outer surface)

A

2K/h0

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
32
Q

Radiator of an automobile engine is a __________ type of heat exchanger.

A

direct contact

33
Q

In pipe flow, heat is transferred from hot wall to the liquid by

A

forced convection and conduction

34
Q

The value of Stefan-Boltazman constant in SI unit is

A

5.6697 x 10-8W/m2.�K4

35
Q

The unit of heat transfer co-efficient is

A

BTU/hr. ft2�F

36
Q

For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus-Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of

37
Q

The inner wall of a furnace is at a temperature of 700�C. The composite wall is made of two substances, 10 and 20 cm thick with thermal conductivities of 0.05 and 0.1 W.m-1.�C-1 respectively. The ambient air is at 30�C and the heat transfer co-efficient between the outer surface of wall and air is 20 W.m-2.�C-1. The rate of heat loss from the outer surface in W.m-2is

38
Q

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

39
Q

Low thermal conductivity of heat insulating materials is due to its

A

high proportion of air space

40
Q

The most conducive surface for dropwise condensation to occur is the __________ surface.

41
Q

In an interphase heat transfer process, the equilibrium state corresponds to equality of temperature in the two phases, while the condition for equilibrium in an interphase mass transfer process is equality of

A

concentrations

42
Q

Calburn analogy is applicable for the value of Prandtl number from

A

0.6 to 120

43
Q

Pick out the correct equation.

A

jH = (St)(Pr)^2/3 = f/2

44
Q

Multiple effect evaporators ar used to

A

increase the steam economy & the capacity.

45
Q

Prandtl number is given by

A

(Cp � ?)/k

46
Q

Small scale evaporation is done in a

A

steam jacketed kettle

47
Q

Heat exchanger tubes are never made of

48
Q

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

49
Q

Reason for operating an evaporator in multiple effect is to secure

A

both (a) and (b).

50
Q

In a cooling tower, water becomes cool by

A

loosing sensible heat.

51
Q

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

A

thermal conductivity

52
Q

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

A

lower than

53
Q

Pick out the wrong statement.

A

Thermal conductivity of a dry material is more than that of the damp material.

54
Q

Duhring’s plot’ is of use in

A

evaporation

55
Q

Which has the lowest Prandtl number?

A

Liquid metal

56
Q

Pick out the wrong statement.

A

Duhring’s plot is used for calculating the concentration of solution.

57
Q

Prandtl number for most of dry gases is about

58
Q

Prandtl number is the reciprocal of

A

Thermal diffusivity/Momentum diffusivity

59
Q

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

A

more than 45�C

60
Q

For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is

A

Nu = 2/pi x Gz

61
Q

Multiple effect evaporation accounts for

A

steam economy

62
Q

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

63
Q

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

64
Q

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

A

volume to surface area

65
Q

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

A

85% magnesia cement and glass wool.

66
Q

Heat transfer co-efficient equation for forced convection, Nu = 0.023 Re^0.8 . Pr^n, is not valid, if the value of

A

Reynolds number for the flow involved is < 2100.

67
Q

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

A

Triangular pitch

68
Q

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

A

and the wall are proportional to individual resistances.

69
Q

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

A

account for the uneven expansion of shell and tube bundles.

70
Q

A graph between __________ is called Wilson plot.

A

1/U Vs. 1/V^0.8

71
Q

Grashhoff number is given by

A

gD^3.?.?t?2/?^2

72
Q

The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is

73
Q

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 0.08 on a dry basis. A tray dryer is used to dry 100 kg (dry basis) of the same material under identical conditions. The surface area of the material is 0.04 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

74
Q

Pick out the wrong statement.

A

Heat transfer co-efficient during nucleate boiling is not influenced by the agitation imparted.

75
Q

What is the geometric mean of two heat transfer areas A1 and A2?

A

sqrt*(A1 . A2)

76
Q

Evaporation by thermocompression results in the

A

both (a) and (b).

77
Q

Forced circulation evaporators are normally used for concentrating liquids having

A

both(a) & (b)

78
Q

Steam economy in case of a triple effect evaporator will be