Heat & Mass Transfer Week 05 Instructor: Mr....

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Heat & Mass Transfer

Week_05

Instructor: Mr. Adnan Qamar

Mechanical Engineering Department

1

One Dimensional Steady State Heat Conduction

Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

Let us consider a cylinder and a slab both made of the same material of uniform

thermal conductivity (k)

2

Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

3

Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

4

Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

5

One Dimensional Steady State Heat Conduction

Logarithmic Mean Area for the Hollow Sphere and Plane Wall

6

Logarithmic Mean Area for the Hollow Sphere and Plane Wall

7

One Dimensional Steady State Heat Conduction

Variable Thermal Conductivity

➢ Effects of Various Parameters on the Thermal Conductivity of Solids

8

Effects of Various Parameters on the Thermal Conductivity of Solids

9

One Dimensional Steady State Heat Conduction

Plane Wall (Slab) with variable Thermal Conductivity (kT)

10

Plane Wall (Slab) with variable Thermal Conductivity (kT)

11

Plane Wall (Slab) with variable Thermal Conductivity (kT)

12

Plane Wall (Slab) with variable Thermal Conductivity (kT)

13

Plane Wall (Slab) with variable Thermal Conductivity (kT)

14

One Dimensional Steady State Heat Conduction

Hollow Cylinder with variable Thermal Conductivity (kT)

15

Hollow Cylinder with variable Thermal Conductivity (kT)

v

16

Hollow Cylinder with variable Thermal Conductivity (kT)

17

One Dimensional Steady State Heat Conduction

Spherical System with variable Thermal Conductivity (kT)

18

Spherical System with variable Thermal Conductivity (kT)

19

Spherical System with variable Thermal Conductivity (kT)

20

Spherical System with variable Thermal Conductivity (kT)

21

One Dimensional Steady State Heat Conduction

Heat Conduction Through A Composite Wall

22

Heat Conduction Through A Composite Wall

23

Heat Conduction Through A Composite Wall

24

Heat Conduction Through A Composite Wall

25

One Dimensional Steady State Heat Conduction

Thermal Contact Resistance

26

Thermal Contact Resistance

27

One Dimensional Steady State Heat Conduction

Overall Heat Transfer Coefficient (U)

28

Overall Heat Transfer Coefficient (U)

29

Overall Heat Transfer Coefficient (U)

30

Overall Heat Transfer Coefficient (U)

Then compare equation (15) & (16);

31

One Dimensional Steady State Heat Conduction

Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

32

Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

33

Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

34

Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

35

Overall Heat Transfer Through a Plane Wall

Consider a plane wall with thickness “dx” as shown in Fig;

Fig: Overall heat transfer through a plane wall

36

Overall Heat Transfer Through a Plane Wall

Convection Heat Transfer 1:

Conduction Heat Transfer:

Convection Heat Transfer 2:

Cross multiplying and adding equations 1,2 &3 we will have;

37

)1(1

)( 11

1

11111

conv

convR

TT

Ah

TTTTAhQ

)2()( 312121

cond

condR

TT

kA

dx

TT

dx

TTkAQ

)3(1

)( 22

2

22222

conv

convR

TT

Ah

TTTTAhQ

21 convcondconv QQQQ

Overall Heat Transfer Through a Plane Wall

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combined

effect of conduction and convection.

38

)4()(11 21

21

21

21

TTUA

R

TT

AhkA

dx

Ah

TTQ

222111

21

11 TTTTTT

AhQ

KA

dxQ

AhQ

21

21

)11

( TTAhKA

dx

AhQ

Overall Heat Transfer Through a Composite Wall

Consider a composite wall with thickness “dx1 & dx2” as shown in Fig;

Fig: Overall heat transfer through a composite wall

39

Overall Heat Transfer Through a Composite Wall

Convection Heat Transfer 1:

Conduction Heat Transfer 1:

Conduction Heat Transfer 2:

40

)1(1

)( 11

1

11111

conv

convR

TT

Ah

TTTTAhQ

)2()(

1

21

1

1

21

1

2111

cond

condR

TT

Ak

dx

TT

dx

TTAkQ

)3()(

2

32

2

2

32

2

3222

cond

condR

TT

Ak

dx

TT

dx

TTAkQ

Overall Heat Transfer Through a Composite Wall

Convection Heat Transfer 2:

Cross multiplying and adding equations 1,2, 3& 4, we will have;

41

)4(1

)(2

23

2

232322

conv

convR

TT

Ah

TTTTAhQ

2211 convcondcondconv QQQQQ

23322111

22

2

1

1

1

1...

1. TTTTTTTT

AhQ

AK

dxQ

AK

dxQ

AhQ

21

22

2

1

1

1

)11

( TTAhAk

dx

Ak

dx

AhQ

Overall Heat Transfer Through a Composite Wall

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combined

effect of conduction and convection.

42

)5(11

21

22

2

1

1

1

21

R

TT

AhAk

dx

Ak

dx

Ah

TTQ

)6()( 21 TTUAQ

Overall Heat Transfer Through a Hollow Cylinder

Consider a hollow cylinder with length “L” as shown in Fig;

Fig: Overall heat transfer through a hollow cylinder

43

Overall Heat Transfer Through a Hollow Cylinder

Convection Heat Transfer 1:

Conduction Heat Transfer:

Convection Heat Transfer 2:

44

)1(1

)(1

11

11

1111111

conv

convR

TT

Ah

TTTTAhQ

)2(

ln.2

1)( 21

1

2

1221

cond

condR

TT

r

r

KL

TTTTkAQ

)3(1

)(2

22

22

2222222

conv

convR

TT

Ah

TTTTAhQ

Overall Heat Transfer Through a Hollow Cylinder

Cross multiplying and adding equations 1,2 & 3, we will have;

45

QQQQ convcondconv 21

222111

221

2

11

1.ln.

2

1.

1.

TTTTTT

AhQ

r

r

KLQ

AhQ

21

221

2

11

1ln.

2

11.

TT

Ahr

r

kLAhQ

)4(1

ln.2

1121

221

2

11

21

R

TT

Ahr

r

KLAh

TTQ

)5()( 21 TTUAQ

Overall Heat Transfer Through a Hollow Cylinder

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combined

effect of conduction and convection.

Note: If heat is moving inside the fluid, then take area A1 and if the heat is

moving outside the fluid then take A2.

46

Overall Heat Transfer Through a Composite Hollow Cylinder

Consider a composite hollow cylinder with length “L” as shown in Fig;

Fig: Overall heat transfer through a composite hollow cylinder

47

Overall Heat Transfer Through a Composite Hollow Cylinder

Convection Heat Transfer 1:

Conduction Heat Transfer 1:

Conduction Heat Transfer 2:

48

)1(1

)(1

11

11

1111111

conv

convR

TT

Ah

TTTTAhQ

)2(

ln2

1)(

1

21

1

2

1

212111

cond

condR

TT

r

r

Lk

TTTTAkQ

)3(

ln2

1)(

2

32

2

3

2

323222

cond

condR

TT

r

r

Lk

TTTTAkQ

Overall Heat Transfer Through a Composite Hollow Cylinder

Convection Heat Transfer 2:

Cross multiplying and adding equations 1,2,3 & 4, we will have;

49

)4(1

)(2

23

32

2323322

conv

convR

TT

Ah

TTTTAhQ

QQQQQ convcondcondconv 2211

23322111

222

3

21

2

111

1.ln.

2

1.ln.

2

1.

1.

TTTTTTTT

AhQ

r

r

LkQ

r

r

LkQ

AhQ

Overall Heat Transfer Through a Composite Hollow Cylinder

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combinedeffect of conduction and convection.

Note: If heat is moving inside the fluid, then take area A1 and if the heat ismoving outside the fluid then take A3.

50

21

322

3

21

2

111

1ln

2

1ln

2

11

TT

Ahr

r

LKr

r

LKAhQ

)5(

2

1ln

2

1ln

2

1

2.

1

322

3

21

2

111

21

Lrhr

r

LKr

r

LKLrh

TTQ

)6()( 21 TTUAQ

Overall Heat Transfer Through a Hollow Sphere

Consider a composite hollow sphere with radius “r1 & r2” as shown in Fig;

Fig: Overall heat transfer through a hollow sphere

51

Overall Heat Transfer Through a Hollow Sphere

Convection Heat Transfer 1:

Conduction Heat Transfer:

Convection Heat Transfer 2:

52

)1(1

)(1

11

11

1111111

conv

convR

TT

Ah

TTTTAhQ

)2(

]11

[4

1)( 21

21

2121

conv

condR

TT

rrk

TTTTkAQ

)3(1

)( 22

22

2222222

conv

convR

TT

Ah

TTTTAhQ

Overall Heat Transfer Through a Hollow Sphere

Cross multiplying and adding equations 1,2 & 3, we will have;

53

)4(1

)11

(4

1121

222111

21

R

TT

AhrrkAh

TTQ

222111

222111

1)

11(

4

11

TTTTTT

AhQ

rrkQ

AhQ

21

222111

1)

11(

4

11

TT

AhrrkAhQ

)5()( 21 TTUAQ

Overall Heat Transfer Through a Hollow Sphere

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combined

effect of conduction and convection.

Note: If heat is moving inside the fluid, then take area A1 and if the heat is

moving outside the fluid then take A3.

54

Overall Heat Transfer Through a Composite Hollow Sphere

Consider a composite hollow sphere with radius “r1 & r2” as shown in Fig;

Fig: Overall heat transfer through a composite hollow sphere

55

Overall Heat Transfer Through a Hollow Sphere

Convection Heat Transfer 1:

Conduction Heat Transfer 1:

Conduction Heat Transfer 2:

56

)1(1

)(1

11

11

1111111

conv

convR

TT

Ah

TTTTAhQ

)2(

]11

[4

1)( 21

211

21211

conv

condR

TT

rrk

TTTTAkQ

)3(

]11

[4

1)(

2

2

32

322

32322

cond

condR

TT

rrk

TTTTAkQ

Overall Heat Transfer Through a Composite Hollow Sphere

Convection Heat Transfer 2:

Cross multiplying and adding equations 1,2,3 & 4, we will have;

57

)4(1

)( 23

32

2323322

conv

convR

TT

Ah

TTTTAhQ

QQQQQ convcondcondconv 2211

23322111

3232221111

1.

11

4

1.

11

4

1.

1.

TTTTTTTT

AhQ

rrkQ

rrkQ

AhQ

21

3232221111

1]

11[

4

1]

11[

4

11

TT

AhrrkrrkAhQ

Overall Heat Transfer Through a Composite Hollow Sphere

Where ΣR=1/UA, and U= overall heat transfer coefficient. It is the combined

effect of conduction and convection.

Note: If heat is moving inside the fluid, then take area A1 and if the heat is

moving outside the fluid then take A3.

58

)5(1

)11

(4

1)

11(

4

1121

2232221111

21

R

TT

AhrrKrrKAh

TTQ

)6()( 21 TTUAQ

One Dimensional Steady State Heat Conduction

Critical Radius of Insulation

59

Critical Radius of Insulation

60

Critical Radius of Insulation

61

Critical Radius of Insulation

62

Critical Radius of Insulation

63

Critical Radius of Insulation

64

Critical Radius of Insulation

65

One Dimensional Steady State Heat Conduction

Critical Radius of Insulation For Cylinder

66

Conduction Heat Transfer-Class Problems

Example 5.1:

67

Conduction Heat Transfer-Class Problems

68

Conduction Heat Transfer-Class Problems

Under Steady state, heat flux is constant throughout the wall and each layer

69

Conduction Heat Transfer-Class Problems

70

Conduction Heat Transfer-Class Problems

71

Conduction Heat Transfer-Class Problems

Example 5.2:

72

Conduction Heat Transfer-Class Problems

73

Conduction Heat Transfer-Class Problems

74

Conduction Heat Transfer-Class Problems

75

Conduction Heat Transfer-Class Problems

Example 5.3:

76

Conduction Heat Transfer-Class Problems

77

Conduction Heat Transfer-Class Problems

78

Conduction Heat Transfer-Class Problems

79

Conduction Heat Transfer-Class Problems

80

Conduction Heat Transfer-Class Problems

Example 5.4:

81

Conduction Heat Transfer-Class Problems

82

Conduction Heat Transfer-Class Problems

83

Conduction Heat Transfer-Class Problems

84

Conduction Heat Transfer-Class Problems

Example 5.5:

85

Conduction Heat Transfer-Class Problems

86

Conduction Heat Transfer-Class Problems

87

Conduction Heat Transfer-Class Problems

88

Conduction Heat Transfer-Class Problems

89

Conduction Heat Transfer-Class Problems

Example 5.6:

90

Conduction Heat Transfer-Class Problems

91

Conduction Heat Transfer-Class Problems

92

Conduction Heat Transfer-Class Problems

93

Conduction Heat Transfer-Class Problems

94

Conduction Heat Transfer-Class Problems

95

Conduction Heat Transfer-Class Problems

96

Conduction Heat Transfer-Class Problems

Example 5.7:

97

Conduction Heat Transfer-Class Problems

98

Conduction Heat Transfer-Class Problems

99

Conduction Heat Transfer-Class Problems

100

Conduction Heat Transfer-Class Problems

Example 5.8:

101

Conduction Heat Transfer-Class Problems

102

Conduction Heat Transfer-Class Problems

103

Conduction Heat Transfer-Class Problems

104