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

104
Heat & Mass Transfer Week_05 Instructor: Mr. Adnan Qamar Mechanical Engineering Department 1

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

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Heat & Mass Transfer

Week_05

Instructor: Mr. Adnan Qamar

Mechanical Engineering Department

1

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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)

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Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

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Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

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Logarithmic Mean Area for the Hollow Cylinder and Plane Wall

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One Dimensional Steady State Heat Conduction

Logarithmic Mean Area for the Hollow Sphere and Plane Wall

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Logarithmic Mean Area for the Hollow Sphere and Plane Wall

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One Dimensional Steady State Heat Conduction

Variable Thermal Conductivity

➢ Effects of Various Parameters on the Thermal Conductivity of Solids

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Effects of Various Parameters on the Thermal Conductivity of Solids

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One Dimensional Steady State Heat Conduction

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

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

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

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

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

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One Dimensional Steady State Heat Conduction

Hollow Cylinder with variable Thermal Conductivity (kT)

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Hollow Cylinder with variable Thermal Conductivity (kT)

v

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Hollow Cylinder with variable Thermal Conductivity (kT)

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One Dimensional Steady State Heat Conduction

Spherical System with variable Thermal Conductivity (kT)

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Spherical System with variable Thermal Conductivity (kT)

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Spherical System with variable Thermal Conductivity (kT)

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Spherical System with variable Thermal Conductivity (kT)

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One Dimensional Steady State Heat Conduction

Heat Conduction Through A Composite Wall

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Heat Conduction Through A Composite Wall

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Heat Conduction Through A Composite Wall

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Heat Conduction Through A Composite Wall

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One Dimensional Steady State Heat Conduction

Thermal Contact Resistance

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Thermal Contact Resistance

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One Dimensional Steady State Heat Conduction

Overall Heat Transfer Coefficient (U)

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Overall Heat Transfer Coefficient (U)

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Overall Heat Transfer Coefficient (U)

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Overall Heat Transfer Coefficient (U)

Then compare equation (15) & (16);

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One Dimensional Steady State Heat Conduction

Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

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Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

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Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

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Series and Parallel One Dimensional Heat Transfer Through A Composite Wall

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

Page 57: Heat & Mass Transfer Week 05 Instructor: Mr. …engineersedge.weebly.com/uploads/4/6/8/0/4680709/heat...Convection Heat Transfer 2: Cross multiplying and adding equations 1,2 &3 we

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

Page 58: Heat & Mass Transfer Week 05 Instructor: Mr. …engineersedge.weebly.com/uploads/4/6/8/0/4680709/heat...Convection Heat Transfer 2: Cross multiplying and adding equations 1,2 &3 we

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

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One Dimensional Steady State Heat Conduction

Critical Radius of Insulation

59

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Critical Radius of Insulation

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Critical Radius of Insulation

61

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Critical Radius of Insulation

62

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Critical Radius of Insulation

63

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Critical Radius of Insulation

64

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Critical Radius of Insulation

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One Dimensional Steady State Heat Conduction

Critical Radius of Insulation For Cylinder

66

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Conduction Heat Transfer-Class Problems

Example 5.1:

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Conduction Heat Transfer-Class Problems

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Conduction Heat Transfer-Class Problems

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

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Example 5.2:

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Example 5.3:

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Conduction Heat Transfer-Class Problems

Example 5.4:

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Conduction Heat Transfer-Class Problems

Example 5.5:

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Conduction Heat Transfer-Class Problems

Example 5.6:

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Example 5.7:

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Conduction Heat Transfer-Class Problems

Example 5.8:

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