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부산대학교 현규 유체역학 및 열전달 1 유체역학 및 열전달 Chapter 10. Heat transfer by conduction 부산대학교 화공생명공학부 현규 (Kyu Hyun)

유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

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Page 1: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규유체역학및열전달 1

유체역학및열전달

Chapter 10. Heat transfer by conduction

부산대학교 화공생명공학부현 규 (Kyu Hyun)

Page 2: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat transfer by conduction

유체역학및열전달 2

dydu

AF m=

-Newtonian Fluids

Page 3: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat transfer by conduction

÷øö

çèæ

¶¶

+¶¶

+¶¶

-=Ñ-=¶¶

zTT

rrTkTk

Aq

q1

÷÷ø

öççè

涶

+¶¶

+¶¶

-=Ñ-=¶¶

fqqT

rT

rrTkTk

Aq

sin11

-Cartesian coordinate

-Cylindrical coordinate

-Spherical coordinate

유체역학및열전달 3

TkzT

yT

xTk

dAdq

Ñ-=÷÷ø

öççè

涶

+¶¶

+¶¶

-=

General Expression of Fourier’s law in all three directions

Page 4: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Thermal conductivity

유체역학및열전달 4

Page 5: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Steady state conduction

유체역학및열전달 5

Page 6: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Steady state conduction

유체역학및열전달 6

Page 7: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Thermal resistance (1)

-Compound resistance in series

유체역학및열전달 7

Page 8: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Thermal resistance (2)

유체역학및열전달 8

Page 9: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat flow through a cylinder (1)

유체역학및열전달 9

Page 10: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat flow through a cylinder (2)

유체역학및열전달 10

Page 11: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat conduction through composite walls – Plate (1)

-Newton’s cooling law

-q0 (heat flux) = constant

Page 12: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat conduction through composite walls – Plate (2)

유체역학및열전달 12

Individual heat transfer coefficient

Page 13: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Heat conduction through composite walls - Pipe

-r0q0 (heat flux) = constant

Page 14: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Individual heat-transfer coefficient

Page 15: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Internal Energy balance equation (1)

gτVVV rrr+Ñ-×Ñ-×-Ñ=

¶¶ p

t][)()(

l Momentum balance equation l Internal energy balance equation

VVqV Ñ-×Ñ-×Ñ-×-Ñ=¶

¶ :)(][)ˆ()ˆ( trr pUtU

이부분은우리가배우는범위를넘는내용이지만알아두면유용하기때문에첨부하였습니다

4학년과목인 “이동현상”내용을발췌했습니다.

두가지식을비교해보면공통점이있습니다.1. Momentum (ρV)와 internal

energy (ρÛ)를이용한 balance 식이라는점이다

2. 유동이존재하는상황에서momentum과내부에너지가전달된다.

3. 특히 3가지 (빨, 초, 파)부분은특히나유사한형식의방정식입니다.

유체역학및열전달 15

Page 16: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Internal Energy balance equation (2)

VVqV Ñ-×Ñ-×Ñ-×-Ñ=¶

¶ :)(][)ˆ()ˆ( trr pUtU

VVq Ñ-×Ñ-×-Ñ= :)(ˆ

tr pDtUD

DtDp

DtHD

+Ñ-×-Ñ= Vq :ˆ

tr

)(/ˆˆˆˆ formulaodynamicthermPHVPHU r-=-=

DtDp

TDtDTC p ÷

øö

çè涶

-Ñ-×-Ñ=lnln:ˆ rtr Vq

)'()( neqcontinuityDtD

t00 =×Ñ+=×Ñ+

¶¶ VV rrrr

유체역학및열전달 16

)'()( neqcontinuityDtD

t00 =×Ñ+=×Ñ+

¶¶ VV rrrr

Page 17: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Internal Energy balance equation (3)

DtDp

TDtDTC p ÷

øö

çè涶

-Ñ-×-Ñ=lnln:ˆ rtr Vq

-Heat conduction equation for solid

유체역학및열전달 17

Page 18: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Unsteady-state Conduction

유체역학및열전달 18

Page 19: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Semi-Infinite solid (1)

TtT 2Ñ=¶¶ a

-앞의식에서 solid에서의열전도반응식을이용하면

y=0

y=∞T0

T0 T1

As time goes by

01

0

TTTT

--

=q

2

2

yt ¶¶

=¶¶ qaq

로치환하면

¥====£=

yatCByatCBtatCI

0201100

qqq

..

....

tya

hhqq4

== ),( 라면

hqhh

hqq

dd

ttdd

t 21

-=¶¶

=¶¶

tdd

y

tdd

ydd

y

ahqq

ahqh

hqq

41

41

2

2

2

2

=¶¶

=¶¶

=¶¶

022

2

=+hqh

hq

dd

dd

010=¥===

qhqh,,

P.D.E

O.D.E

유체역학및열전달 19

Page 20: 유체역학및열전달 Chapter 10. Heat transfer by conductioncontents.kocw.net/KOCW/document/2014/Pusan/hyeongyu/10.pdf · 2016. 9. 9. · 부산대학교현규 Heat transfer by

부산대학교현규

Semi-Infinite solid (2)

y=0

y=∞T0

T0 T1

As time goes by

022

2

=+hqh

hq

dd

dd

010=¥===

qhqh,,

ò --=ty

da

hhp

q4

0

221/

)exp(

tyerf

TTTT

a41

01

0 -=--

\

유체역학및열전달 20