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Värmeledningsekvationen (Heat<br />

conduction equation),<br />

isotropt (isotropic) material<br />

∂t<br />

∂ ⎛ ∂t<br />

ρc<br />

= ⎜λ<br />

∂τ<br />

∂x<br />

⎝ ∂x<br />

∂ ⎛ ∂t<br />

⎜<br />

∂z ⎝<br />

λ ∂z<br />

⎞<br />

⎟ +<br />

⎠<br />

⎞<br />

⎟ +<br />

⎠<br />

∂ ⎛ ∂t<br />

⎜λ<br />

∂y<br />

⎝ ∂y<br />

Q′<br />

⎞<br />

⎟ +<br />

⎠<br />

( 1−18)<br />

Om λ = konstant, if λ constant ⇒ homogent<br />

(homogeneous) material<br />

∂t<br />

∂τ<br />

=<br />

2<br />

⎧ ∂ t<br />

a⎨<br />

2<br />

⎩<br />

∂<br />

x<br />

+<br />

∂<br />

2<br />

∂<br />

y<br />

t<br />

2<br />

+<br />

2<br />

∂ t ⎫<br />

+<br />

2 ⎬<br />

∂<br />

z<br />

⎭<br />

Q′<br />

ρ<br />

c<br />

(1 −19)<br />

a<br />

λ ⎧termisk diffusivitet⎫<br />

= ⎨ ⎬<br />

ρ c<br />

⎩ thermal diffusivity<br />


Enkel Plan Vägg, Simple Plane<br />

Wall, Kap., Ch. 3<br />

t 1 b<br />

t 1 > t<br />

t 2<br />

2<br />

x<br />

Q & ∂<br />

stationär värmeledning ⇒ = 0<br />

∂τ<br />

steady heat conduction:<br />

∂ ∂<br />

endimensionellt:<br />

= ≡ 0<br />

∂yy<br />

∂zz<br />

one dimensional case:<br />

ingen intern värmegenerering: Q′ = 0<br />

no internal heat generation:<br />

λ = konstant ober av t och x: λ constant independent of<br />

t and x:<br />

2<br />

(1 - 19) ⇒<br />

d t<br />

= 0<br />

2<br />

dx<br />

lösning, solution: t = c 1 x + c 2<br />

RV, BC: x = 0 t = t 1 ; x = b t = t 2<br />

⇒ linjär temperaturfördelning


Enkel Plan Vägg,forts, Simple plane<br />

wall<br />

t t<br />

t<br />

2 −<br />

= 1 + x (3 − 3)<br />

b<br />

t<br />

1<br />

Värmeflödet, The heat flow:<br />

dt<br />

Q&<br />

= −λA<br />

dx<br />

Q<br />

1<br />

Q&<br />

= λA<br />

(t1 − t 2 ) (3 − 4)<br />

b<br />

Alternativ formulering, Alternate formulation<br />

b<br />

t<br />

{<br />

1− t2<br />

= ⋅<br />

{<br />

Q&<br />

λ A<br />

drivkraft { flöde<br />

" spänning " resi−<br />

" ström "<br />

potential stan s current<br />

resis tan ce


Sammansatt plan vägg-<br />

Composite Wall<br />

t 1<br />

λ1<br />

λ 3<br />

λ 2<br />

t 4<br />

λ<br />

b 1 b 2 b 3<br />

λ 3<br />

Q &<br />

”Seriekoppling - Serial circuit”<br />

Q<br />

t<br />

1<br />

∑<br />

t 1− t4 = ( termisk res, thermal res)<br />

⋅Q&<br />

− t<br />

4<br />

=<br />

⎛<br />

⎜<br />

⎝<br />

b1<br />

b<br />

+<br />

2<br />

+<br />

λ A λ A<br />

1<br />

2<br />

b3<br />

λ A<br />

⇒<br />

t<br />

t<br />

Q&<br />

1 −<br />

=<br />

4<br />

(3 − 6)<br />

b1<br />

b b<br />

+<br />

2<br />

+<br />

3<br />

λ1A<br />

λ2A<br />

λ3A<br />

Konvektion, Convection<br />

Q&<br />

= α A( t −t ) ⇒ Konvektiv resis tan s :<br />

f<br />

3<br />

⎞<br />

⎟⋅<br />

⎠<br />

Q&<br />

1<br />

Convective resis tan ce<br />

α A<br />

w


Sammansatt Vägg- Composite Wall,<br />

forts, continuation<br />

t f1<br />

α 1<br />

λ 1 λ 2<br />

λ 3<br />

α 2<br />

t f2<br />

Q&<br />

=<br />

1<br />

α A<br />

1<br />

+<br />

b 1 b 2 b 3<br />

)<br />

t<br />

f 1<br />

3<br />

∑<br />

i=<br />

l<br />

− t<br />

i<br />

f 2<br />

bi<br />

+<br />

λ A<br />

1<br />

α A<br />

2<br />

(3 − 7


Cirkulärt rör eller skikt-Circular<br />

tube or layer (shell)<br />

• Innerradie, inner radius r i ;Ytterradie, outer radius r o ; Innerytans<br />

temperatur, inner temperature t i ; Ytterytans temperatur, outer<br />

temperature t o<br />

r o<br />

radiell temperaturfördelning<br />

t i<br />

> t o<br />

r i<br />

t i<br />

r<br />

dr<br />

r i<br />

radial temperature distribution<br />

r o<br />

t o<br />

t i<br />

> t o<br />

)<br />

&<br />

t<br />

−t<br />

i o<br />

Q= −1<br />

1<br />

⎛<br />

r<br />

ln<br />

i ⎞<br />

⎜ ⎟<br />

2πλL<br />

⎝ro<br />

⎠<br />

(3−10


Cirkulärt rör eller skikt sammansatt av olika<br />

material, Composite circular wall (shell)<br />

radiell temperaturfördelning<br />

t fi > t fo<br />

r 1<br />

λ 1<br />

λ 2<br />

t fi<br />

r 2<br />

r 3<br />

t 1<br />

t 2<br />

t 3<br />

t fo<br />

radial a temperature e distribution<br />

t fi > t fo<br />

0<br />

Q&<br />

=<br />

tf<br />

−t<br />

i fo<br />

1 1 r 1 r 1<br />

+ ln + ln +<br />

2 πrL<br />

π<br />

r<br />

L<br />

α<br />

2<br />

3<br />

1L<br />

α<br />

i<br />

2<br />

π<br />

L<br />

λ<br />

1<br />

r<br />

1<br />

2<br />

π<br />

L<br />

λ<br />

2<br />

r<br />

2<br />

2<br />

3<br />

0

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