Heat conduction through a slab with internal heat generation

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SUMMARY

The discussion focuses on solving the heat conduction problem through a slab with internal heat generation, specifically a point source represented by Qvol. The approach involves dividing the slab into two sections and applying Fourier's Law to derive heat transfer equations for both sides. Key variables include TL, TM, TR for temperatures, and Qin, Qmid, Qout for heat transfer rates. The solution requires careful consideration of boundary conditions and the relationship between heat flux and temperature gradients.

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  • Understanding of Fourier's Law of heat conduction
  • Familiarity with differential equations in heat transfer
  • Knowledge of boundary conditions in thermal systems
  • Ability to manipulate algebraic equations for solving unknowns
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Homework Statement


There's a slab of a material with temperature T1 on the left and the T2 on the right. The thickness of the material is l with area A. In the centre, there is heat generation Qvol in the centre, which is a thin rod.

Find the heat transfer Q through the material.

Homework Equations





The Attempt at a Solution


My issue is with modeling the Qvol. If it was heat generation through the material, I'd just use the DE
D2T/dt2 = -(1/k)Qvol
with BCs T(0) = T1
T(l) = T2
which is easily solved,

But it's a 'point' source of heat, and unless I'm mistaken, I can't use this. The lecturer seemed to hint that it could be solved with looking at each side of the slab separately.

Any help?
 
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I think the lecturer gave a good hint. Assume that the heat flux from Qvol is divided up between the left and right sides. For each side, you have a known temperature on one side and an unknown fraction of Qvol entering from the other side. Also, the fractions must add up to one. And finally, the temperature at the middle is the same in each equation. That should give you an equal number of equations and unknowns to solve the problem.
 
So basically treat it as a series question?

Defining the temps as
TL, TM and TR, (left, mid, right),
Qin as the Q coming in from the left,
Qmid as the heat through the middle,
Qout as the heat from the right,
a*Qvol as the fraction going into the left,
a*Qvol as the fraction going into the right,
L a the length with each side = to L/2:

Qin - a*Qvol = Qmid
Qout = Qmid + b*Qvol

Qin = (Tm - T1)*(2A*k)/L
so that
Qmid = (Tm - T1)*(2A*k)/L - a*Qvol

and (Fourier's Equation for the right side):
Qmid = (T2 - Tm)*(2A*k)/L

Solving the above two equations to get rid of Tm:
Qmid = (T2 - T1)*(A*k)/L - (a/2)*Qvol

So,
Qout = (T2 - T1)*(A*k)/L + (b - a/2)*Qvol

Qout = (T2 - T1)*(A*k)/L + (1 - 3a/2)*Qvol
 
Why 2A instead of A?
 
2A because each side has length L/2 - so Ak/(L/2) = 2Ak/L.

Is the reasoning right?
 
Ah, got it. That part's OK, then. It's just that your last line looks a little off and I'm looking for problems in the calculations.

Why do you have Qin = (Tm - T1)*(2A*k)/L when Qin is defined as the heat transfer coming in? If Tm>T1, this predicts positive flux coming in from the left, which doesn't make sense.

Then you have Qmid = (T2 - Tm)*(2A*k)/L; shouldn't this be Qout? (And again there seems to be a minus sign missing.)
 

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