Thermal Physics problem: Heat transfer coefficient?

AI Thread Summary
The discussion centers on understanding the heat transfer coefficient in the context of a thermal physics problem involving a hollow cylinder. The user seeks clarification on the definition of the heat transfer coefficient and its relevance to their assignment, which involves finding the temperature distribution in the cylinder after stationary conditions are reached. A helpful response provides the equation for heat flow rate and suggests using thermal conductivity to solve the problem. The user successfully derives the temperature function T(r) and concludes that the result does not depend on the heat transfer coefficient H. This highlights the importance of correctly interpreting terms and equations in thermal physics problems.
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I'm having a bit of trouble with a Thermal Physics excercise. I was wondering if anyone knew what the definition of the heat transfer coefficient was? I can't find anything about it in my textbook (Thermal Physics, 2nd ed., C.B.P. Finn).

More specifically, the assignment at hand says to find the temperature T(r) in a hollow cyllinder with length L (where r is the distance from the axis of the cyllinder, so that the cyllinder is symmetric about this axis), inner radius r_1, outer radius r_2, inner wall is kept at temperature T_1 and outer wall temperature is kept at T_2 (temperature of the surroundings), after equilibrium has been reached. The material of the cyllinder has heat transfer coefficient H. Also, T_2<T_1. (It also asks explicitly if the result depends on H.)

Any tips or hints to get me started?
 
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Thermal Conductivity coefficient is what you're looking for. The equation to use is:
q = -(kA)\frac{dt}{dx}

where

q is heat flow rate is watts.

k is thermal conductivity in \frac{W}{m \Dot K}

A is cross sectional area normal to flow in m^2

\frac{dt}{dx} is the temperature gradient in \frac{K}{m}

Regards,

Nenad
 
First of all, thanks for the help Nenad.
I guess I should've mentioned the text was in Norwegian, and heat transfer coefficient seemed like the most direct translation of the wording in the text. Another thing I think i mis-translated was that it said stationary conditions, not equillibrium.

I think I got it right thanks to your help though:
First setting A=2 \pi rL, and then using your equation: \frac{dQ}{dt}=-(HA)\frac{dT}{dr}=C , where I set the heat flow rate to a constant since there are stationary conditions (but not zero since that would be absurd as long as we are using energy to maintain T_1 on the inner wall, right?).
For simplicity, I then set C'=-\frac{C}{H2 \pi L}, and the resulting differential equation is:
dT=\frac{C'}{r}dr
which gives:
T(r)=C'\ln(r)+T_0
solving for C' and T_0 using given initial conditions (T(r_1)=T_1 and T(r_2)=T_2) gives:
T(r)=\frac{T_2-T_1}{\ln(\frac{r_2}{r_1})}\ln(\frac{r}{r_1})+T_1
Thus T(r) doesn't depend on H.
 
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