1-D steady state heat conduction equation (Cartisian, Cylindrical and Sperical)

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Homework Help Overview

The discussion revolves around the one-dimensional steady-state heat conduction equation in a medium with constant conductivity and volumetric heat generation, specifically in Cartesian, cylindrical, and spherical coordinate systems. Participants are exploring the temperature distribution in these systems, particularly in the context of fuel rods in a nuclear power plant.

Discussion Character

  • Exploratory, Conceptual clarification, Mathematical reasoning

Approaches and Questions Raised

  • Participants are attempting to derive expressions for temperature distribution using series expansions and are questioning the implications of coefficients in their series. There is also discussion on the nature of the heat generation term and its constancy with respect to distance.

Discussion Status

The discussion is active, with participants providing insights and corrections to each other's reasoning. Some participants have offered guidance on integrating and interpreting the equations, while others are exploring the implications of their findings on the coefficients of the series. There is a recognition of the need to satisfy boundary conditions in the solutions.

Contextual Notes

Participants are working under the constraints of specific boundary conditions for each coordinate system and are discussing the implications of zero heat generation on temperature distributions. There is an ongoing examination of assumptions regarding the constancy of the heat generation term.

  • #31
There is no need for a power series here...see my last post ^^^
 
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  • #32
Ok so I'm on the last one and have:
T(r)=1+\frac{\dot{q}}{4k}(R^2-r^2)+C_1(\frac{1}{R}-\frac{1}{r})

Now T(x)=\sum_{n=0}^{\infty}b_n x^n ?
 
  • #33
I think you should have:

T(r)=1+\frac{\dot{q}}{6k}(R^2-r^2)+C_1(\frac{1}{R}-\frac{1}{r})

Again, you would expect the temperature to be finite everywhere inside the sphere; so you can set C_1=0 since the 1/r blows up at r=0.

PS. don't forget to answer part (b) of the question for each case ;0)
 
  • #34
b. T(r)=1 when q_dot=0 for all three cases right?

Edit: Except the first one where T(r)=1+x
 
  • #35
Schmoozer said:

Homework Statement



The one dimensional steady-state heat conduction equation in a medium with constant conductivity (k) with a constant volumetric heat generation in three different coordinate systems (fuel rods in a nuclear power plant) is given as:

\frac{d^2 T}{dx^2}=-\frac{\dot{q}}{k} T(x=0)=1 T(x=1)=2 Cartisian

\frac{1}{r}\frac{d}{dr}(r\frac{dT}{dr})=-\frac{\dot{q}}{k} T(r=R)=1 Cylindrical

\frac{1}{r^2}\frac{d}{dr}(r^2\frac{dT}{dr})=-\frac{\dot{q}}{k} T(r=R)=1 Sperical

a. Find an expression for the temperature distribution in a solid for each case
b. What is a temperature distribution if the heat generation is zero?

Homework Equations



The Attempt at a Solution



T(x)=\sum_{n=0}^{\infty}b_n x^n

T'(x)=\sum_{n=0}^{\infty}nb_n x^n^-^1

T''(x)=\sum_{n=0}^{\infty}n(n-1)b_n x^n^-^2 so n=0, n=1

b_{0}=0

b_{1}=0

b_{2}=2x

b_{3}=3x^2

Am I at least on the right track?

LOL. Navaz's class? MECH522? Awesome!
 

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