Deriving Steady-State Heat Conduction Equation in a Sphere

In summary, jdwood suggests that the equation governing the stead-state radial conduction of heat in a sphere or spherical shell with volumetric heat production is given by\frac{k}{r^2}\frac{d}{dr}(r^2\frac{dT}{dr})+\rho H = 0where k is thermal conductivity, H is the heat production per unit mass and \rho is the density. My first attempt was to start with the 3-dimensional fourier's law equation with a steady-state case, but I became lost at some point and ended up with an equation for q_{total} instead.The Attempt at a Solution
  • #1
protonchain
98
0

Homework Statement



Show that the equation governing the stead-state radial conduction of heat in a sphere or spherical shell with volumetric heat production is given by

[tex]\frac{k}{r^2}\frac{d}{dr}(r^2\frac{dT}{dr})+\rho H = 0[/tex]

where k is thermal conductivity, H is the heat production per unit mass and [tex]\rho[/tex] is the density

Homework Equations



See above

The Attempt at a Solution



My first attempt was to start off with the 3-dimensional fourier's law equation with a steady-state case aka

[tex]\nabla^2 T = -\frac{A}{k}[/tex]
[tex]\frac{d^2T}{dr^2} = -\frac{4\pi r^2}{k}[/tex]
[tex]\frac{d}{dr}(\frac{dT}{dr}) = -\frac{4\pi r^2}{k}[/tex]
[tex]\int \frac{d}{dr}(\frac{dT}{dr}) dr = \int -\frac{4\pi r^2}{k} dr[/tex]
[tex]\frac{dT}{dr} = -\frac{4\pi r^3}{3k}[/tex]

At this point I'm totally lost as to how to proceed. Have I even got the right equation to start with?
 
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  • #2
Doesn't look right to start there. Almost seems like you want to take the answer and find the starting point, which might not get you anywhere.

Consider the shell having inner radius of [tex]r[/tex] and total thickness [tex]\delta r[/tex]. The heat flow out of the surface is given by
[tex]
4\pi\left(r+\delta r\right)^2q_r(r+\delta r)
[/tex]

while the heat flow into the surface is
[tex]
4\pi r^2q_r(r)
[/tex]

The total heat flow out will be the first minus the second equation. If you then Taylor expand the first equation about the variation [tex]\delta r[/tex], you should see the direction which you need to go to finish the problem
 
  • #3
protonchain said:
[tex]\nabla^2 T = -\frac{A}{k}[/tex]
[tex]\frac{d^2T}{dr^2} = -\frac{4\pi r^2}{k}[/tex]

You seem to be claiming that [itex]\nabla^2T(r)=\frac{d^2T}{dr^2}[/itex]...that's not really what you get for the Laplacian in spherical coordinates is it?:wink:
 
  • #4
gabbagabbahey said:
You seem to be claiming that [itex]\nabla^2T(r)=\frac{d^2T}{dr^2}[/itex]...that's not really what you get for the Laplacian in spherical coordinates is it?:wink:

It is if there is no angular dependence, which he does seem to imply in the initial problem.
 
  • #5
jdwood983 said:
It is if there is no angular dependence, which he does seem to imply in the initial problem.

No, it isn't...look up the Laplacian in spherical coordinates.
 
  • #6
gabbagabbahey said:
No, it isn't...look up the Laplacian in spherical coordinates.

I think we may be disagreeing on different aspects. I was talking about the use of [tex]d[/tex] instead of [tex]\partial[/tex] and not the form while you were talking about the form and not the use of [tex]d[/tex].
 
  • #7
jdwood983 said:
I think we may be disagreeing on different aspects. I was talking about the use of [tex]d[/tex] instead of [tex]\partial[/tex] and not the form while you were talking about the form and not the use of [tex]d[/tex].

Okay, but that wasn't very clear from your last post.
 
  • #8
Sorry about the late response guys, I got held up at work.

So I followed your instructions jdwood, and I see how you had come up with the equation that you came up with. This is how far I've gotten.

[tex]4\pi\left((r^2+\delta r^2)\left(-k\frac{dT}{dr}+\delta r \left(-k\frac{d^2T}{dr^2}\right)\right) + r^2 k\frac{dT}{dr}\right) = q_{total}[/tex]

I am unsure of how to proceed from this part though.

Is the [tex]q_{total}[/tex] = some constant value?

Sorry if I'm asking the stupidest questions.
 
  • #9
I don't see why you are deriving the heat conduction equation...surely you've already seen it done in your textbook/class? If so, just use it.

[tex]\rho H=-k\nabla^2T[/tex]

Have you not seen the above form before?
 
  • #10
I have seen the above, but the problem is that because this is spherical, we need to start from the beginning and render the equation proper. At least that's how the prof wants to see it on the homework.

A HUGE thank you to jdwood for that massively helpful hint.

I just set your equation to what I should have realized it was right from the beginning

[tex]\rho H (4\pi r^2)\delta r [/tex]

I was able to derive it using just basic algebra, taylor expansion, and assumption that [tex]\delta r^2 = 0[/tex].
 

FAQ: Deriving Steady-State Heat Conduction Equation in a Sphere

What is heat conduction?

Heat conduction is the transfer of heat energy from one object to another through direct contact. In other words, it is the movement of heat from a warmer object to a cooler object.

How does heat conduction occur in a sphere?

In a sphere, heat conduction occurs through the movement of molecules. As the molecules in the warmer part of the sphere vibrate faster, they collide with the slower-moving molecules in the cooler part of the sphere, transferring heat energy.

What factors affect heat conduction in a sphere?

The rate of heat conduction in a sphere is affected by several factors, including the material of the sphere, the temperature difference between the two points, and the distance between the two points.

How is heat conduction in a sphere calculated?

The rate of heat conduction in a sphere can be calculated using the Fourier's Law equation, which takes into account the thermal conductivity of the material, the temperature difference, and the surface area of the sphere.

How is heat conduction in a sphere different from other shapes?

The rate of heat conduction in a sphere is different from other shapes because it has a symmetrical shape, which allows for heat to be transferred equally in all directions. Other shapes, such as cubes or cylinders, may have uneven heat distribution due to their asymmetrical shape.

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