Consider a nuclear fuel element \((k=57 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) that can be modeled as a plane wall with thickness of \(4 \mathrm{~cm}\). The fuel element generates \(3 \times 10^{7} \mathrm{~W} / \mathrm{m}^{3}\) of heat uniformly. Both side surfaces of the fuel element are cooled by liquid with temperature of \(80^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(8000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Using a uniform nodal spacing of \(8 \mathrm{~mm},(a)\) obtain the finite difference equations, \((b)\) determine the nodal temperatures by solving those equations, and (c) compare the surface temperatures of both sides of the fuel element with analytical solution.

Short Answer

Expert verified
#Answer: (a) The finite difference equations for the given system are: At node 1: $\frac{k}{\Delta x^2}(T_2 - T_1) + q'' - \frac{h \Delta x}{2}(T_1 - T_\infty) = 0$ At nodes 2 - 5: $\frac{k}{\Delta x^2}(T_{i+1} - 2T_i + T_{i-1}) + q'' = 0$ At node 6: $\frac{k}{\Delta x^2}(T_6 - T_5) + q'' + \frac{h \Delta x}{2}(T_6 - T_\infty) = 0$ (b) The nodal temperatures, $T_1, T_2, T_3, T_4, T_5,$ and $T_6$, can be obtained by solving the system of linear equations detailed in the solution. (c) To compare the surface temperatures with the analytical solution, we need to find the temperatures $T_0$ and $T_L$ from the conduction-convection equation for a plane wall with volumetric heat generation. Then, compare these values with the obtained nodal temperatures, $T_1$ and $T_6$. The difference between these values shows the accuracy of our numerical solution.

Step by step solution

01

Problem Setup

First, we need to assign some variables for the given input parameters and constants and also divide the plane wall into equal segments of the specified nodal spacing. Let the nodal spacing be \(\Delta x\), where \(\Delta x = 8 \times 10^{-3} \, \text{m}\). Let the thickness of the wall be \(L = 4 \times 10^{-2} \, \text{m}\). Based on the thickness and the nodal spacing, we can find the number of nodes, n: $$n = \frac{L}{\Delta x} + 1 = \frac{4 \times 10^{-2}}{8 \times 10^{-3}} + 1 = 6$$ Now, let's assign some variables for the given data: $$k = 57 \, \mathrm{W/m \cdot K}$$ $$q'' = 3 \times 10^7 \, \mathrm{W/m^3}$$ $$T_\infty=80^{\circ} \mathrm{C}$$ $$h = 8000 \, \mathrm{W/m^2 \cdot K}$$
02

a) Obtain Finite Difference Equations

Using the energy balance in a one-dimensional cartesian coordinate system, we can write the discretized form of the heat conduction equation for each node i as: $$\frac{k}{\Delta x^2}(T_{i+1} - 2T_i + T_{i-1}) + q'' = 0$$ We can rewrite the equation for all nodes, including the boundary conditions at nodes 1 and 6. At node 1, we have to consider the convection from the liquid: $$\frac{k}{\Delta x^2}(T_2 - 2T_1 + T_1) + q'' - \frac{h \Delta x}{2}(T_1 - T_\infty) = 0$$ At node 6, we have to consider the convection from the liquid: $$\frac{k}{\Delta x^2}(T_6 - 2T_5 + T_4) + q'' + \frac{h \Delta x}{2}(T_6 - T_\infty) = 0$$
03

b) Determine Nodal Temperatures by Solving Equations

We can now set up a system of linear equations for the nodal temperatures \(T_1, T_2, T_3, T_4, T_5,\) and \(T_6\). We have six equations: 1. \(\frac{k}{\Delta x^2}(T_2 - T_1) + q'' - \frac{h \Delta x}{2}(T_1 - T_\infty) = 0\) 2. \(\frac{k}{\Delta x^2}(T_3 - 2T_2 + T_1) + q'' = 0\) 3. \(\frac{k}{\Delta x^2}(T_4 - 2T_3 + T_2) + q'' = 0\) 4. \(\frac{k}{\Delta x^2}(T_5 - 2T_4 + T_3) + q'' = 0\) 5. \(\frac{k}{\Delta x^2}(T_6 - 2T_5 + T_4) + q'' = 0\) 6. \(\frac{k}{\Delta x^2}(T_6 - T_5) + q'' + \frac{h \Delta x}{2}(T_6 - T_\infty) = 0\) By solving these equations (e.g, using matrix inversion, Gaussian elimination, or any suitable numerical solver), we can obtain the nodal temperatures \(T_1, T_2, T_3, T_4, T_5,\) and \(T_6\).
04

c) Compare Surface Temperatures with Analytical Solution

To find the analytical solution for this problem, we can use the conduction-convection equation for a plane wall with volumetric heat generation: $$k \frac{dT}{dx} = h \cdot (T - T_\infty) + \frac{q'' x}{2}$$ Solving for the temperature distribution in both sides, we can find the surface temperatures at \(x = 0\) and \(x = L\), let's call them \(T_0\) and \(T_L\). Then, we can compare these values with the obtained nodal temperatures at \(T_1\) and \(T_6\), which are the numerical surface temperatures. By comparing these values, we can determine the accuracy of our numerical solution.

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Most popular questions from this chapter

In many engineering applications variation in thermal properties is significant especially when there are large temperature gradients or the material is not homogeneous. To account for these variations in thermal properties, develop a finite difference formulation for an internal node in case of a three dimensional steady state heat conduction equation with variable thermal conductivity.

How can a node on an insulated boundary be treated as an interior node in the finite difference formulation of a plane wall? Explain.

What are the basic steps involved in solving a system of equations with Gauss- Seidel method?

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