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Consider steady heat conduction in a plane wall whose left surface (node 0 ) is maintained at \(40^{\circ} \mathrm{C}\) while the right surface (node 8 ) is subjected to a heat flux of \(3000 \mathrm{~W} / \mathrm{m}^{2}\). Express the finite difference formulation of the boundary nodes 0 and 8 for the case of no heat generation. Also obtain the finite difference formulation for the rate of heat transfer at the left boundary.

Short Answer

Expert verified
Question: Express the finite difference formulation for the boundary nodes 0 and 8 and find the finite difference formulation for the rate of heat transfer at node 0 in a steady heat conduction problem with no heat generation inside the wall. Given that the temperature at node 0 is 40ºC and the heat flux at node 8 is 3000 W/m². Answer: The finite difference formulations for the boundary nodes are: 1. For node 0: \(\frac{\partial T}{\partial x} = \frac{T_1 - 40}{\Delta x}\) 2. For node 8: \(3000 = -k \frac{T_8 - T_7}{\Delta x}\) The finite difference formulation for the rate of heat transfer at node 0 is: \(q_0 = -k \frac{T_1 - 40}{\Delta x}\).

Step by step solution

01

1. Discretize the heat equation.

Start by discretizing the one-dimensional heat equation without heat generation using central differencing. We can write the second derivative as follows: \(\frac{\partial^2 T}{\partial x^2} = \frac{T_{i-1} - 2T_i + T_{i+1}}{\Delta x^2}\), where \(T_i\) is the temperature at node i and \(\Delta x\) is the distance between two adjacent nodes.
02

2. Apply boundary conditions at node 0.

At node 0, the temperature is fixed at \(40^{\circ} C\). Since we are using central differencing, we need to use a backward difference at node 0 for the finite difference formulation: \(\frac{\partial T}{\partial x} = \frac{T_1 - T_0}{\Delta x}\), where \(\Delta x\) is the distance between nodes 0 and 1.
03

3. Apply boundary conditions at node 8.

At node 8, the heat flux is fixed at \(3000 \, W/m^2\). The heat flux can be expressed in terms of temperature gradient, using Fourier's law of heat conduction: \(q = -k \frac{\partial T}{\partial x}\), where k is the thermal conductivity of the material. Since we are using central differencing, we need to use a forward difference at node 8 for the finite difference formulation: \(\frac{\partial T}{\partial x} = \frac{T_8 - T_7}{\Delta x}\), where \(\Delta x\) is the distance between nodes 7 and 8. Now, substitute the given heat flux into Fourier's law: \(3000 = -k \frac{T_8 - T_7}{\Delta x}\).
04

4. Obtain the finite difference formulation for the rate of heat transfer at node 0.

To find the rate of heat transfer at the left boundary (node 0), we can use Fourier's law of heat conduction and the previously found temperature gradient at node 0. The rate of heat transfer \(q_0\) can be expressed as follows: \(q_0 = -k \frac{T_1 - T_0}{\Delta x}\), where k is the thermal conductivity of the material and \(T_0\) is the temperature at node 0 (\(40^{\circ} C\)). So, the finite difference formulations we have obtained are: 1. For node 0: \(\frac{\partial T}{\partial x} = \frac{T_1 - 40}{\Delta x}\) 2. For node 8: \(3000 = -k \frac{T_8 - T_7}{\Delta x}\) 3. For the rate of heat transfer at node 0: \(q_0 = -k \frac{T_1 - 40}{\Delta x}\)

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Most popular questions from this chapter

Consider steady one-dimensional heat conduction in a plane wall with variable heat generation and constant thermal conductivity. The nodal network of the medium consists of nodes \(0,1,2,3,4\), and 5 with a uniform nodal spacing of \(\Delta x\). The temperature at the right boundary (node 5) is specified. Using the energy balance approach, obtain the finite difference formulation of the boundary node 0 on the left boundary for the case of combined convection, radiation, and heat flux at the left boundary with an emissivity of \(\varepsilon\), convection coefficient of \(h\), ambient temperature of \(T_{\infty}\), surrounding temperature of \(T_{\text {surr }}\) and uniform heat flux of \(\dot{q}_{0}\). Also, obtain the finite difference formulation for the rate of heat transfer at the right boundary.

Write a two-page essay on the finite element method, and explain why it is used in most commercial engineering software packages. Also explain how it compares to the finite difference method.

The explicit finite difference formulation of a general interior node for transient heat conduction in a plane wall is given by $$ T_{m=1}^{i}-2 T_{m}^{i}+T_{m+1}^{i}+\frac{e_{m}^{i} \Delta x^{2}}{k}=\frac{T_{m}^{i+1}-T_{m}^{i}}{\tau} $$ Obtain the finite difference formulation for the steady case by simplifying the preceding relation.

How is the finite difference formulation for the first derivative related to the Taylor series expansion of the solution function?

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