Consider transient 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 wall is initially at a specified temperature. Using the energy balance approach, obtain the explicit finite difference formulation of the boundary nodes for the case of insulation at the left boundary (node 0 ) and radiation at the right boundary (node 5) with an emissivity of \(\varepsilon\) and surrounding temperature of \(T_{\text {surr }}\).

Short Answer

Expert verified
Answer: For Node 0 (insulated boundary): \(T_{0} - T_{1} = 0\) For Node 5 (radiative boundary): \(T_{4} - T_{5} = \frac{\varepsilon \sigma \Delta x}{k} (T_5)^4 - \frac{\varepsilon \sigma \Delta x}{k} (T_{\text {surr }})^4\)

Step by step solution

01

Write the energy balance equation for an internal node

We will first write the heat balance equation for an internal node, say node i. Considering the heat generation within the volume and neglecting the heat conduction in the y and z directions, the energy balance equation can be written as: \(Q_{in} - Q_{out} = \dot{Q}_{gen} \Delta V\) For the finite difference method, we can write the heat flux using Taylor's series expansion: \(Q_{in} = k \frac{T_{i-1} - T_{i}}{\Delta x}\) and \(Q_{out} = k \frac{T_{i} - T_{i+1}}{\Delta x}\) Then, the energy balance equation becomes: \(k \frac{T_{i-1} - T_{i}}{\Delta x} - k \frac{T_{i} - T_{i+1}}{\Delta x} = \dot{Q}_{gen} \Delta x \Delta y \Delta z\)
02

Write the energy balance equation for the boundary nodes

Now, we will write the energy balance equation for the boundary nodes. Node 0 (insulated boundary condition): As there is no heat flux through the left boundary (insulated), we need to consider only the heat flux between node 0 and node 1: \(Q_{0 \to 1} = k \frac{T_{1} - T_{0}}{\Delta x}\) Node 5 (radiative boundary condition): The heat flux from node 5 to the surroundings is given by: \(Q_{5 \to \text{surr}} = \varepsilon \sigma\left((T_5)^4 - (T_{\text {surr }})^4\right)\) The heat flux between node 5 to node 4 is given by: \(Q_{5 \to 4} = k \frac{T_{4} - T_{5}}{\Delta x}\) So, the energy balance at node 5 becomes: \(k \frac{T_{4} - T_{5}}{\Delta x} = \varepsilon \sigma \left( (T_5)^4 - (T_{\text {surr }})^4 \right)\)
03

Perform the discretization to get the finite difference equations

Now, we need to discretize the energy balance equation for the internal nodes to get the finite difference equations. For internal nodes, the finite difference equation can be derived from the energy balance equation derived in step 1: \(\frac{k}{\Delta x}(T_{i-1} - 2T_i + T_{i+1}) = \dot{Q}_{gen} \Delta x \Delta y \Delta z\) For boundary nodes, we can write the finite difference equations based on the energy balance equation derived in step 2: Node 0 (insulated boundary condition): \(T_{0} - T_{1} = 0\) Node 5 (radiative boundary condition): \(T_{4} - T_{5} = \frac{\varepsilon \sigma \Delta x}{k} (T_5)^4 - \frac{\varepsilon \sigma \Delta x}{k} (T_{\text {surr }})^4\) Now, we have obtained the explicit finite difference equations for the boundary nodes as well as the internal nodes. These equations can be used to solve the transient heat conduction problem in the plane wall with variable heat generation and given boundary conditions.

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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 \(\Delta x\). Using the energy balance approach, obtain the finite difference formulation of the boundary nodes for the case of insulation at the left boundary (node 0 ) and radiation at the right boundary (node 5) with an emissivity of \(\varepsilon\) and surrounding temperature of \(T_{\text {surr }}\)

Consider transient one-dimensional heat conduction in a pin fin of constant diameter \(D\) with constant thermal conductivity. The fin is losing heat by convection to the ambient air at \(T_{\infty}\) with a heat transfer coefficient of \(h\) and by radiation to the surrounding surfaces at an average temperature of \(T_{\text {surr }}\). The nodal network of the fin consists of nodes 0 (at the base), 1 (in the middle), and 2 (at the fin tip) with a uniform nodal spacing of \(\Delta x\). Using the energy balance approach, obtain the explicit finite difference formulation of this problem for the case of a specified temperature at the fin base and negligible heat transfer at the fin tip.

A plane wall with surface temperature of \(350^{\circ} \mathrm{C}\) is attached with straight rectangular fins \((k=235 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The fins are exposed to an ambient air condition of \(25^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(154 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Each fin has a length of \(50 \mathrm{~mm}\), a base of \(5 \mathrm{~mm}\) thick, and a width of \(100 \mathrm{~mm}\). For a single fin, using a uniform nodal spacing of \(10 \mathrm{~mm}\), determine \((a)\) the finite difference equations, \((b)\) the nodal temperatures by solving the finite difference equations, and \((c)\) the heat transfer rate and compare the result with analytical solution.

Is there any limitation on the size of the time step \(\Delta t\) in the solution of transient heat conduction problems using (a) the explicit method and \((b)\) the implicit method?

Suggest some practical ways of reducing the roundoff error.

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