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Consider steady one-dimensional heat conduction in a composite plane wall consisting of two layers \(A\) and \(B\) in perfect contact at the interface. The wall involves no heat generation. The nodal network of the medium consists of nodes 0,1 (at the interface), and 2 with a uniform nodal spacing of $\Delta x$. Using the energy balance approach, obtain the finite difference formulation of this problem for the case of insulation at the left boundary (node 0 ) and radiation at the right boundary (node 2 ) with an emissivity of \(\varepsilon\) and surrounding temperature of \(T_{\text {sarr }}\).

Short Answer

Expert verified
Answer: The finite difference formulation can be represented by the following equations: 1. \(T_1 - T_0 = 0\) 2. \(\frac{\Delta x_A}{k_A} \frac{T_1 - T_0}{\Delta x} = \frac{\Delta x_B}{k_B} \frac{T_2 - T_1}{\Delta x}\) 3. \(k_B \frac{T_2 - T_1}{\Delta x_B} = \varepsilon \sigma(T_2^4 - T_{sarr}^4)\) These equations can be solved numerically to find the temperature distribution across the composite wall.

Step by step solution

01

Energy balance equation

In a steady-state one-dimensional heat conduction, the energy balance equation for each layer can be written as: Layer A: \(k_{A} \frac{T_1 - T_0}{\Delta x} = k_{A} \frac{T_1 - T_0}{\Delta x_A}\) Layer B: \(k_{B} \frac{T_2 - T_1}{\Delta x} = k_{B} \frac{T_2 - T_1}{\Delta x_B}\) where \(k_A\) and \(k_B\) are the thermal conductivities of layers A and B, respectively, and \(T_0\), \(T_1\), and \(T_2\) are the temperatures at nodes 0, 1, and 2, respectively.
02

Insulation Boundary Condition

At node 0, there is insulation, which means there is no heat flow through the left boundary. Mathematically, this condition is expressed as \(k_A \frac{dT_A}{dx}=0\). Since \(T_0\) is insulated, we can set the energy balance equation of Layer A at this node as: \(k_A \frac{T_1 - T_0}{\Delta x_A} = 0\)
03

Radiation Boundary Condition

At node 2, there is radiation, which means there is heat loss by radiation. The heat loss due to radiation is given by the Stefan-Boltzmann law, \(q_R = \varepsilon \sigma (T^4 - T_{surr}^4)\), where \(\varepsilon\) is emissivity and \(\sigma\) is the Stefan-Boltzmann constant. We can write the energy balance of Layer B at node 2 as: \(k_B \frac{T_2 - T_1}{\Delta x_B} = \varepsilon \sigma(T_2^4 - T_{sarr}^4)\)
04

Finite difference formulation

Now we have three equations with three unknowns, \(T_0\), \(T_1\), and \(T_2\). We can rearrange them in the form of finite difference equations: 1. \(T_1 - T_0 = 0\) 2. \(\frac{\Delta x_A}{k_A} \frac{T_1 - T_0}{\Delta x} = \frac{\Delta x_B}{k_B} \frac{T_2 - T_1}{\Delta x}\) 3. \(k_B \frac{T_2 - T_1}{\Delta x_B} = \varepsilon \sigma(T_2^4 - T_{sarr}^4)\) These finite difference equations can be solved numerically to obtain the temperature distribution across the composite wall.

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Most popular questions from this chapter

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 , \(1,2,3\), and 4 with a uniform nodal spacing of $\Delta x$. The wall is initially at a specified temperature. The temperature at the right boundary (node 4) is specified. Using the energy balance approach, obtain the explicit finite difference formulation of the boundary node 0 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 \(\dot{q}_{0}\) toward the wall. Also, obtain the finite difference formulation for the total amount of heat transfer at the right boundary for the first 20 time steps.

What is a practical way of checking if the round-off error has been significant in calculations?

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.

Consider a long solid bar \((k=28 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=12 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) of square cross section that is initially at a uniform temperature of \(32^{\circ} \mathrm{C}\). The cross section of the bar is \(20 \mathrm{~cm} \times 20 \mathrm{~cm}\) in size, and heat is generated in it uniformly at a rate of $\dot{e}=8 \times 10^{5} \mathrm{~W} / \mathrm{m}^{3}$. All four sides of the bar are subjected to convection to the ambient air at \(T_{\infty}=30^{\circ} \mathrm{C}\) with a heat transfer coefficient of $h=45 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Using the explicit finite difference method with a mesh size of \(\Delta x=\Delta y=10 \mathrm{~cm}\), determine the centerline temperature of the bar \((a)\) after \(20 \mathrm{~min}\) and \((b)\) after steady conditions are established.

Consider a 2-m-long and \(0.7-\mathrm{m}\)-wide stainless steel plate whose thickness is \(0.1 \mathrm{~m}\). The left surface of the plate is exposed to a uniform heat flux of \(2000 \mathrm{~W} / \mathrm{m}^{2}\), while the right surface of the plate is exposed to a convective environment at $0^{\circ} \mathrm{C}\( with \)h=400 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The thermal conductivity of the stainless steel plate can be assumed to vary linearly with temperature range as \(k(T)=k_{o}(1+\beta T)\) where $k_{o}=48 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\beta=9.21 \times 10^{-4 \circ} \mathrm{C}^{-1}$. The stainless steel plate experiences a uniform volumetric heat generation at a rate of $8 \times 10^{5} \mathrm{~W} / \mathrm{m}^{3}$. Assuming steady-state one-dimensional heat transfer, determine the temperature distribution along the plate thickness.

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