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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 \(T_{\text {carr }}\)

Short Answer

Expert verified
Answer: The finite difference equation for node 0 is given by the insulation boundary condition, which states that the temperature is constant and there is no heat conduction out of the boundary. Therefore, the equation is: $$ T_{0} = T_{1} $$ For node 5, the finite difference equation is derived from the radiation boundary condition, where heat loss occurs due to radiation. The resulting equation is: $$ k \left(\frac{T_{5} - T_{4}}{\Delta x}\right) = \varepsilon \sigma (T_{5}^4 - T_{\text {carr}}^4) $$

Step by step solution

01

Heat conduction equation

The steady one-dimensional heat conduction in a plane wall can be modeled by the following equation: $$ k\frac{d^2T}{dx^2} - q_\text{gen} = 0$$ where \(k\) is the thermal conductivity, \(T\) is the temperature, \(x\) is the spatial coordinate, and \(q_\text{gen}\) is the heat generation per unit volume.
02

Finite difference formulation for boundary nodes

We can discretize the heat conduction equation using the central difference approximation for the second derivative: $$ \frac{d^2T}{dx^2} = \frac{T_{i-1} - 2T_{i} + T_{i+1}}{\Delta x^2}$$ This equation will be used to obtain the finite difference formulations for the boundary nodes 0 and 5.
03

Insulation boundary condition at node 0

The insulation boundary condition states that the heat flux at node 0 is zero, which means the temperature is constant and there is no heat conduction out of the boundary. The finite difference equation can be written as: $$ k\left(\frac{T_{1} - T_{0}}{\Delta x}\right) = 0$$ From this equation, we have: $$ T_{0} = T_{1} $$
04

Radiation boundary condition at node 5

The radiation boundary condition states that there is heat loss at node 5 due to radiation. It can be expressed as: $$ q_\text{rad} = \varepsilon \sigma (T_{5}^4 - T_{\text {carr}}^4) $$ The heat flux at the boundary can be approximated by: $$ q_\text{rad} = k\left(\frac{T_{5} - T_{4}}{\Delta x}\right) $$ By setting these equations equal, we have: $$ k \left(\frac{T_{5} - T_{4}}{\Delta x}\right) = \varepsilon \sigma (T_{5}^4 - T_{\text {carr}}^4) $$ These last two equations provide the finite difference formulation at nodes 0 and 5 required to solve the problem with the defined boundary conditions.

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Most popular questions from this chapter

A stainless steel plate is connected to an insulation plate by square ASTM A479 904L stainless steel bars. Each square bar has a thickness of $1 \mathrm{~cm}\( and a length of \)5 \mathrm{~cm}$. The bars are exposed to convection heat transfer with a hot gas. The temperature of the hot gas is \(300^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $25 \mathrm{~W} / \mathrm{m}^{2}$. . The thermal conductivity for ASTM A479 904L stainless steel is known to be \(12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The stainless steel plate maintains a uniform temperature of $100^{\circ} \mathrm{C}$. According to the ASME Code for Process Piping (ASME B31.3-2014, Table A-1M), the maximum use temperature for ASTM A479 904L stainless steel bar is \(260^{\circ} \mathrm{C}\). Using the finite difference method with a uniform nodal spacing of \(\Delta x=5 \mathrm{~mm}\) along the bar, determine the temperature at each node. Compare the numerical results with the analytical solution. Plot the temperature distribution along the bar. Would any part of the ASTM A479 904L bars be above the maximum use temperature of \(260^{\circ} \mathrm{C}\) ?

Consider a stainless steel spoon $(k=15.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\varepsilon=0.6$ ) that is partially immersed in boiling water at \(100^{\circ} \mathrm{C}\) in a kitchen at \(32^{\circ} \mathrm{C}\). The handle of the spoon has a cross section of about $0.2 \mathrm{~cm} \times 1 \mathrm{~cm}\( and extends \)18 \mathrm{~cm}$ in the air from the free surface of the water. The spoon loses heat by convection to the ambient air with an average heat transfer coefficient of $h=13 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ as well as by radiation to the surrounding surfaces at an average temperature of \(T_{\text {surr }}=295 \mathrm{~K}\). Assuming steady one- dimensional heat transfer along the spoon and taking the nodal spacing to be \(3 \mathrm{~cm},(a)\) obtain the finite difference formulation for all nodes, \((b)\) determine the temperature of the tip of the spoon by solving those equations, and (c) determine the rate of heat transfer from the exposed surfaces of the spoon.

A stainless steel plate $(k=13 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 1 \mathrm{~cm}\( thick) is attached to an ASME SB-96 coppersilicon plate ( \)k=36 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 3 \mathrm{~cm}$ thick) to form a plane wall. The bottom surface of the ASME SB-96 plate (surface 1) is subjected to a uniform heat flux of \(750 \mathrm{~W} / \mathrm{m}^{2}\). The top surface of the stainless steel plate (surface 2 ) is exposed to convection heat transfer with air at \(T_{\infty}=20^{\circ} \mathrm{C}\), and thermal radiation with the surroundings at \(T_{\text {surr }}=20^{\circ} \mathrm{C}\). The combined heat transfer coefficient for convection and radiation is \(h_{\mathrm{comb}}=7.76 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ASME Boiler and Pressure Vessel Code (ASME BPVC.IV-2015, HF-300) limits equipment constructed with ASME SB-96 plate to be operated at a temperature not exceeding \(93^{\circ} \mathrm{C}\). Using the finite difference method with a uniform nodal spacing of \(\Delta x=5 \mathrm{~mm}\) along the plate thicknesses, determine the temperature at each node. Would the use of the ASME SB-96 plate under these conditions be in compliance with the ASME Boiler and Pressure Vessel Code? What is the highest heat flux that the bottom surface can be subjected to such that the ASME SB-96 plate is still operating below \(93^{\circ} \mathrm{C}\) ?

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?

Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=1.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=24 \mathrm{~m}^{2}\). The left side of the wall is subjected to a heat flux of \(\dot{q}_{0}=350 \mathrm{~W} / \mathrm{m}^{2}\), while the temperature at that surface is measured to be \(T_{0}=60^{\circ} \mathrm{C}\). Assuming steady one-dimensional heat transfer and taking the nodal spacing to be $6 \mathrm{~cm},(a)$ obtain the finite difference formulation for the six nodes and \((b)\) determine the temperature of the other surface of the wall by solving those equations.

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