In the energy balance formulation of the finite difference method, it is recommended that all heat transfer at the boundaries of the volume element be assumed to be into the volume element even for steady heat conduction. Is this a valid recommendation even though it seems to violate the conservation of energy principle?

Short Answer

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Answer: Yes, the recommendation is valid for the energy balance formulation of the finite difference method even for steady heat conduction. Although it may appear to violate the conservation of energy principle, any potential imbalance is compensated for in the discretized problem domain, maintaining the conservation of energy. This simplification does not negatively impact the overall energy balance or accuracy of the numerical solution when convergence is met.

Step by step solution

01

Understand the finite difference method

The finite difference method is a numerical technique to solve partial differential equations by discretizing the problem domain into a grid and solving the equations at the grid points. In the context of heat conduction, the finite difference method is used to find the temperature distribution in a material given the boundary conditions.
02

Analyze the energy balance formulation

In the energy balance formulation of the finite difference method, we consider the energy entering and leaving a volume element, as well as any internal energy generated within the element. The principle of conservation of energy, which states that the total energy in a closed system remains constant, should be maintained throughout the problem domain.
03

Examine the recommendation of assuming all heat transfer at the boundaries as inward heat transfer

The recommendation states that all heat transfer at the boundaries of the volume element should be assumed as into the volume element, even for steady heat conduction. This means that the energy being transferred across the boundary is always considered as being added to the volume element, irrespective of its direction (inward or outward).
04

Assess the impact of the recommendation on the conservation of energy principle

At first glance, this recommendation may seem to violate the conservation of energy principle, as it appears to increase energy within a volume element without accounting for energy leaving the element. However, in the case of steady heat conduction, the rate of heat transfer across the boundaries is constant, and there is no net accumulation or loss of energy within the volume element. Furthermore, considering neighboring volume elements, heat transfer considered as inward for one volume element would also be considered as inward for the neighboring volume element, effectively canceling out and maintaining the conservation of energy in the discretized problem domain. In addition, it's important to note that the finite difference method is a numerical approximation method, and this recommendation is a simplification to ease the computation, which doesn't affect the accuracy of the solution when convergence is met.
05

Conclude the analysis

In conclusion, while the recommendation to assume all heat transfer at the boundaries of volume element as inward heat transfer may seem to violate the conservation of energy principle, it is indeed valid for the energy balance formulation of the finite difference method even for steady heat conduction. This simplification does not negatively impact the overall energy balance or accuracy of the numerical solution, as any potential imbalance is compensated for in the discretized problem domain, maintaining the conservation of energy.

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Most popular questions from this chapter

For a one dimensional steady state variable thermal conductivity heat conduction with uniform internal heat generation, develop a generalized finite difference formulation for the interior nodes, with left surface boundary node exposed to constant heat flux and right surface boundary node exposed to convective environment. The variable conductivity is modeled such that the thermal conductivity varies linearly with the temperature as \(k(T)=k_{o}(1+\beta T)\) where \(T\) is the average temperature between the two nodes.

Consider steady 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 \(h\). 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 finite difference formulation of this problem to determine \(T_{1}\) and \(T_{2}\) for the case of specified temperature at the fin base and negligible heat transfer at the fin tip. All temperatures are in \({ }^{\circ} \mathrm{C}\).

Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), 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.

Consider steady two-dimensional heat conduction in a square cross section \((3 \mathrm{~cm} \times 3 \mathrm{~cm}, k=20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=\) \(6.694 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) with constant prescribed temperature of \(100^{\circ} \mathrm{C}\) and \(300^{\circ} \mathrm{C}\) at the top and bottom surfaces, respectively. The left surface is exposed to a constant heat flux of \(1000 \mathrm{~W} / \mathrm{m}^{2}\) while the right surface is in contact with a convective environment \(\left(h=45 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\right)\) at \(20^{\circ} \mathrm{C}\). Using a uniform mesh size of \(\Delta x=\Delta y\), determine \((a)\) finite difference equations and \((b)\) the nodal temperatures using Gauss-Seidel iteration method.

Consider steady heat conduction in a plane wall whose left surface (node 0 ) is maintained at \(30^{\circ} \mathrm{C}\) while the right surface (node 8 ) is subjected to a heat flux of \(1200 \mathrm{~W} / \mathrm{m}^{2}\). 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.

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