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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

Expert verified
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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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Heat Conduction
Heat conduction is a method of heat transfer through a material without any movement of the material itself. This process occurs at the molecular level as kinetic energy is transferred from a hotter part of the material to a cooler region. In practical terms, this means heat moves from areas of high temperature to areas with lower temperature until an equilibrium is reached. Heat conduction is crucial in many engineering applications, such as designing insulation materials or understanding how engines cool down.

To mathematically describe heat conduction, we often use Fourier's Law, which states:
  • The heat transfer rate is proportional to the negative gradient of temperatures and the area across which heat conduction occurs.
This law is foundational in analyzing heat transfer problems and leads to the heat equation, which is used in various heat conduction calculations.
Energy Balance
The energy balance principle is a fundamental concept that ensures all energy entering a system is accounted for, either staying within the system, being transformed, or leaving it. This principle is vital for modeling systems in thermal engineering, ensuring that calculations accurately represent physical reality.

In the context of the finite difference method, the energy balance approach involves accounting for all energies entering, leaving, and generated within a volume element. When studying heat conduction using numerical methods, an energy balance helps to make sure that the total energy in the system remains constant, maintaining a correct and realistic model.
  • Energy entering the system is considered through heat sources or boundary influx.
  • Energy leaving the system could be due to heat sinks or through boundaries.
In practice, the energy balance ensures that calculations respect the physical laws of energy transfer, crucial for obtaining accurate results.
Conservation of Energy
The conservation of energy is a fundamental principle in physics stating that energy cannot be created or destroyed in an isolated system; it can only change forms. This principle applies to all energy-related calculations and is particularly relevant when using numerical methods to solve heat conduction problems.

In scenarios such as steady-state heat conduction, maintaining the conservation of energy is essential. Even when assumptions, like considering all boundary heat transfer as inward, seem to contradict conservation, they must ultimately yield zero net energy accumulation over time.

This can be achieved in discretized domains by ensuring that:
  • Energy transfers between volume elements counterbalance perfectly.
  • Net energy flow across system boundaries results in zero change within the domain.
Thus, even with certain simplifying assumptions, energy conservation can still be faithfully respected using accurate numerical techniques like the finite difference method.
Numerical Approximation
Numerical approximation refers to using mathematical techniques to find approximate solutions to complex equations or models. In thermal engineering, exact solutions to heat conduction problems may not always be feasible due to irregular shapes or complex boundary conditions.

The finite difference method is one such numerical approximation technique. It involves discretizing the domain into a grid and approximating derivatives by finite differences. This method translates continuous equations like the heat equation into a set of algebraic equations that can be solved with a computer.
  • Discrepancies between assumptions made for calculation ease and real-world conditions are minimized through convergence checks.
  • Accurate solutions can be achieved by refining the grid or improving algorithms.
This allows engineers and scientists to still achieve highly accurate simulations of heat conduction, making numerical methods invaluable for designing and analyzing thermal systems.

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Most popular questions from this chapter

A hot brass plate is having its upper surface cooled by impinging jet of air at temperature of \(15^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(220 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The 10 -cm-thick brass plate \(\left(\rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\), and \(\alpha=33.9 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) had a uniform initial temperature of \(650^{\circ} \mathrm{C}\), and the lower surface of the plate is insulated. Using a uniform nodal spacing of \(\Delta x=2.5 \mathrm{~cm}\) and time step of \(\Delta t=10 \mathrm{~s}\) determine \((a)\) the implicit finite difference equations and \((b)\) the nodal temperatures of the brass plate after 10 seconds of cooling.

How can a node on an insulated boundary be treated as an interior node in the finite difference formulation of a plane wall? Explain.

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.

Using EES (or other) software, solve these systems of algebraic equations. (a) $$ \begin{array}{r} 3 x_{1}-x_{2}+3 x_{3}=0 \\ -x_{1}+2 x_{2}+x_{3}=3 \\ 2 x_{1}-x_{2}-x_{3}=2 \end{array} $$ (b) $$ \begin{aligned} 4 x_{1}-2 x_{2}^{2}+0.5 x_{3} &=-2 \\ x_{1}^{3}-x_{2}+x_{3} &=11.964 \\ x_{1}+x_{2}+x_{3} &=3 \end{aligned} $$

Consider a 2-m-long and 0.7-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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