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The unsteady forward-difference heat conduction for a constant-area \((A)\) pin fin with perimeter \(p\), when exposed to air whose temperature is \(T_{0}\) with a convection heat transfer coefficient of \(h\), is $$ \begin{aligned} T_{m}^{*+1}=& \frac{k}{\rho c_{p} \Delta x^{2}}\left[T_{m-1}^{*}+T_{m+1}^{*}+\frac{h p \Delta x^{2}}{A} T_{0}\right] \\\ &-\left[1-\frac{2 k}{\rho c_{p} \Delta x^{2}}-\frac{h p}{\rho c_{p} A}\right] T_{m}^{*} \end{aligned} $$ In order for this equation to produce a stable solution, the quantity $\frac{2 k}{\rho c_{p} \Delta x^{2}}+\frac{h p}{\rho c_{p} A}$ must be (a) negative (b) zero (c) positive (d) greater than 1 (e) less than 1

Short Answer

Expert verified
Answer: The stability condition for the given equation is that the sum of the terms (S) must be positive and less than 1 (option e).

Step by step solution

01

Identify given equation and terms

The given equation is: $$ T_{m}^{*+1} = \frac{k}{\rho c_{p} \Delta x^{2}}\left[T_{m-1}^{*}+T_{m+1}^{*}+\frac{h p \Delta x^{2}}{A} T_{0}\right] -\left[1-\frac{2 k}{\rho c_{p} \Delta x^{2}}-\frac{h p}{\rho c_{p} A}\right] T_{m}^{*} $$ where - \(T_m^*\) represents the temperature at location \(m\) and time \(t^*\), - \(\rho\), \(c_p\), \(k\) are the material properties (density, specific heat, and thermal conductivity, respectively), - \(\Delta x\) is the spatial step size, - \(h\) is the convection heat transfer coefficient, - \(p\) is the perimeter of the pin fin, and - \(A\) is the constant-area of the pin fin. The stability condition is related to the sum of the following two terms: $$ \frac{2k}{\rho c_p \Delta x^2} + \frac{hp}{\rho c_p A} $$
02

Simplify and compute the sum of the terms

Let's simplify the sum of the terms given and compute its value: $$ S = \frac{2k}{\rho c_p \Delta x^2} + \frac{hp}{\rho c_p A} $$ Factor out common terms: $$ S = \frac{2k + hp\Delta x^2 / A}{\rho c_p \Delta x^2} $$ Now, we need to determine the condition for stability.
03

Evaluate the stability condition

To produce a stable solution, we must find whether the sum of these terms \(S\) fulfills one of the following conditions: (a) negative (b) zero (c) positive (d) greater than 1 (e) less than 1 Notice that \(2k\), \(hp\Delta x^2 / A\), \(\rho\), and \(c_p \Delta x^2\) are all positive since they represent physical properties and steps. Thus, the sum \(S\) must be positive as the sum of positive terms. Therefore, the only possible conditions are (c), (d), or (e). It tells us that condition (a) and (b) are incorrect.
04

Eliminate remaining options

We have left options (c), (d), and (e). Since all terms in the denominator and numerator are positive, that means that the sum must be greater than 0. So, it is not zero, nor can it be negative. Now, let's look at the term within the brackets of the given equation: $$ 1 - \frac{2k}{\rho c_p \Delta x^2} - \frac{hp}{\rho c_p A} $$ In order to produce a stable solution, this term must be positive if the given equation converges to correct values. So, given that \(1 > \frac{2k}{\rho c_p \Delta x^2} + \frac{hp}{\rho c_p A}\), it's clear that the sum must be less than 1. From above, the sum \(S\) is positive and less than 1. This leads us to the conclusion that the stability condition is given by option (e), less than 1.

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Most popular questions from this chapter

What are the basic steps involved in solving a system of equations with the Gauss-Seidel method?

Write a two-page essay on the finite element method, and explain why it is used in most commercial engineering software packages. Also explain how it compares to the finite difference method.

A circular fin of uniform cross section, with diameter of \(10 \mathrm{~mm}\) and length of \(50 \mathrm{~mm}\), is attached to a wall with a surface temperature of \(350^{\circ} \mathrm{C}\). The fin is made of material with thermal conductivity of \(240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), it is exposed to an ambient air condition of \(25^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is \(250 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\). Assume steady one-dimensional heat transfer along the fin and the nodal spacing to be uniformly \(10 \mathrm{~mm}\). (a) Using the energy balance approach, obtain the finite difference equations to determine the nodal temperatures. (b) Determine the nodal temperatures along the fin by solving those equations, and compare the results with the analytical solution. (c) Calculate the heat transfer rate, and compare the result with the analytical solution.

Solar radiation incident on a large body of clean water $\left(k=0.61 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\( and \)\left.\alpha=0.15 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)$ such as a lake, a river, or a pond is mostly absorbed by water, and the amount of absorption varies with depth. For solar radiation incident at a \(45^{\circ}\) angle on a \(1-\mathrm{m}\)-deep large pond whose bottom surface is black (zero reflectivity), for example, \(2.8\) percent of the solar energy is reflected back to the atmosphere, \(37.9\) percent is absorbed by the bottom surface, and the remaining \(59.3\) percent is absorbed by the water body. If the pond is considered to be four layers of equal thickness \((0.25 \mathrm{~m}\) in this case), it can be shown that \(47.3\) percent of the incident solar energy is absorbed by the top layer, \(6.1\) percent by the upper mid layer, \(3.6\) percent by the lower mid layer, and 2.4 percent by the bottom layer [for more information, see Cengel and Ozi?ik, Solar Energy, 33, no. 6 (1984), pp. 581-591]. The radiation absorbed by the water can be treated conveniently as heat generation in the heat transfer analysis of the pond. Consider a large \(1-\mathrm{m}\)-deep pond that is initially at a uniform temperature of \(15^{\circ} \mathrm{C}\) throughout. Solar energy is incident on the pond surface at \(45^{\circ}\) at an average rate of $500 \mathrm{~W} / \mathrm{m}^{2}$ for a period of 4 h. Assuming no convection currents in the water and using the explicit finite difference method with a mesh size of \(\Delta x=0.25 \mathrm{~m}\) and a time step of \(\Delta t=15 \mathrm{~min}\), determine the temperature distribution in the pond under the most favorable conditions (i.e., no heat losses from the top or bottom surfaces of the pond). The solar energy absorbed by the bottom surface of the pond can be treated as a heat flux to the water at that surface in this case.

The roof of a house consists of a \(15-\mathrm{cm}\)-thick concrete slab \(\left(k=1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\) and \(\left.\alpha=0.69 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\) that is \(18 \mathrm{~m}\) wide and \(32 \mathrm{~m}\) long. One evening at $6 \mathrm{p} . \mathrm{m}$., the slab is observed to be at a uniform temperature of \(18^{\circ} \mathrm{C}\). The average ambient air and the night sky temperatures for the entire night are predicted to be \(6^{\circ} \mathrm{C}\) and \(260 \mathrm{~K}\), respectively. The convection heat transfer coefficients at the inner and outer surfaces of the roof can be taken to be $h_{i}=5 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\( and \)h_{o}=12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The house and the interior surfaces of the walls and the floor are maintained at a constant temperature of \(20^{\circ} \mathrm{C}\) during the night, and the emissivity of both surfaces of the concrete roof is \(0.9\). Considering both radiation and convection heat transfers and using the explicit finite difference method with a time step of \(\Delta t=5 \mathrm{~min}\) and a mesh size of $\Delta x=3 \mathrm{~cm}$, determine the temperatures of the inner and outer surfaces of the roof at 6 a.m. Also, determine the average rate of heat transfer through the roof during that night.

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