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Consider a medium in which the finite difference formulation of a general interior node is given in its simplest form as $$ \frac{T_{m-1}-2 T_{m}+T_{m+1}}{\Delta x^{2}}+\frac{\dot{e}_{m}}{k}=0 $$ (a) Is heat transfer in this medium steady or transient? (b) Is heat transfer one-, two-, or three-dimensional? (c) Is there heat generation in the medium? (d) Is the nodal spacing constant or variable? (e) Is the thermal conductivity of the medium constant or variable?

Short Answer

Expert verified
#Answer# The heat transfer in this medium is steady.

Step by step solution

01

Question (a)

Is heat transfer in this medium steady or transient? The given finite difference formulation is: $$ \frac{T_{m-1}-2 T_{m}+T_{m+1}}{\Delta x^{2}}+\frac{\dot{e}_{m}}{k}=0 $$ To determine whether the heat transfer is steady or transient, we should look for any time dependency within the equation. In this formulation, there is no term containing any time variable, and the temperatures are not time-dependent. Therefore, we can conclude that the heat transfer in this medium is steady.
02

Question (b)

Is heat transfer one-, two-, or three-dimensional? When we consider the heat transfer dimensions, we should inspect whether there are terms corresponding to each direction (x, y, and z). The given equation is only given in terms of x-direction (\(\Delta x\)). There are no y or z terms. Hence, we can deduce that the heat transfer in this medium is one-dimensional.
03

Question (c)

Is there heat generation in the medium? In this finite difference formulation, the term \(\frac{\dot{e}_{m}}{k}\) represents the heat generation rate per unit volume (\(\dot{e}_m\)) in the medium, divided by the thermal conductivity (k). If there were no heat generation in the medium, this term would be absent or equal to zero. However, since the term is present in the equation, we can infer that there is heat generation in the medium.
04

Question (d)

Is the nodal spacing constant or variable? To determine if nodal spacing is constant or variable, we should examine the denominator of the first term in the equation, which is \(\Delta x^2\). In this equation, the nodal spacing is only represented by \(\Delta x\), and no other variable is present in the denominator. Since there is no dependency on other variables or indexes, we can conclude that the nodal spacing is constant.
05

Question (e)

Is the thermal conductivity of the medium constant or variable? The thermal conductivity of the medium is represented by the symbol "k" in the equation. If the thermal conductivity were variable, it would typically be denoted with a subscript (e.g., \(k_m\)) or as a function of temperature or position (e.g., \(k(T)\) or \(k(x)\)). However, in this equation, the thermal conductivity is denoted simply as "k" without any further specifications. Thus, we can conclude that the thermal conductivity of the medium is constant.

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Most popular questions from this chapter

Starting with an energy balance on a volume element, obtain the steady two- dimensional finite difference equation for a general interior node in rectangular coordinates for \(T(x, y)\) for the case of variable thermal conductivity and uniform heat generation.

A hot surface at \(100^{\circ} \mathrm{C}\) is to be cooled by attaching \(3-\mathrm{cm}-\) long, \(0.25-\mathrm{cm}\)-diameter aluminum pin fins $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ with a center-to-center distance of \(0.6 \mathrm{~cm}\). The temperature of the surrounding medium is \(30^{\circ} \mathrm{C}\), and the combined heat transfer coefficient on the surfaces is \(35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming steady one-dimensional heat transfer along the fin and taking the nodal spacing to be \(0.5 \mathrm{~cm}\), determine \((a)\) the finite difference formulation of this problem, \((b)\) the nodal temperatures along the fin by solving these equations, \((c)\) the rate of heat transfer from a single fin, and \((d)\) the rate of heat transfer from a \(1-\mathrm{m} \times 1-\mathrm{m}\) section of the plate.

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 the Gauss- Seidel iteration method.

A composite wall is made of stainless steel $\left(k_{1}=13 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \quad 30 \mathrm{~mm}\right.$ thick), concrete $\left(k_{2}=1.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 30 \mathrm{~mm}\right.\( thick \))\(, and nonmetal \)\left(k_{3}=0.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, \)15 \mathrm{~mm}$ thick) plates. The concrete plate is sandwiched between the stainless steel plate at the bottom and the nonmetal plate at the top. A series of ASTM B21 naval brass bolts are bolted to the nonmetal plate, and the upper surface of the plate is exposed to convection heat transfer with air at \(20^{\circ} \mathrm{C}\) and $h=20 \mathrm{~W} / \mathrm{m}^{2}$.K. At the bottom surface, the stainless steel plate is subjected to a uniform heat flux of $2000 \mathrm{~W} / \mathrm{m}^{2}$. The ASME Code for Process Piping (ASME B31.3-2014, Table A-2M) limits the maximum use temperature for the ASTM B21 bolts to \(149^{\circ} \mathrm{C}\). Using the finite difference method with a uniform nodal spacing of \(\Delta x_{1}=10 \mathrm{~mm}\) for the stainless steel and concrete plates, and \(\Delta x_{2}=5 \mathrm{~mm}\) for the nonmetal plate, determine the temperature at each node. Plot the temperature distribution as a function of \(x\) along the plate thicknesses. Would the ASTM B21 bolts in the nonmetal plate comply with the ASME code?

Design a defrosting plate to speed up defrosting of flat food items such as frozen steaks and packaged vegetables, and evaluate its performance using the finite difference method. Compare your design to the defrosting plates currently available on the market. The plate must perform well, and it must be suitable for purchase and use as a household utensil, durable, easy to clean, easy to manufacture, and affordable. The frozen food is expected to be at an initial temperature of \(-18^{\circ} \mathrm{C}\) at the beginning of the thawing process and \(0^{\circ} \mathrm{C}\) at the end with all the ice melted. Specify the material, shape, size, and thickness of the proposed plate. Justify your recommendations by calculations. Take the ambient and surrounding surface temperatures to be \(20^{\circ} \mathrm{C}\) and the convection heat transfer coefficient to be \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) in your analysis. For a typical case, determine the defrosting time with and without the plate.

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