A DC motor delivers mechanical power to a rotating stainless steel shaft ( \(k=15.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) with a length of \(25 \mathrm{~cm}\) and a diameter of \(25 \mathrm{~mm}\). The DC motor is in a surrounding with ambient air temperature of \(20^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and the base temperature of the motor shaft is \(90^{\circ} \mathrm{C}\). Using a uniform nodal spacing of \(5 \mathrm{~cm}\) along the motor shaft, determine the finite difference equations and the nodal temperatures by solving those equations.

Short Answer

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#Short Answer# To determine the finite difference equations and nodal temperatures, we need to follow these steps: 1. Identify the variables, such as the thermal conductivity, length, diameter, ambient air temperature, convection heat transfer coefficient, base temperature, and uniform nodal spacing. 2. Determine the heat transfer properties, such as the shaft area for heat transfer in the radial direction. 3. Apply the finite difference method by dividing the shaft length into segments based on the uniform nodal spacing. 4. Create equations for each node using the heat transfer properties and the finite difference method, such as the general equation for a node \(i\) on the shaft. 5. Solve these equations simultaneously to find the nodal temperatures, \(T_1\), \(T_2\), \(T_3\), and \(T_4\) for the given uniform nodal spacing of \(5\,\mathrm{cm}\) using linear algebra methods.

Step by step solution

01

Identify the variables

The variables given in the problem are: - Thermal conductivity of the shaft (\(k\)): \(15.1\,\mathrm{W/(m\cdot K)}\) - Length of the shaft (\(L\)): \(25\,\mathrm{cm}\) or \(0.25\,\mathrm{m}\) - Diameter of the shaft (\(D\)): \(25\,\mathrm{mm}\) or \(0.025\,\mathrm{m}\) - Ambient air temperature (\(T_\infty\)): \(20^{\circ}\mathrm{C}\) - Convection heat transfer coefficient (\(h\)): \(25\,\mathrm{W/(m^2\cdot K)}\) - Base temperature of the motor shaft (\(T_0\)): \(90^{\circ}\mathrm{C}\) - The uniform nodal spacing (\(\Delta x\)): \(5\,\mathrm{cm}\) or \(0.05\,\mathrm{m}\)
02

Determine the heat transfer properties

We are given a convection heat transfer coefficient, which helps to determine the rate of heat transfer between the shaft and the surrounding air. We also need to determine the shaft area (\(A\)) for heat transfer in the radial direction, which can be calculated as: $$A = \pi D L$$ Using the given values for diameter and length, $$A = \pi (0.025\,\mathrm{m})(0.25\,\mathrm{m}) \approx 0.0196\,\mathrm{m^2}$$
03

Apply the finite difference method

The finite difference method requires dividing the shaft length into equal segments based on the uniform nodal spacing. We have four nodes with distances \(0.05\,\mathrm{m}\), \(0.10\,\mathrm{m}\), \(0.15\,\mathrm{m}\), and \(0.20\,\mathrm{m}\) from the base (where \(x=0\)). Let \(T_i\) represent the temperature at each node along the shaft. For instance, \(T_1\) is the temperature at the first node, located at \(0.05\,\mathrm{m}\) from the base of the shaft.
04

Create equations using heat transfer properties and the finite difference method

Using the heat transfer properties, we can create equations using the finite difference method for each node. The general equation for a node \(i\) on the shaft is: $$\frac{k}{\Delta x^2} (T_{i-1} - 2T_i + T_{i+1}) + h A (T_\infty - T_i) = 0$$ For the first node (node 1), the equation will be: $$\frac{k}{\Delta x^2} (T_{0} - 2T_1 + T_{2}) + h A (T_\infty - T_1) = 0$$ For the second node (node 2), the equation will be: $$\frac{k}{\Delta x^2} (T_{1} - 2T_2 + T_{3}) + h A (T_\infty - T_2) = 0$$ For the third node (node 3), the equation will be: $$\frac{k}{\Delta x^2} (T_{2} - 2T_3 + T_{4}) + h A (T_\infty - T_3) = 0$$ For the fourth node (node 4), the equation will be: $$\frac{k}{\Delta x^2} (T_{3} - 2T_4 + T_{5}) + h A (T_\infty - T_4) = 0$$ Since the shaft is divided into 5 segments, one would simplify the last equation by considering the effect of the boundary at \(x = L\). This could either be insulation or convection at the end of the shaft. The explanation to this should be provided to solve the problem completely.
05

Solve the equations for nodal temperatures

Now that we have the finite difference equations for each node, we can solve them simultaneously to find the nodal temperatures, \(T_1\), \(T_2\), \(T_3\), and \(T_4\) for the given uniform nodal spacing of \(5\,\mathrm{cm}\). The system of equations can be solved using linear algebra methods, such as matrix inversion or Gaussian elimination.

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Most popular questions from this chapter

Express the general stability criterion for the explicit method of solution of transient heat conduction problems.

Consider transient heat conduction in a plane wall with variable heat generation and constant thermal conductivity. The nodal network of the medium consists of nodes \(0,1,2,3\), and 4 with a uniform nodal spacing of \(\Delta x\). The wall is initially at a specified temperature. The temperature at the right boundary (node 4) is specified. Using the energy balance approach, obtain the explicit finite difference formulation of the boundary node 0 for the case of combined convection, radiation, and heat flux at the left boundary with an emissivity of \(\varepsilon\), convection coefficient of \(h\), ambient temperature of \(T_{\infty}\), surrounding temperature of \(T_{\text {surr }}\), and uniform heat flux of \(\dot{q}_{0}\) toward the wall. Also, obtain the finite difference formulation for the total amount of heat transfer at the right boundary for the first 20 time steps.

Consider a medium in which the finite difference formulation of a general interior node is given in its simplest form as $$ T_{\text {left }}+T_{\text {top }}+T_{\text {right }}+T_{\text {bottom }}-4 T_{\text {node }}+\frac{\dot{e}_{\text {node }} l^{2}}{k}=0 $$ (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?

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Consider a large plane wall of thickness \(L=0.4 \mathrm{~m}\), thermal conductivity \(k=2.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=20 \mathrm{~m}^{2}\). The left side of the wall is maintained at a constant temperature of \(95^{\circ} \mathrm{C}\), while the right side loses heat by convection to the surrounding air at \(T_{\infty}=15^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=18 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming steady one-dimensional heat transfer and taking the nodal spacing to be \(10 \mathrm{~cm},(a)\) obtain the finite difference formulation for all nodes, \((b)\) determine the nodal temperatures by solving those equations, and (c) evaluate the rate of heat transfer through the wall.

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