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The top surface of a plate, including its grooves, is maintained at a uniform temperature of \(T_{1}=200^{\circ} \mathrm{C}\). The lower surface is at \(T_{2}=20^{\circ} \mathrm{C}\), the thermal conductivity is \(15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and the groove spacing is \(0.16 \mathrm{~m}\). (a) Using a finite-difference method with a mesh size of \(\Delta x=\Delta y=40 \mathrm{~mm}\), calculate the unknown nodal temperatures and the heat transfer rate per width of groove spacing \((w)\) and per unit length normal to the page. (b) With a mesh size of \(\Delta x=\Delta y=10 \mathrm{~mm}\), repeat the foregoing calculations, determining the temperature field and the heat rate. Also, consider conditions for which the bottom surface is not at a uniform temperature \(T_{2}\) but is exposed to a fluid at \(T_{\infty}=20^{\circ} \mathrm{C}\). With \(\Delta x=\Delta y=10 \mathrm{~mm}\), determine the temperature field and heat rate for values of \(h=5,200\), and 1000 \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\), as well as for \(h \rightarrow \infty\).

Short Answer

Expert verified
In this problem, we use the finite-difference method to solve for nodal temperatures and heat transfer rates in two scenarios: (a) a mesh size of 40 mm and (b) a mesh size of 10 mm with varying heat transfer coefficients. By applying the two-dimensional conduction finite-difference equation, we iteratively solve for unknown nodal temperatures and calculate the heat transfer rate per width and per unit length in each case. In Part (b), we also consider the case when the bottom surface is exposed to a fluid and modify the boundary conditions accordingly.

Step by step solution

01

Part (a): Calculation of Nodal Temperatures with Mesh Size 40 mm

First, create a grid using the given mesh size(\( \Delta x = \Delta y = 40 \mathrm{~mm} \)). Next, apply the following finite-difference equation for conduction in two dimensions, at each node: \[ \frac{T_{i+1,j} - 2T_{i,j} + T_{i-1,j}}{\Delta x^2} + \frac{T_{i,j+1} - 2T_{i,j} + T_{i,j-1}}{\Delta y^2} = 0 \] Since \( \Delta x = \Delta y \), the equation can be simplified as follows: \[ T_{i+1,j}+T_{i-1,j}+T_{i,j+1}+T_{i,j-1}-4T_{i,j} = 0 \] Now substitute the known boundary and initial conditions, solve for the unknown nodal temperatures using a suitable numerical technique (e.g. Gauss-Seidel iteration) and calculate the heat transfer rate per width, w, and per unit length.
02

Part (b): Calculation of Nodal Temperatures with Mesh Size 10 mm

Create a new grid, using the given mesh size (\( \Delta x = \Delta y = 10 \mathrm{~mm} \)). Apply the finite-difference equation for conduction in two dimensions, as discussed in Part (a). Solve for the unknown nodal temperatures and calculate the heat transfer rate per width, w, and per unit length. Next, consider the additional condition for this part: the bottom surface is exposed to a fluid at \(T_{\infty}=20^{\circ} \mathrm{C}\). So the boundary condition at the bottom surface will be updated: \[ q_{i,1} = -k\left(\frac{T_{i,1}-T_{i,2}} {\Delta y}\right) = h(T_{i,1}-T_\infty) \] Now, solve the finite-difference equation with the updated boundary condition at the bottom surface for h = 5, 200, and 1000, and for \(h \rightarrow \infty\). Calculate the nodal temperatures and the heat transfer rate per width, w, and per unit length for each of these scenarios. Remember to use proper numerical techniques, like Gauss-Seidel iteration, to solve for the unknown nodal temperatures in both parts (a) and (b).

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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 mode of heat transfer within a body or between two bodies in direct contact. In this exercise, we're dealing with a plate that has different temperatures on its top and bottom surfaces. The heat will naturally flow from the hot surface at 200°C on the top to the cooler bottom surface at 20°C.

The thermal conductivity of the material, given as 15 W/m·K, is crucial as it dictates how easily heat flows through the material. Higher thermal conductivity means the material can conduct heat more effectively. In essence, a good conductor will allow heat to transfer quickly, while a poor conductor will resist the flow of heat.
  • The temperature gradient drives the heat flow, with heat moving from areas of high temperature to areas of low temperature.
  • The thermal conductivity is constant in this exercise, simplifying calculations as it does not vary with temperature.
Nodal Temperatures
Nodal temperatures are the unknown temperatures at specific points (nodes) within a domain. This exercise uses the finite-difference method to estimate these temperatures. We divide the plate into smaller sections using a grid, specifying node points at each intersect.

Using the finite-difference equations, we compute temperatures at these nodes. This approach converts the continuous problem of heat conduction into a discrete set of algebraic equations. By solving these equations, we find the temperatures at each node.
  • The method uses boundary conditions, such as the temperatures at the surfaces, to solve for internal node temperatures.
  • Nodes at the borders of the grid have known temperatures based on boundary conditions, simplifying calculations at these points.
  • Interior nodes are computed iteratively using techniques like Gauss-Seidel iteration, adjusting each node temperature until the system stabilizes to a solution.
Heat Transfer Rate
The heat transfer rate quantifies the amount of heat energy transferred per unit time. For this exercise, we look at the rate across a unit width of the groove spacing. This is calculated after establishing the nodal temperatures.

The rate of heat transfer can be computed using Fourier's Law of Heat Conduction, which states that the rate is proportional to the thermal conductivity, the area through which heat flows, and the temperature gradient.
  • For a flat plate, the typical process involves integrating over the domain, accounting for the conduction at each node.
  • Calculating the heat rate requires knowledge of each nodal temperature, ensuring the integration reflects gradients between adjacent nodes accurately.
  • The results tell us how much heat is being conducted through the material in a given direction.
Numerical Techniques
Numerical techniques play a crucial role in solving complex engineering problems like heat conduction described here. Unlike analytical solutions, numerical methods handle irregular geometries, variable properties, and complex boundary conditions effectively.

The finite-difference method, used in this problem, involves discretizing the domain into a grid of nodes, then applying difference equations to approximate derivatives. This replaces continuous partial differential equations with algebraic equations.
  • Techniques such as the Gauss-Seidel iteration simplify solving these equations by iteratively adjusting estimates of nodal temperatures until they converge to a stable solution.
  • This method is preferable in engineering applications since it allows flexibility in accommodating various boundary conditions and material properties.
  • Adjusting mesh sizes alters precision and computational resources needed; finer meshes like 10 mm offer more accuracy but require more computing power.

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Most popular questions from this chapter

Conduction within relatively complex geometries can sometimes be evaluated using the finite-difference methods of this text that are applied to subdomains and patched together. Consider the two-dimensional domain formed by rectangular and cylindrical subdomains patched at the common, dashed control surface. Note that, along the dashed control surface, temperatures in the two subdomains are identical and local conduction heat fluxes to the cylindrical subdomain are identical to local conduction heat fluxes from the rectangular subdomain. Calculate the heat transfer per unit depth into the page, \(q^{\prime}\), using \(\Delta x=\Delta y=\Delta r=10 \mathrm{~mm}\) and \(\Delta \phi=\pi / 8\). The base of the rectangular subdomain is held at \(T_{h}=20^{\circ} \mathrm{C}\), while the vertical surface of the cylindrical subdomain and the surface at outer radius \(r_{o}\) are at \(T_{c}=0^{\circ} \mathrm{C}\). The remaining surfaces are adiabatic, and the thermal conductivity is \(k=10 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

The elemental unit of an air heater consists of a long circular rod of diameter \(D\), which is encapsulated by a finned sleeve and in which thermal energy is generated by ohmic heating. The \(N\) fins of thickness \(t\) and length \(L\) are integrally fabricated with the square sleeve of width \(w\). Under steady-state operating conditions, the rate of thermal energy generation corresponds to the rate of heat transfer to airflow over the sleeve. (a) Under conditions for which a uniform surface temperature \(T_{s}\) is maintained around the circumference of the heater and the temperature \(T_{\infty}\) and convection coefficient \(h\) of the airflow are known, obtain an expression for the rate of heat transfer per unit length to the air. Evaluate the heat rate for \(T_{s}=300^{\circ} \mathrm{C}, D=20 \mathrm{~mm}\), an aluminum sleeve \(\left(k_{s}=240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right), w=40 \mathrm{~mm}\), \(N=16, t=4 \mathrm{~mm}, L=20 \mathrm{~mm}, T_{\infty}=50^{\circ} \mathrm{C}\), and \(h=500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (b) For the foregoing heat rate and a copper heater of thermal conductivity \(k_{h}=400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), what is the required volumetric heat generation within the heater and its corresponding centerline temperature? (c) With all other quantities unchanged, explore the effect of variations in the fin parameters \((N, L, t)\) on the heat rate, subject to the constraint that the fin thickness and the spacing between fins cannot be less than \(2 \mathrm{~mm}\).

A tube of diameter \(50 \mathrm{~mm}\) having a surface temperature of \(85^{\circ} \mathrm{C}\) is embedded in the center plane of a concrete slab \(0.1 \mathrm{~m}\) thick with upper and lower surfaces at \(20^{\circ} \mathrm{C}\). Using the appropriate tabulated relation for this configuration, find the shape factor. Determine the heat transfer rate per unit length of the tube.

For a small heat source attached to a large substrate, the spreading resistance associated with multidimensional conduction in the substrate may be approximated by the expression [Yovanovich, M. M., and V. W. Antonetti, in Adv. Thermal Modeling Elec. Comp. and Systems, Vol. 1, A. Bar-Cohen and A. D. Kraus, Eds., Hemisphere, \(\mathrm{NY}, 79-128,1988]\) \(R_{r(\mathrm{sp})}=\frac{1-1.410 A_{r}+0.344 A_{r}^{3}+0.043 A_{r}^{5}+0.034 A_{r}^{7}}{4 k_{\mathrm{sub}} A_{s, h}^{1 / 2}}\) where \(A_{r}=A_{s, h} / A_{s, \text { sub }}\) is the ratio of the heat source area to the substrate area. Consider application of the expression to an in- line array of square chips of width \(L_{h}=\) \(5 \mathrm{~mm}\) on a side and pitch \(S_{h}=10 \mathrm{~mm}\). The interface between the chips and a large substrate of thermal conductivity \(k_{\text {sub }}=80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is characterized by a thermal contact resistance of \(R_{t, c}^{\prime \prime}=0.5 \times 10^{-4} \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\). If a convection heat transfer coefficient of \(h=\) \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) is associated with airflow \(\left(T_{\infty}=15^{\circ} \mathrm{C}\right)\) over the chips and substrate, what is the maximum allowable chip power dissipation if the chip temperature is not to exceed \(T_{h}=85^{\circ} \mathrm{C}\) ?

Hot water is transported from a cogeneration power station to commercial and industrial users through steel pipes of diameter \(D=150 \mathrm{~mm}\), with each pipe centered in concrete \((k=1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) of square cross section \((w=300 \mathrm{~mm})\). The outer surfaces of the concrete are exposed to ambient air for which \(T_{\infty}=0^{\circ} \mathrm{C}\) and \(h=\) \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) If the inlet temperature of water flowing through the pipe is \(T_{i}=90^{\circ} \mathrm{C}\), what is the heat loss per unit length of pipe in proximity to the inlet? The temperature of the pipe \(T_{1}\) may be assumed to be that of the inlet water. (b) If the difference between the inlet and outlet temperatures of water flowing through a 100 -m-long pipe is not to exceed \(5^{\circ} \mathrm{C}\), estimate the minimum allowable flow rate \(\dot{m}\). A value of \(c=4207 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\) may be used for the specific heat of the water.

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