/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 76 A plane wall of thickness \(2 L\... [FREE SOLUTION] | 91Ó°ÊÓ

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A plane wall of thickness \(2 L\) and thermal conductivity \(k\) experiences a uniform volumetric generation rate 4. As shown in the sketch for Case I. the surface at \(x=-L\) is perfectly insulated, while the other surface is maintained at a uniform, constant temperature \(T_{a}\). For Case 2, a very thin dielectric strip is inserted at the midpoint of the wall \((x=0)\) in order to electrically isolate the two sections, \(A\) and B. The thermal resistance of the strip is \(R_{7}^{*}=0.0005 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\). The parameters associated with the wall are \(k=50 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, L=20 \mathrm{~mm}\), \(q=5 \times 10^{6} \mathrm{~W} / \mathrm{m}^{3}\), and \(T_{e}=50^{\circ} \mathrm{C}\). (a) Sketch the temperature distribution for case I on \(T-x\) coordinates. Deseribe the key features of this distribution. Identify the location of the maxirmum temperature in the wall and calculate this temperature. (b) Sketch the temperature distribution for Cuse 2 on the same \(T-x\) coordinates. Describe the key features of this distribution. (c) What is the temperature difference between the two walls at \(x=0\) for Case 2? (d) What is the location of the maximum temperature in the composite wall of Case 2? Calculate this temperature.

Short Answer

Expert verified
Maximum temperature is 64°C for Case 1. In Case 2, maximum temperature is slightly higher by 2.5°C near x=0.

Step by step solution

01

Understand the problem statement

We need to solve for temperature distributions in a plane wall with uniform heat generation. For Case 1, there's no heat conduction at one boundary, and for Case 2, a thermal resistance is introduced at the midpoint (x=0) of the wall. We need to plot temperature distributions, find maximum temperature, and compute temperature differences between sections in both cases.
02

Sketch the temperature distribution for Case 1

For Case 1, the heat equation for a plane wall with volumetric generation is \[ T(x) = -\frac{q}{2k}x^2 + C_1x + C_2 \]where C_1 and C_2 are integration constants. With the boundary conditions: insulated surface at \(x = -L\) and \(T = T_a\) at \(x = L\), we can determine C_1 and C_2 by applying these conditions.The insulated boundary gives:\[\frac{dT}{dx}\Big|_{x=-L} = 0\]and\[ T(L) = T_a\]
03

Calculate integration constants for Case 1

Using the insulated boundary condition, we find:\[\frac{dT}{dx} = -\frac{q}{k}x + C_1 = 0 \quad \Rightarrow \quad C_1 = \frac{qL}{k}\]Substituting into the temperature profile equation and using \(T(L) = T_a\):\[T(L) = -\frac{q}{2k}L^2 + \frac{qL^2}{k} + C_2 = T_a \quad \Rightarrow \quad C_2 = T_a - \frac{q}{2k}L^2\]
04

Maximum temperature location and value in Case 1

The location of the maximum temperature is at \(x = 0\) due to symmetry and the parabolic nature of the temperature profile. Substituting \(x = 0\) back:\[ T_{max} = C_2 = T_a - \frac{q}{2k}L^2\]Plugging in the given values:\[ T_{max} = 50 - \frac{5 \times 10^6 \times (0.02)^2}{2 \times 50} = 64^\circ C\]
05

Sketch temperature distribution for Case 2

For Case 2, we have an additional thermal resistance at the midpoint. This divides the wall into two sections, each having its heat generation and distinct temperature profiles, influenced by the thermal resistance:\[T_{1}(x) = -\frac{q}{2k}x^2 + C_3x + C_4\]\[T_{2}(x) = -\frac{q}{2k}x^2 + C_5x + C_6\]
06

Boundary conditions to find constants for Case 2

Using the continuity of heat flux and temperature at \(x = 0\):\[-k \frac{dT_{1}}{dx}\Big|_{x=0} = -k \frac{dT_{2}}{dx}\Big|_{x=0}\]and the condition across the thermal resistance:\[T_{1}(0) - T_{2}(0) = q R^{*}\]
07

Maximum temperature and its location for Case 2

Considering two symmetrical sections and continuous insulation effects, maximum temperature still occurs at the center of each section (near \(x = 0\) but influenced by the thermal resistance). The calculations simplify to show that maximum temperature increases slightly due to the resistance:\[ T_{max} = (T_{max \, \text{without} \, R^{*} }) + \frac{q R^{*}}{k}\]Substitute the known values and solve for Case 2 specifics.
08

Calculate temperature difference across the dielectric strip

The temperature difference across the strip at \(x=0\) is given by:\[ \Delta T = q R^{*}\]Substitute the known value for \(R^{*}\):\[ \Delta T = 5 \times 10^6 \times 0.0005 = 2.5^\circ C\]

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Key Concepts

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

Thermal Conductivity
Thermal conductivity is a material property that measures a material's ability to conduct heat. It is essential in calculating how heat spreads through a material. Imagine holding a metal rod in your hand. If you heat one end, you'll soon feel the warmth at the other end due to the rod's thermal conductivity.
In this exercise, thermal conductivity (\(k\)) is crucial for determining the heat's journey through the plane wall. With \(k = 50 \, \text{W/m}\cdot\text{K}\), this tells us that for every meter of wall thickness, and for each degree of temperature difference, 50 watts of heat passes through. It reflects how efficiently the wall passes heat from a hotter region to a cooler one.
  • This factor directly influences the temperature distribution within the wall.
  • The higher the thermal conductivity, the faster the heat can flow through the material.
  • Application of boundary conditions will determine specific heat flow paths.
Understanding thermal conductivity helps predict how long it will take for heat to reach different parts of the wall and how efficiently it moves. Essentially, it determines the relationship between temperature gradients (how fast temperature changes in space) and heat flux (the rate of heat flow).
Temperature Distribution
Temperature distribution describes how temperature varies within a given system, like a wall, over space. In Case 1, temperature changes in the wall follow a particular pattern or profile because the left boundary is insulated, and the right boundary is kept at a constant temperature \(T_a\).
The pattern or distribution often depends on factors like heat generation, thermal conductivity, and other boundary conditions. For Case 1, the temperature along the wall follows a parabolic shape, based on the equation:\[T(x) = -\frac{q}{2k}x^2 + C_1x + C_2\]Understanding the temperature distribution is vital because it helps locate the maximum and minimum temperatures within the wall. This is particularly important for materials that might degrade or fail under extreme temperatures.
  • In Case 1, maximum temperature occurs around the center of the wall due to symmetry.
  • In Case 2, the introduction of a thermal resistance changes the distribution, causing a slight increase in maximum temperature.
  • Profiles are affected by the volumetric heat generation (\(q\)) within the wall.
Temperature distribution is crucial for designing systems that efficiently manage heat to avoid hotspots that can lead to material failure.
Boundary Conditions
Boundary conditions are specific constraints or conditions at the boundaries of a material or system that must be satisfied for an accurate solution to a heat transfer problem.
Think of them as the rules that govern how heat interacts at the edges of the wall. In our exercise, Case 1 has two boundaries:
  • At \(x = -L\), the surface is perfectly insulated, meaning no heat passes through this boundary. This condition leads to \(\frac{dT}{dx} = 0\) at \(x = -L\)
  • At \(x = L\), the surface is maintained at a constant temperature \(T_a\)
These conditions allow us to solve for the constants in the heat equation, defining how temperature varies throughout the wall.
For Case 2, additional boundary conditions come into play due to the dielectric strip at \(x=0\). Here, continuity of temperature and heat flux is required:
  • Temperatures on either side of the strip need to fulfill the condition \(T_{1}(0) - T_{2}(0) = q R^{*}\)
  • Heat flux should be consistent across the strip.
Correctly setting these boundary conditions is essential because they ground the mathematical model in physical reality, leading to accurate predictions of how temperature changes across the wall.

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Most popular questions from this chapter

A spherical vessel used as a reactor for producing pharmaceuticals has a 10 -mam-thick stainless steel wall \((k=\) \(17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) and an inner diameter of \(1 \mathrm{~m}\). The exteria surface of the vessel is exposed to ambient air \(\left(T_{z}=\right.\) \(25^{\circ} \mathrm{C}\) ) for which a convection coefficient of \(6 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\) may be assumed. (a) During steady-state operation, an inner surfact temperature of \(50^{\circ} \mathrm{C}\) is maintained by enengy geneated within the reactor. What is the heat loss from the vessel? (b) If a 20-mm-thick layer of fiberglass insulation \((k=\) \(0.040 \mathrm{~W} / \mathrm{m}\) - K) is applied to the exterior of the ve sel and the rate of thermal energy generation is inchanged, what is the inner surface temperature of the vessel?

The rear window of an automobile is defogged by attaching a thin, transparent, film-type heating clement to its inner surface. By electrically heating this element, a uniform heat flux may be established at the inner surface. (a) For 4-mm-thick window glass, determine the electrical power required per unit window area to maintain an inner surface temperature of \(15^{\circ} \mathrm{C}\) when the interior air temperature and convection cocfficient are \(T_{=i}=25^{\circ} \mathrm{C}\) and \(h_{i}=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the exterior (ambient) air temperature and convection coefficient are \(T_{\text {we }}=\) \(-10^{\circ} \mathrm{C}\) and \(h_{e}=65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (b) In practice \(T_{w e}\) and \(h_{y}\) vary according to weather conditions and car speed. For values of \(h_{\mathrm{m}}=2,20,65\), and \(100 \mathrm{~W} / \mathrm{m}^{2}-\mathrm{K}\), determine and plot the electrical power requirement as a function of \(T_{z,}\) for \(-30 \leq T_{x p} \leq\) \(0^{\circ} \mathrm{C}\). From your results, what can you conclude about the need for heater operation at low values of \(h_{e}\) ? How is this conclusion affected by the value of \(T_{\text {w, }, 0}\) ? If \(h \propto\) \(V^{*}\), where \(V\) is the vehicle speed and \(n\) is a positive exponent, how does the vehicle speed affect the need for heater eperation?

An electrical current of 700 A flows through a stainless steel cable having a diameter of \(5 \mathrm{~mm}\) and an electrical resistance of \(6 \times 10^{-4} \mathrm{\Omega} / \mathrm{m}\) (i.e., per meter of cable length). The cable is in environment having a temperature of \(30^{\circ} \mathrm{C}\), and the total coefficient associated with convection and radiation between the cable and the environment is approximately \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) If the cable is bare, what is its surface temperature? (b) If a very thin coating of electrical insulation is applied to the cable, with a contact resistance of \(0.02 \mathrm{~m}^{2}+\mathrm{K} / \mathrm{W}\), what are the insulation and cable surface temperatures? (c) There is some concern about the ability of the insulation to withstand elevated temperatures. What thickness of this insulation \((k=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) will yield the lowest value of the maximum insulation temperature? What is the valie of the maximum temperature when the thickness is used?

In a manufacturing process, as transparent film is being bonded to a substrate as shown in the sketch. To cure the bond at a temperature \(T_{\text {ty }}\) a radiant source is used to provide a heat flux \(q_{i}^{\pi}\left(\mathrm{W} / \mathrm{m}^{2}\right)\), all of which is absorbed at the bonded surface. The back of the substrate is maintained at \(T_{1}\) while the free surface of the film is exposed to air at \(T_{m}\) and a convection heat transfer coefficient \(h\). (a) Show the thermal circuit representing the steady-state heat transfer situation, Be sure to label all elements, nodes, and heat rates. Leave in symbolic form. (b) Assume the following conditions: \(T_{w}=20^{\circ} \mathrm{C}, h=\) \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}_{\text {, }}\) and \(T_{1}=30^{\circ} \mathrm{C}\). Calculate the heat flux \(q_{0}^{\prime}\) that is required to maintain the bonded surface at \(T_{0}=60^{\circ} \mathrm{C}\). (c) Compute and plot the required heat flux as a function of the film thickness for \(0 \leq L_{y} \leq 1 \mathrm{~mm}\). (d) If the film is not transparent and all of the radiant heat flux is absorbed at its upper surface, determine the heat flux required to achieve bonding. Plot your results as a function of \(L_{f}\) for \(0 \leq L_{f} \leq 1 \mathrm{~mm}\).

The energy transferred from the anterior chamber of the eye through the cornea varies considerably depending on whether a contact lens is worm. Treat the eye as a splerical system and assume the system to be at steady state. The convection coefficient \(h_{e}\) is unchanged with and without the contact lens in place. The cornea and the lens cover one-third of the spherical surface area. Values of the parameters representing this situation are as follows: \(\begin{array}{ll}r_{1}=10.2 \mathrm{~mm} & r_{2}=12.7 \mathrm{~mm} \\\ r_{3}=16.5 \mathrm{~mm} & T_{-a}=21^{\circ} \mathrm{C} \\ T_{s 1}=37^{\circ} \mathrm{C} & k_{2}=0.80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\\ k_{1}=0.35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} & h_{n}=6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \\ h_{4}=12 \mathrm{~W} / \mathrm{m}^{2}-\mathrm{K} & \end{array}\) (a) Construct the thermal circuits, labeling all potentials and flows for the systems excluding the contact lens and including the contact lens. Write resistance elements in terms of appropriate parameters. (b) Determine the heat loss from the anterior chamber with and without the contact lens in place. (c) Discuss the implication of your results.

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