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Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=\) \(12 \mathrm{~m}^{2}\). The left side of the wall at \(x=0\) is subjected to a net heat flux of \(\dot{q}_{0}=700 \mathrm{~W} / \mathrm{m}^{2}\) while the temperature at that surface is measured to be \(T_{1}=80^{\circ} \mathrm{C}\). Assuming constant thermal conductivity and no heat generation in the wall, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and \((c)\) evaluate the temperature of the right surface of the wall at \(x=L\).

Short Answer

Expert verified
Question: Calculate the temperature at the right surface of a large plane wall with a steady one-dimensional heat conduction when its properties and conditions are given. Answer: The temperature at the right surface of the wall is 44°C.

Step by step solution

01

Write the governing equation for heat conduction

The governing equation for steady one-dimensional heat conduction with no heat generation is given by the following expression: \[\dfrac{d^2T}{dx^2} = 0\]
02

Write Fourier's Law of heat conduction

Fourier's law states the relationship between heat flux and the temperature gradient as follows: \[\dot{q} = -k \dfrac{dT}{dx}\]
03

Integrate the governing equation once

Integration of the governing equation (\(\dfrac{d^2T}{dx^2} = 0\)) with respect to x gives: \[\dfrac{dT}{dx} = C_{1}\] where \(C_{1}\) is the integration constant.
04

Apply the boundary condition at the left surface (x = 0)

At the left surface (\(x=0\)), the net heat flux \(\dot{q}_{0}\) and surface temperature \(T_{1}\) are given. Using Fourier's law, we can find the integration constant \(C_{1}\). \[\dot{q}_{0} = -k \dfrac{dT}{dx} |_{x=0} = -k C_{1} \Rightarrow C_{1} = -\dfrac{\dot{q}_{0}}{k}\]
05

Substitute the value of C1 into the equation for the temperature gradient

Substituting the calculated value of \(C_{1}\) into the equation for the temperature gradient, we have: \[\dfrac{dT}{dx} = -\dfrac{\dot{q}_{0}}{k}\]
06

Integrate the temperature gradient to obtain the temperature variation

Integration of the temperature gradient equation with respect to x gives the temperature variation: \[T(x) - T_{1} = -\dfrac{\dot{q}_{0}}{k}x + C_{2}\] Since the temperature at the left surface is \(T_{1}\), we have the boundary condition \(T(0) = T_{1}\). Applying this condition, we can find the value of \(C_{2}\) to be: \[C_{2} = 0\] So, the temperature variation in the wall can be expressed as: \[T(x) = T_{1} - \dfrac{\dot{q}_{0}}{k}x\]
07

Calculate the temperature at the right surface (x = L)

Now, we can evaluate the temperature at the right surface of the wall (\(x=L\)) using the temperature variation equation: \[T(L) = T_{1} - \dfrac{\dot{q}_{0}}{k}L\] Substitute the given values for \(T_{1}\), \(\dot{q}_{0}\), \(k\), and \(L\): \[T(L) = 80^{\circ} \mathrm{C} - \dfrac{700 \mathrm{~W} / \mathrm{m}^{2}}{2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}} \cdot 0.3 \mathrm{~m}\] Solve for \(T(L)\): \[T(L) = 44^{\circ} \mathrm{C}\] The temperature of the right surface of the wall at \(x=L\) is \(44^{\circ} \mathrm{C}\).

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Key Concepts

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

Fourier's Law
Fourier's Law is fundamental to understanding heat conduction. It describes how heat transfers through a material due to a temperature gradient. This law is expressed mathematically as: \[ \dot{q} = -k \dfrac{dT}{dx} \] Here, \( \dot{q} \) represents the heat flux, which is the rate of heat transfer per unit area. The minus sign indicates the direction of heat flow is opposite to the temperature gradient. The term \( k \) is the thermal conductivity of the material, indicating how well the material conducts heat, and \( \dfrac{dT}{dx} \) is the temperature gradient across the material. Understanding Fourier's Law is crucial because it forms the basis for determining how temperature changes within a material and helps in solving heat conduction problems.
Differential Equation
In the context of heat conduction, we encounter differential equations representing the mathematical model of how heat is distributed over a medium. For steady one-dimensional heat conduction with no heat generation, the governing differential equation is: \[\dfrac{d^2T}{dx^2} = 0 \] This equation signifies that the rate of change of the temperature gradient is zero, implying a linear temperature distribution within the material. To solve for temperature variation, this second-order differential equation is integrated step-by-step. The first integration gives the temperature gradient as a constant: \[ \dfrac{dT}{dx} = C_1 \] Where \( C_1 \) is an integration constant determined by applying boundary conditions.
Boundary Conditions
Boundary conditions are essential for solving differential equations in physical systems. They provide additional information to find unknown constants and ensure the solution is physically meaningful. In heat conduction problems, boundary conditions can specify temperatures or heat flux at the boundaries of the material. For the given plane wall, the boundary conditions include the net heat flux \( \dot{q}_0 = 700 \mathrm{~W/m}^2 \) and the temperature at the left surface \( x=0 \) is \( T_1 = 80^{\circ}\mathrm{C} \). These conditions help in determining the constants in the integrated equation for temperature distribution, allowing the correct description of the temperature variation within the wall.
Temperature Distribution
The temperature distribution is the expression showing how temperature changes with position within a material. It is derived by integrating the differential equation and applying boundary conditions. For the steady-state one-dimensional heat conduction we are examining, the temperature distribution is given by: \[ T(x) = T_1 - \dfrac{\dot{q}_0}{k} x \] This equation shows a linear relationship between temperature \( T \) and the position \( x \) in the material. The slope of this line (\( -\dfrac{\dot{q}_0}{k} \)) is a result of the constant heat flux and characteristic of the material's thermal conductivity. By evaluating this equation at different positions, such as \( x=L \), we can determine the temperature at specific points within the wall, like at its right surface in the original problem, where it was solved to be \(44^{\circ}\mathrm{C}\).

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Most popular questions from this chapter

Consider steady one-dimensional heat conduction in a plane wall in which the thermal conductivity varies linearly. The error involved in heat transfer calculations by assuming constant thermal conductivity at the average temperature is \((a)\) none, \((b)\) small, or \((c)\) significant.

Consider a spherical reactor of \(5-\mathrm{cm}\) diameter operating at steady condition has a temperature variation that can be expressed in the form of \(T(r)=a-b r^{2}\), where \(a=850^{\circ} \mathrm{C}\) and \(b=5 \times 10^{5} \mathrm{~K} / \mathrm{m}^{2}\). The reactor is made of material with \(c=\) \(200 \mathrm{~J} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, k=40 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=9000 \mathrm{~kg} / \mathrm{m}^{3}\). If the heat generation of reactor is suddenly set to \(9 \mathrm{MW} / \mathrm{m}^{3}\), determine the time rate of temperature change in the reactor. Is the heat generation of reactor suddenly increased or decreased to \(9 \mathrm{MW} / \mathrm{m}^{3}\) from its steady operating condition?

A large plane wall, with a thickness \(L\) and a thermal conductivity \(k\), has its left surface \((x=0)\) exposed to a uniform heat flux \(\dot{q}_{0}\). On the right surface \((x=L)\), convection and radiation heat transfer occur in a surrounding temperature of \(T_{\infty}\). The emissivity and the convection heat transfer coefficient on the right surface are \(\bar{\varepsilon}\) and \(h\), respectively. Express the houndary conditions and the differential equation of this heat conduction problem during steady operation.

A cylindrical nuclear fuel rod of \(1 \mathrm{~cm}\) in diameter is encased in a concentric tube of \(2 \mathrm{~cm}\) in diameter, where cooling water flows through the annular region between the fuel rod \((k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) and the concentric tube. Heat is generated uniformly in the rod at a rate of \(50 \mathrm{MW} / \mathrm{m}^{3}\). The convection heat transfer coefficient for the concentric tube surface is \(2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the surface temperature of the concentric tube is \(40^{\circ} \mathrm{C}\), determine the average temperature of the cooling water. Can one use the given information to determine the surface temperature of the fuel rod? Explain.

Consider a small hot metal object of mass \(m\) and specific heat \(c\) that is initially at a temperature of \(T_{i}\). Now the object is allowed to cool in an environment at \(T_{\infty}\) by convection with a heat transfer coefficient of \(h\). The temperature of the metal object is observed to vary uniformly with time during cooling. Writing an energy balance on the entire metal object, derive the differential equation that describes the variation of temperature of the ball with time, \(T(t)\). Assume constant thermal conductivity and no heat generation in the object. Do not solve.

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