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 \(44^{\circ} \mathrm{C}\).

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

How do you distinguish a linear differential equation from a nonlinear one?

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 spherical shell of inner radius \(r_{1}\), outer radius \(r_{2}\), thermal conductivity \(k\), and emissivity \(\varepsilon\). The outer surface of the shell is subjected to radiation to surrounding surfaces at \(T_{\text {surr }}\), but the direction of heat transfer is not known. Express the radiation boundary condition on the outer surface of the shell.

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.

A pipe is used for transporting boiling water in which the inner surface is at \(100^{\circ} \mathrm{C}\). The pipe is situated in surroundings where the ambient temperature is \(10^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(70 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The wall thickness of the pipe is \(3 \mathrm{~mm}\) and its inner diameter is \(30 \mathrm{~mm}\). The pipe wall has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.23 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.002 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). For safety reasons and to prevent thermal burn to workers, the outer surface temperature of the pipe should be kept below \(50^{\circ} \mathrm{C}\). Determine whether the outer surface temperature of the pipe is at a safe temperature so as to avoid thermal burn.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free