A \(1200-W\) iron is left on the iron board with its base exposed to ambient air at \(26^{\circ} \mathrm{C}\). The base plate of the iron has a thickness of \(L=0.5 \mathrm{~cm}\), base area of \(A=150 \mathrm{~cm}^{2}\), and thermal conductivity of \(k=18 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The inner surface of the base plate is subjected to uniform heat flux generated by the resistance heaters inside. The outer surface of the base plate whose emissivity is \(\varepsilon=0.7\), loses heat by convection to ambient air with an average heat transfer coefficient of \(h=\) \(30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) as well as by radiation to the surrounding surfaces at an average temperature of \(T_{\text {surr }}=295 \mathrm{~K}\). Disregarding any heat loss through the upper part of the iron, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the plate, \((b)\) obtain a relation for the temperature of the outer surface of the plate by solving the differential equation, and (c) evaluate the outer surface temperature.

Short Answer

Expert verified
In summary, to determine the outer surface temperature of the iron's base plate, follow these steps: 1. Write the differential equation for steady one-dimensional heat conduction through the plate: \(\frac{d^2 T}{d x^2} =0\) 2. Establish boundary conditions for the inner surface (i.e., heat flux generated by the heaters) and the outer surface (i.e., heat loss due to convection and radiation). 3. Solve the differential equation to find the linear temperature relation within the plate: \(T(x) = C_1x + C_2\) 4. Obtain the relation for the outer surface temperature by substituting the boundary conditions found in Steps 1 and 2: \(T_{out} = T(L) = C_1L + C_2\) 5. Evaluate the outer surface temperature, \(T_{out}\), by plugging in the given parameters. By analyzing the heat transfer processes and applying differential equations for heat conduction, the outer surface temperature of the iron's base plate can be determined.

Step by step solution

01

Write Differential Equation for Steady One-Dimensional Heat Conduction

Since the problem is one-dimensional, we will only consider the heat transfer in the direction normal to the base plate. The differential equation for steady one-dimensional heat conduction in a solid is given by: \[\frac{d^{2} T}{d x^{2}}=0\] In the given problem, heat is conducted from the inner surface of the base plate to the outer surface.
02

Boundary Conditions

There are two boundary conditions for this problem. The first boundary condition is at the inner surface of the base plate and the second is at the outer surface. At the inner surface (x=0), heat flux is generated by the resistance heaters inside, and it is equal to the power of the iron divided by the base area. So we can write: \[ q_{in} = \frac{1200\,\text{W}}{150\,\text{cm}^2} = - k \left(\frac{dT}{dx}\right)_{x=0}\] At the outer surface (x=L), heat is lost by convection to the ambient air and radiation to the surrounding surfaces. We can write two equations relating the heat flux from the plate to the ambient air: \[q_{conv} = h (T_{out} - T_{\infty})\] \[q_{rad} = \varepsilon \sigma (T_{out}^4 - T_{surr}^4)\] Combined heat loss (\(q_{out}\)) at the outer surface can be written as the sum of convective and radiative heat losses: \[q_{out} = q_{conv} + q_{rad}\] Now, we have another boundary condition (at x=L), which states that the heat flux conducted through the plate is equal to the combined heat loss at the outer surface. This can be written as: \[q_{out} = k\left(-\frac{dT}{dx}\right)_{x=L}\]
03

Solve the Differential Equation

The differential equation, \(\frac{d^2 T}{d x^2} =0\), implies a linear temperature profile within the plate. Integrating twice with respect to x, we obtain the following linear temperature relation (with arbitrary constants C1 and C2): \[T(x) = C_1x + C_2\] To solve this equation, substitute the boundary conditions from Steps 1 and 2 into the temperature relation and solve for C1 and C2.
04

Obtain the Relation for the Outer Surface Temperature

After finding the values of C1 and C2, we can substitute them into the temperature relation to obtain the function for the outer surface temperature (at x=L): \[T_{out} = T(L) = C_1L + C_2\]
05

Evaluate the Outer Surface Temperature

With the temperature relation for the outer surface established, we can plug in the given parameters and evaluate the outer surface temperature, \(T_{out}\).

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!

Key Concepts

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

Thermal Conductivity
Thermal conductivity is a key concept when discussing heat conduction. It is a material-specific trait that tells us how well the material conducts heat. Mathematically, it is denoted by the symbol \(k\) and is measured in watts per meter-kelvin (\(W/m\cdot K\)). The higher the thermal conductivity, the more efficient the material is at transferring heat. In the context of the iron base plate in the exercise, the thermal conductivity is given as \(k=18 W/m\cdot K\), indicating it transfers heat effectively.

One interesting point to be noted here is that when we talk about thermal conductivity in a steady one-dimensional heat transfer situation, it assumes a constant value within the material, implying uniform heat transfer characteristics across the material. Therefore, in the solved problem, the rate of heat flow through the iron's base plate is consistent, leading to the establishment of a steady temperature profile that can be determined by solving appropriate mathematical equations under given boundary conditions.
Steady One-Dimensional Heat Transfer
In the realm of heat transfer, the term 'steady' implies that temperature does not change with time, while 'one-dimensional' specifies that heat flows in only one direction. Steady one-dimensional heat transfer is a simplified scenario that is often used to model heat transfer in systems where temperature gradients exist in only one dimension and remain constant over time.

In our discussed exercise, the heat transfer through the thickness of the iron's base plate represents a classic example of steady one-dimensional heat transfer. This assumption simplifies the problem, allowing us to use the basic heat conduction equation \(\frac{d^{2} T}{d x^{2}}=0\) to describe the system. The solution to this differential equation points to a linear temperature gradient within the base plate, making the analysis far more manageable and the computation of temperature profiles straightforward once the boundary conditions are addressed.
Boundary Conditions
Boundary conditions are essential for solving differential equations in heat transfer problems as they define how the system interacts with its surroundings. They're set based on the physical constraints and forces acting at the boundaries of the system. There are generally two types of boundary conditions in heat transfer: temperature-based (Dirichlet) and flux-based (Neumann).

In the example of the iron's base plate, we have a flux-based boundary condition at the inner surface where heat is being generated by the resistance heater. This is expressed by a uniform heat flux that determines the temperature gradient at that surface. Conversely, at the base plate's outer surface, the heat loss due to convection and radiation to the surroundings sets the boundary condition, which matches the heat flux leaving the plate. Adequately defining and applying these boundary conditions is critical for accurately assessing the temperature distribution within the base plate. Understanding and implementing these conditions correctly allows us to predict how the plate's temperature will react to the internal generation of heat and external cooling influences.

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

The outer surface of an engine is situated in a place where oil leakage can occur. Some oils have autoignition temperatures of approximately above \(250^{\circ} \mathrm{C}\). When oil comes in contact with a hot engine surface that has a higher temperature than its autoignition temperature, the oil can ignite spontaneously. Treating the engine housing as a plane wall, the inner surface \((x=0)\) is subjected to \(6 \mathrm{~kW} / \mathrm{m}^{2}\) of heat. The engine housing \((k=13.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) has a thickness of \(1 \mathrm{~cm}\), and the outer surface \((x=L)\) is exposed to an environment where the ambient air is \(35^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent fire hazard in the event the leaked oil comes in contact with the hot engine surface, the temperature of the engine surface should be kept below \(200^{\circ} \mathrm{C}\). Determine the variation of temperature in the engine housing and the temperatures of the inner and outer surfaces. Is the outer surface temperature of the engine below the safe temperature?

In a food processing facility, a spherical container of inner radius \(r_{1}=40 \mathrm{~cm}\), outer radius \(r_{2}=41 \mathrm{~cm}\), and thermal conductivity \(k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is used to store hot water and to keep it at \(100^{\circ} \mathrm{C}\) at all times. To accomplish this, the outer surface of the container is wrapped with a 800 -W electric strip heater and then insulated. The temperature of the inner surface of the container is observed to be nearly \(120^{\circ} \mathrm{C}\) at all times. Assuming 10 percent of the heat generated in the heater is lost through the insulation, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the container, \((b)\) obtain a relation for the variation of temperature in the container material by solving the differential equation, and \((c)\) evaluate the outer surface temperature of the container. Also determine how much water at \(100^{\circ} \mathrm{C}\) this tank can supply steadily if the cold water enters at \(20^{\circ} \mathrm{C}\).

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 \(x=L\).

Consider a plane wall of thickness \(L\) whose thermal conductivity varies in a specified temperature range as \(k(T)=\) \(k_{0}\left(1+\beta T^{2}\right)\) where \(k_{0}\) and \(\beta\) are two specified constants. The wall surface at \(x=0\) is maintained at a constant temperature of \(T_{1}\), while the surface at \(x=L\) is maintained at \(T_{2}\). Assuming steady one-dimensional heat transfer, obtain a relation for the heat transfer rate through the wall.

A spherical metal ball of radius \(r_{o}\) is heated in an oven to a temperature of \(T_{i}\) throughout and is then taken out of the oven and dropped into a large body of water at \(T_{\infty}\) where it is cooled by convection with an average convection heat transfer coefficient of \(h\). Assuming constant thermal conductivity and transient one-dimensional heat transfer, express the mathematical formulation (the differential equation and the boundary and initial conditions) of this heat conduction problem. Do not solve.

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