Consider a medium in which the heat conduction equation is given in its simplest form as $$ \frac{1}{r} \frac{\partial}{\partial r}\left(k r \frac{\partial T}{\partial r}\right)+\frac{\partial}{\partial z}\left(k \frac{\partial T}{\partial z}\right)+\dot{e}_{\mathrm{gen}}=0 $$ (a) Is heat transfer steady or transient? (b) Is heat transfer one-, two-, or three-dimensional? (c) Is there heat generation in the medium? (d) Is the thermal conductivity of the medium constant or variable?

Short Answer

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Question: Based on the given heat conduction equation of a medium, identify if the heat transfer is (a) steady or transient, (b) one-, two-, or three-dimensional, (c) if there is heat generation in the medium, and (d) whether the thermal conductivity of the medium is constant or variable. Answer: (a) Steady, (b) Two-dimensional, (c) Yes, (d) Constant

Step by step solution

01

: A heat transfer process is steady if it does not change with time and transient if it does change with time. In the given equation, there is no time derivative term, which means that heat transfer has reached a steady-state as there is no change in temperature with respect to time. So, the answer to part (a) is Steady. #Step 2: Determine the dimensions of heat transfer#

: To determine the number of dimensions in which the heat transfer occurs, we must look at the variables in the equation. Here, the temperature T depends on two spatial variables, r (radial coordinate) and z (axial coordinate). Since there are only two spatial variables involved, the heat transfer is two-dimensional. Answer for part (b) is Two-dimensional. #Step 3: Check for heat generation in the medium#
02

: Heat generation is represented by the term \(\dot{e}_{\mathrm{gen}}\) in the given equation. In this equation, the term \(\dot{e}_{\mathrm{gen}}\) is present and not equal to zero, which means there is heat generation occurring in the medium. With this information, we can conclude that there is heat generation in the medium. Answer for part (c) is Yes. #Step 4: Determine the thermal conductivity of the medium#

: Thermal conductivity is represented by the variable k in the given equation. If k is constant, then the conductivity of the medium is constant, and if k is variable, it indicates the conductivity is variable. In the given equation, k is not multiplied by any other variable and has no additional terms, which means the thermal conductivity of the medium is constant. Answer for part (d) is Constant.

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Key Concepts

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

Steady-State Heat Transfer
When we examine the manner in which heat moves through a substance, it's important to determine whether this process changes over time. If it doesn't, we call this a steady-state heat transfer. This situation is characterized by heat being transferred at a consistent rate, without any variations as time advances. There is a defining mathematical feature that signals a steady state: the absence of time derivatives in the heat conduction equation. In simpler terms, the temperature within the medium remains constant over time, making predictions and calculations relatively straightforward since the temporal aspect can be ignored.

In the context of our problem, we conclude that since no temperature variation with time is indicated—no time derivative is present in the equation—the process is indeed steady. Understanding this key concept is crucial since it significantly simplifies the analysis of thermal problems by focusing only on the spatial variations of temperature.
Two-Dimensional Heat Transfer
Heat can be transferred in different ways within a medium, and it can move in one, two, or three dimensions. The number of dimensions involved has profound implications on how we approach solving heat transfer problems. In a one-dimensional scenario, temperature varies along only one spatial dimension; in two dimensions, it varies along two orthogonal directions; and in three dimensions, it changes along all three spatial directions.

The problem at hand reveals a two-dimensional heat transfer phenomenon because the temperature is a function of two spatial coordinates—radial (r) and axial (z). These two directions form a plane, and any point within this plane can have a unique temperature. For problems of this kind, visualizing heat flow as a map across a surface can be helpful, where each point on the surface has a distinct temperature value independent of points in the third dimension.
Heat Generation
Within many materials, heat is not only transferred but can also be generated internally due to various processes such as chemical reactions, electrical resistance, or radioactive decay. This internal heat generation is an important aspect of the heat transfer equation and adds a source term to the equation, which must be accounted for in any realistic analysis.

In our exercise, the presence of the \(\dot{e}_{\mathrm{gen}}\) term in the conduction equation tells us that there's an internal heat production within the medium. This term can represent anything from the metabolic heat produced by organisms to heat generated by electrical components. Its inclusion means that when we are calculating the temperature distribution within the material, we need to consider this internal energy source as well as the heat being conducted in or out of every region.
Thermal Conductivity
An essential property that dictates how well a material can conduct heat is its thermal conductivity, typically denoted by the symbol \(k\). This property can significantly vary between different materials—metals, for example, usually have higher thermal conductivity than insulating materials like foam. Thermal conductivity can also vary with temperature, which leads to complex, temperature-dependent equations in some cases.

In this scenario, the constant thermal conductivity implies that the medium's ability to transfer heat does not change with temperature or position within the material. This eliminates the need to consider varying rates of heat conduction across the medium and simplifies the task of solving the heat conduction equation. Constant thermal conductivity is often an assumption used to model and analyze systems where the temperature range is limited or the material properties are uniform.

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Most popular questions from this chapter

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.

A 6-m-long 3-kW electrical resistance wire is made of \(0.2\)-cm-diameter stainless steel \((k=15.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The resistance wire operates in an environment at \(20^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(175 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) at the outer surface. Determine the surface temperature of the wire \((a)\) by using the applicable relation and \((b)\) by setting up the proper differential equation and solving it. Answers: (a) \(475^{\circ} \mathrm{C}\), (b) \(475^{\circ} \mathrm{C}\)

Consider a cylindrical shell of length \(L\), inner radius \(r_{1}\), and outer radius \(r_{2}\) 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 inner surface of the shell is maintained at a constant temperature of \(T_{1}\) while the outer surface is maintained at \(T_{2}\). Assuming steady one-dimensional heat transfer, obtain a relation for the heat transfer rate through the shell.

Consider a large plane wall of thickness \(L=0.05 \mathrm{~m}\). The wall surface at \(x=0\) is insulated, while the surface at \(x=L\) is maintained at a temperature of \(30^{\circ} \mathrm{C}\). The thermal conductivity of the wall is \(k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and heat is generated in the wall at a rate of \(\dot{e}_{\text {gen }}=\dot{e}_{0} e^{-0.5 x / L} \mathrm{~W} / \mathrm{m}^{3}\) where \(\dot{e}_{0}=8 \times 10^{6} \mathrm{~W} / \mathrm{m}^{3}\). Assuming steady one-dimensional heat transfer, \((a)\) express the differential equation and the boundary conditions for heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and (c) determine the temperature of the insulated surface of the wall.

Consider a large plate of thickness \(L\) and thermal conductivity \(k\) in which heat is generated uniformly at a rate of \(\dot{e}_{\text {gen. }}\) One side of the plate is insulated while the other side is exposed to an environment at \(T_{\infty}\) with a heat transfer coefficient of \(h\). \((a)\) Express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the plate, \((b)\) determine the variation of temperature in the plate, and \((c)\) obtain relations for the temperatures on both surfaces and the maximum temperature rise in the plate in terms of given parameters.

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