Consider a medium in which the heat conduction equation is given in its simplest form as $$ \frac{1}{r^{2}} \frac{\partial}{\partial r}\left(r^{2} \frac{\partial T}{\partial r}\right)+\frac{1}{r^{2} \sin ^{2} \theta} \frac{\partial^{2} T}{\partial \phi^{2}}=\frac{1}{\alpha} \frac{\partial T}{\partial t} $$ (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

Expert verified
Is there heat generation in the medium, and is the thermal conductivity constant or variable? Answer: The heat transfer is transient, as there is a time-dependent term in the equation. It is three-dimensional, as there are three spatial variables present. There is no heat generation in the medium, and the thermal conductivity is constant.

Step by step solution

01

(a) Steady or transient heat transfer

To determine whether heat transfer is steady or transient, we need to look at the time-dependent term on the right side of the equation. If there is a presence of time in the equation, then it is transient; if not, it is steady. In our case, the equation is: $$ \frac{1}{r^{2}} \frac{\partial}{\partial r}\left(r^{2} \frac{\partial T}{\partial r}\right)+\frac{1}{r^{2} \sin ^{2} \theta} \frac{\partial^{2} T}{\partial \phi^{2}}=\frac{1}{\alpha} \frac{\partial T}{\partial t} $$ As we can see, there is a time-dependent term \(\frac{\partial T}{\partial t}\) on the right side of the equation. Therefore, heat transfer is transient.
02

(b) Dimensionality of heat transfer

To determine the dimensionality of heat transfer, we need to see how many spatial variables are present in the equation. Here, we can see the spatial variables \(r\), \(\theta\), and \(\phi\). Since there are three spatial variables, the heat transfer problem is three-dimensional.
03

(c) Presence of heat generation

If there is heat generation in the medium, it should appear as an additional term in the given heat conduction equation. However, the equation has no such term, which means that there is no heat generation in the medium.
04

(d) Constant or variable thermal conductivity

Given the form of the heat conduction equation, which has spatial derivative terms on the left side, and the time-dependent term on the right side, no additional terms representing the variation in thermal conductivity can be seen. This implies that the thermal conductivity of the medium is constant.

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Key Concepts

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

Heat Conduction Equation
Understanding the heat conduction equation is crucial for analyzing how heat transfer occurs within a material. The equation in question describes how temperature changes within a medium as a function of space and time. In its simplest form, the equation involves partial derivatives that account for temperature gradients in multiple directions, as well as time. These gradients ultimately dictate how heat flows from regions of high temperature to regions of low temperature.

When solving heat conduction problems, identifying whether the process is steady or transient is an essential step. A steady-state condition means that temperature does not change with time, which is not the case here. The presence of the term \(\frac{\partial T}{\partial t}\) indicates the process is transient, meaning temperature changes as time progresses. This time-dependent aspect requires solving the heat conduction equation with respect to time to understand the evolution of temperature within the medium.
Three-Dimensional Heat Transfer
Heat transfer can occur in one, two, or three dimensions. The dimensionality of a heat transfer problem is determined by the number of spatial directions in which heat can flow. In three-dimensional heat transfer, temperature can vary in all three spatial directions, which significantly complicates the analysis compared to one- or two-dimensional problems.

For the exercise at hand, the equation involves derivatives with respect to three spatial variables: \(r\), \(\theta\), and \(\phi\). Therefore, the heat transfer is occurring in a three-dimensional manner. This means that to predict temperature changes, it is necessary to consider how heat moves in radial, azimuthal, and polar directions within the medium, which makes the equation more challenging to solve. Numerical methods are often employed for such complex, multi-dimensional heat transfer scenarios.
Thermal Conductivity

Understanding Thermal Conductivity

Thermal conductivity is a property of materials that measures their ability to conduct heat. Materials with high thermal conductivity can transfer heat swiftly, while those with lower conductivity act as better insulators. In the context of the heat conduction equation, thermal conductivity often appears as a constant multiplier of the temperature gradient terms.

In scenarios where the thermal conductivity is constant, it implies that the material's heat conducting properties do not change with temperature or position within the medium. For complex materials, or under varying conditions, thermal conductivity may instead vary, leading to a more intricate form of the heat conduction equation. However, in our exercise, thermal conductivity is assumed to be constant throughout the medium.
Heat Generation
Heat generation within a medium can occur due to various reasons like chemical reactions, electrical energy conversion, or radioactive decay. In the heat conduction equation, heat generation is typically included as a source term that adds to the heat energy within the medium.

For the given exercise, the absence of an additional source term in the equation indicates that there is no internal heat generation within the medium. This simplifies the problem, as it implies that all changes in temperature across the material result solely from heat transfer due to existing temperature gradients and not from any internal heat being produced. It's essential to accurately identify whether heat generation is present or not, as it significantly affects the thermal behavior of the medium and thereby the solutions to the heat conduction problem.

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Most popular questions from this chapter

Consider a chilled-water pipe of length \(L\), inner radius \(r_{1}\), outer radius \(r_{2}\), and thermal conductivity \(k\). Water flows in the pipe at a temperature \(T_{f}\) and the heat transfer coefficient at the inner surface is \(h\). If the pipe is well-insulated on the outer surface, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the pipe and \((b)\) obtain a relation for the variation of temperature in the pipe by solving the differential equation.

A spherical container, with an inner radius \(r_{1}=1 \mathrm{~m}\) and an outer radius \(r_{2}=1.05 \mathrm{~m}\), has its inner surface subjected to a uniform heat flux of \(\dot{q}_{1}=7 \mathrm{~kW} / \mathrm{m}^{2}\). The outer surface of the container has a temperature \(T_{2}=25^{\circ} \mathrm{C}\), and the container wall thermal conductivity is \(k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Show that the variation of temperature in the container wall can be expressed as \(T(r)=\left(\dot{q}_{1} r_{1}^{2} / k\right)\left(1 / r-1 / r_{2}\right)+T_{2}\) and determine the temperature of the inner surface of the container at \(r=r_{1}\).

A spherical vessel is filled with chemicals undergoing an exothermic reaction. The reaction provides a uniform heat flux on the inner surface of the vessel. The inner diameter of the vessel is \(5 \mathrm{~m}\) and its inner surface temperature is at \(120^{\circ} \mathrm{C}\). The wall of the vessel has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.01 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\beta=0.0018 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). The vessel is situated in a surrounding with an ambient temperature of \(15^{\circ} \mathrm{C}\), the vessel's outer surface experiences convection heat transfer with a coefficient of \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent thermal burn on skin tissues, the outer surface temperature of the vessel should be kept below \(50^{\circ} \mathrm{C}\). Determine the minimum wall thickness of the vessel so that the outer surface temperature is \(50^{\circ} \mathrm{C}\) or lower.

Consider a long solid cylinder of radius \(r_{o}=4 \mathrm{~cm}\) and thermal conductivity \(k=25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Heat is generated in the cylinder uniformly at a rate of \(\dot{e}_{\text {gen }}=35 \mathrm{~W} / \mathrm{cm}^{3}\). The side surface of the cylinder is maintained at a constant temperature of \(T_{s}=80^{\circ} \mathrm{C}\). The variation of temperature in the cylinder is given by $$ T(r)=\frac{\dot{e}_{\text {gen }} r_{o}^{2}}{k}\left[1-\left[1-\left(\frac{r}{r_{o}}\right)^{2}\right]+T_{s}\right. $$ Based on this relation, determine \((a)\) if the heat conduction is steady or transient, \((b)\) if it is one-, two-, or three-dimensional, and \((c)\) the value of heat flux on the side surface of the cylinder at \(r=r_{o^{*}}\)

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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