Consider a medium in which the heat conduction equation is given in its simplest form as $$ \frac{\partial^{2} T}{\partial x^{2}}+\frac{\partial^{2} T}{\partial y^{2}}=\frac{1}{\alpha} \frac{\partial T}{\partial t} $$ (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

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Question: Based on the analysis of the given heat conduction equation, determine whether the heat transfer is steady or transient, one-, two-, or three-dimensional, whether there is heat generation in the medium, and whether the thermal conductivity is constant or variable. Answer: Considering the given heat conduction equation, the heat transfer process is transient, two-dimensional, 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?

Since there is a time (t) component in the given equation, \(\frac{\partial T}{\partial t}\), the heat transfer process is transient instead of steady.
02

(b) Heat Transfer Dimensions?

The given equation has two spatial partial derivatives, \(\frac{\partial^{2} T}{\partial x^{2}}\) and \(\frac{\partial^{2} T}{\partial y^{2}}\), which correspond to the x and y directions. As there are two spatial dimensions, the heat transfer is two-dimensional.
03

(c) Heat Generation in the Medium?

If there were heat generation in the medium, we would see a term representing the heat sources or sinks in the given equation. The given equation doesn't have any term to account for this, so there is no heat generation in the medium.
04

(d) Thermal Conductivity: Constant or Variable?

In the given equation, we do not see any reference to thermal conductivity k(x,y) or its derivatives, which indicates that the medium has a constant thermal conductivity.

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Key Concepts

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

Transient Heat Transfer
In engineering and physics, understanding how heat flows within different materials and structures is crucial. Transient heat transfer refers to the phenomenon where the temperature within a system varies with time. Unlike steady-state heat transfer, where the temperatures are constant over time, transient scenarios are time-dependent and can be considerably more complex to analyze.

For example, when you heat a pan on a stove, initially, the pan's temperature increases over time until it reaches a stable temperature, provided the stove setting remains the same. This initial period of changing temperature is an example of transient heat transfer. The equation from the exercise \(\frac{1}{\text{α}} \frac{\text{∂} T}{\text{∂} t}\) includes a time derivative, indicating that the heat transfer process is transient. In real-world applications, transient analysis is vital for predicting how quickly a system responds to changes in thermal conditions, such as a sudden increase in heat due to a chemical reaction or a rapid drop in temperature after a system shutdown.
Two-Dimensional Heat Transfer
Heat can travel in multiple dimensions within a material. When heat spreads out in two perpendicular directions, we are dealing with two-dimensional heat transfer. This type of heat flow is more complex than one-dimensional but simpler than three-dimensional heat transfer.

In technical terms, we see this represented in our equation by the presence of both \(\frac{\text{∂}^{2} T}{\text{∂} x^{2}}\) and \(\frac{\text{∂}^{2} T}{\text{∂} y^{2}}\), accounting for the variations in temperature across the x and y directions, respectively. An example of a two-dimensional heat transfer scenario could be heat spreading through a wall, where the temperature varies both vertically and horizontally across the wall's surface but not significantly through its thickness. Understanding two-dimensional heat transfer is essential for designing and analyzing systems like heat exchangers, where heat must be effectively managed in multiple directions to ensure efficiency and safety.
Thermal Conductivity
Conductivity is the measure of a material's ability to conduct heat. It is designated by the symbol 'k' and is typically expressed in units of watts per meter-kelvin (W/m·K). Materials with high thermal conductivity, such as metals, facilitate heat transfer quickly, whereas insulators, like wood or foam, have low thermal conductivity and slow down heat transfer.

The heat conduction equation from our exercise does not include any term for varying thermal conductivity. In other words, the absence of a term like \(k(x, y)\) or its derivatives implies a constant thermal conductivity within the medium being studied. This simplifies the problem since it allows us to assume that heat moves through the material uniformly. However, in practice, some materials have variable conductivity that can be affected by factors such as temperature, requiring more advanced calculations to characterize the heat flow accurately.
Heat Generation
Heat generation within a medium can occur due to various processes, including chemical reactions, biological activity, or electrical resistance. In mathematical models, these internal heat sources (or sinks) should be accounted for if they are present. The lack of terms representing internal heat generation in the equation from our exercise \(\frac{\text{∂}^{2} T}{\text{∂} x^{2}}+\frac{\text{∂}^{2} T}{\text{∂} y^{2}}=\frac{1}{\text{α}} \frac{\text{∂} T}{\text{∂} t}\) suggests that the medium has no internal heat generation.

However, in scenarios where heat generation is significant, like in a battery during discharge or a reactor core, appropriate source terms must be included in the heat conduction model. Ignoring such terms could result in inaccurate predictions of temperature distribution and could lead to design flaws or safety issues in thermal management systems.

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Most popular questions from this chapter

In subsea oil and natural gas production, hydrocarbon fluids may leave the reservoir with a temperature of \(70^{\circ} \mathrm{C}\) and flow in subsea surrounding of \(5^{\circ} \mathrm{C}\). As a result of the temperature difference between the reservoir and the subsea surrounding, the knowledge of heat transfer is critical to prevent gas hydrate and wax deposition blockages. Consider a subsea pipeline with inner diameter of \(0.5 \mathrm{~m}\) and wall thickness of \(8 \mathrm{~mm}\) is used for transporting liquid hydrocarbon at an average temperature of \(70^{\circ} \mathrm{C}\), and the average convection heat transfer coefficient on the inner pipeline surface is estimated to be \(250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The subsea surrounding has a temperature of \(5^{\circ} \mathrm{C}\) and the average convection heat transfer coefficient on the outer pipeline surface is estimated to be \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the pipeline is made of material with thermal conductivity of \(60 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), by using the heat conduction equation (a) obtain the temperature variation in the pipeline wall, \((b)\) determine the inner surface temperature of the pipeline, \((c)\) obtain the mathematical expression for the rate of heat loss from the liquid hydrocarbon in the pipeline, and \((d)\) determine the heat flux through the outer pipeline surface.

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 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.

A spherical vessel has an inner radius \(r_{1}\) and an outer radius \(r_{2}\). The inner surface \(\left(r=r_{1}\right)\) of the vessel is subjected to a uniform heat flux \(\dot{q}_{1}\). The outer surface \(\left(r=r_{2}\right)\) is exposed to convection and radiation heat transfer in a surrounding temperature of \(T_{\infty}\). The emissivity and the convection heat transfer coefficient on the outer surface are \(\varepsilon\) and \(h\), respectively. Express the boundary conditions and the differential equation of this heat conduction problem during steady operation.

How do differential equations with constant coefficients differ from those with variable coefficients? Give an example for each type.

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