In order to determine the size of the heating element of a new oven, it is desired to determine the rate of heat loss through the walls, door, and the top and bottom section of the oven. In your analysis, would you consider this to be a steady or transient heat transfer problem? Also, would you consider the heat transfer to be one-dimensional or multidimensional? Explain.

Short Answer

Expert verified
Answer: The heat loss in the oven is a steady heat transfer problem because the temperature distribution does not change once the oven reaches its desired temperature. It is a multidimensional heat transfer problem because the temperature distribution varies in multiple directions due to the heat loss from the walls, door, and top and bottom sections of the oven.

Step by step solution

01

Identify the heat transfer problem: Steady or Transient

To determine if the heat transfer problem is steady or transient, we need to analyze the characteristics of the problem. A steady heat transfer problem happens when the temperature distribution inside the object does not change with time. Conversely, a transient heat transfer problem has temperature distribution that changes with time. Considering the oven is a closed system and heats up to a certain temperature and maintains that temperature in its chambers, it is a steady heat transfer problem. This is because the temperature distribution becomes stable and does not change with time when the oven reaches the desired temperature.
02

Identify the heat transfer type: One-dimensional or Multidimensional

To decide if the heat transfer is one-dimensional or multidimensional, we need to consider how heat flows throughout the oven. In a one-dimensional heat transfer problem, the temperature changes only in one direction, while in a multidimensional heat transfer problem, temperature changes in more than one direction. Since the heat loss occurs through different parts of the oven such as the walls, door, and top and bottom sections, it is a multidimensional heat transfer problem. The temperature distribution changes in more than one direction, considering the spatial configuration of the oven.
03

Summary

In conclusion, the heat transfer problem in this oven is a steady heat transfer problem because the temperature distribution does not change once the oven reaches its desired temperature. Moreover, it is considered a multidimensional heat transfer problem because the temperature distribution varies in multiple directions due to the heat loss from the walls, door, and top and bottom sections of the oven.

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Key Concepts

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

Steady Heat Transfer
In the study of heat transfer, it is crucial to understand different types of thermal phenomena. One fundamental concept is steady heat transfer. This occurs when the temperature distribution of a medium does not change with time. In other words, within a system in steady state, the amount of heat entering a section is equal to the amount of heat leaving, leading to a constant temperature over time.

Applying this to real-world situations, such as the heating element of an oven, if the temperature inside the oven remains unchanged after achieving the desired level, it is said to be in steady-state operation. This implies that the thermal input of the heating element is perfectly balanced with the heat loss through the oven's insulation and surfaces. Knowing that a system operates under steady heat transfer simplifies analysis and design since time-dependent changes can be disregarded in the calculations.
Transient Heat Transfer
Conversely, transient heat transfer, also known as unsteady heat transfer, occurs when the temperature within a system changes with time. This is common when a system is not in equilibrium and thermal adjustments are happening, such as when an oven is preheating. During this phase, different parts of the oven warm up at different rates before reaching a steady state.

Transient analysis is important for understanding how fast systems respond to thermal changes, which can be vital in applications where temperature regulation is crucial for quality and safety, like in food processing or materials engineering. It involves solving time-dependent heat transfer equations, which are often more complex due to the dynamic nature of heat movement within the system.
One-dimensional Heat Transfer
Heat transfer problems are often simplified by considering the predominant direction in which heat moves. In one-dimensional heat transfer, heat is assumed to travel in only one direction. This simplification is often made under the assumption that heat conduction in the other two dimensions is negligible compared to the primary direction.

This concept is frequently used in scenarios where a system has a much greater length in one dimension relative to others, such as heat flow through a long, thin rod. The benefit of one-dimensional analysis is in the reduction of complex equations and data requirements, making problems more tractable and solutions easier to understand. However, this simplification may not always apply, such as in the case of an oven, where heat can be lost in multiple directions from different components.
Multidimensional Heat Transfer
In contrast, multidimensional heat transfer takes into account heat moving in two or more directions. This introduces complexity into the analysis since the temperature gradient and thus the heat flux can change in different spatial dimensions. This type of heat transfer is essential in understanding and solving more realistic and practical problems where heat does not move uniformly in a single direction.

For instance, in an oven, heat loss through walls, doors, and top and bottom sections should be perceived as a multidimensional problem. Here, heat can flow in all three spatial dimensions, and accounting for this is key to accurately estimating heat loss and designing heating elements for thermal management. Multidimensional analysis requires solving partial differential equations and is, therefore, computationally more intensive, but essential for many real-world applications.

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Most popular questions from this chapter

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 allowed to cool in ambient air at \(T_{\infty}\) by convection and radiation. The emissivity of the outer surface of the cylinder is \(\varepsilon\), and the temperature of the surrounding surfaces is \(T_{\text {surr }}\). The average convection heat transfer coefficient is estimated to be \(h\). Assuming variable 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.

The temperature of a plane wall during steady onedimensional heat conduction varies linearly when the thermal conductivity is constant. Is this still the case when the thermal conductivity varies linearly with temperature?

Consider a homogeneous spherical piece of radioactive material of radius \(r_{o}=0.04 \mathrm{~m}\) that is generating heat at a constant rate of \(\dot{e}_{\text {gen }}=5 \times 10^{7} \mathrm{~W} / \mathrm{m}^{3}\). The heat generated is dissipated to the environment steadily. The outer surface of the sphere is maintained at a uniform temperature of \(110^{\circ} \mathrm{C}\) and the thermal conductivity of the sphere is \(k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Assuming steady one-dimensional heat transfer, \((a)\) express the differential equation and the boundary conditions for heat conduction through the sphere, \((b)\) obtain a relation for the variation of temperature in the sphere by solving the differential equation, and \((c)\) determine the temperature at the center of the sphere.

A long homogeneous resistance wire of radius \(r_{o}=\) \(0.6 \mathrm{~cm}\) and thermal conductivity \(k=15.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is being used to boil water at atmospheric pressure by the passage of electric current. Heat is generated in the wire uniformly as a result of resistance heating at a rate of \(16.4 \mathrm{~W} / \mathrm{cm}^{3}\). The heat generated is transferred to water at \(100^{\circ} \mathrm{C}\) by convection with an average heat transfer coefficient of \(h=3200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming steady one-dimensional heat transfer, \((a)\) express the differential equation and the boundary conditions for heat conduction through the wire, \((b)\) obtain a relation for the variation of temperature in the wire by solving the differential equation, and \((c)\) determine the temperature at the centerline of the wire.

When a long section of a compressed air line passes through the outdoors, it is observed that the moisture in the compressed air freezes in cold weather, disrupting and even completely blocking the air flow in the pipe. To avoid this problem, the outer surface of the pipe is wrapped with electric strip heaters and then insulated. Consider a compressed air pipe of length \(L=6 \mathrm{~m}\), inner radius \(r_{1}=3.7 \mathrm{~cm}\), outer radius \(r_{2}=4.0 \mathrm{~cm}\), and thermal conductivity \(k=14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) equipped with a 300 -W strip heater. Air is flowing through the pipe at an average temperature of \(-10^{\circ} \mathrm{C}\), and the average convection heat transfer coefficient on the inner surface is \(h=30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming 15 percent of the heat generated in the strip heater is lost through the insulation, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the pipe, \((b)\) obtain a relation for the variation of temperature in the pipe material by solving the differential equation, and \((c)\) evaluate the inner and outer surface temperatures of the pipe.

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