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Consider an egg being cooked in boiling water in a pan. Would you model the heat transfer to the egg as one-, two-, or three-dimensional? Would the heat transfer be steady or transient? Also, which coordinate system would you use to solve this problem, and where would you place the origin? Explain.

Short Answer

Expert verified
Answer: An egg being cooked in boiling water can be modeled as a one-dimensional, transient heat transfer problem. The appropriate coordinate system to use is the polar (spherical) coordinate system, with the origin placed at the center of the egg.

Step by step solution

01

Determine the dimensionality of the heat transfer problem

Since heat is being conducted from the hot water to the egg, the heat transfer occurs in all three spatial dimensions; therefore, it is a three-dimensional problem. However, because the egg has a symmetrical shape, the temperature distribution would most likely be similar across its surface, and hence it can be simplified to a one-dimensional problem along the radial axis of the egg. In this case, a one-dimensional model is appropriate and practical.
02

Identify steady or transient heat transfer

Steady heat transfer implies that the temperature does not change with time at any point within the object. In the case of the egg being cooked in boiling water, the temperature changes throughout the heating process and depends on the time the egg is in contact with the hot water. That means the heat transfer is transient, not steady.
03

Choose the coordinate system and origin

Since we decided to consider this as a one-dimensional problem, the natural coordinate system to use would be the polar (spherical) coordinate system due to the shape of the egg. In this case, the radial coordinate (r) would represent the distance from center to surface. The origin should be placed at the center of the egg, as this gives the most straightforward way to calculate distances within the egg and simplifies the analysis. In conclusion: For cooking an egg in boiling water, the heat transfer can be modeled as a one-dimensional, transient problem using the polar (spherical) coordinate system with the origin placed at the center of the egg.

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Most popular questions from this chapter

A cylindrical nuclear fuel rod \(1 \mathrm{~cm}\) in diameter is encased in a concentric tube \(2 \mathrm{~cm}\) in diameter, where cooling water flows through the annular region between the fuel rod $(k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ and the concentric tube. Heat is generated uniformly in the rod at a rate of \(50 \mathrm{MW} / \mathrm{m}^{3}\). The convection heat transfer coefficient for the concentric tube surface is $2000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. If the surface temperature of the concentric tube is \(40^{\circ} \mathrm{C}\), determine the average temperature of the cooling water. Can one use the given information to determine the surface temperature of the fuel rod? Explain.

A \(1000-W\) iron is left on the ironing 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 \(T_{\text {sarr }}=295 \mathrm{~K}\). 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.

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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 \(x=L\). Answer: (c) \(-4^{\circ} \mathrm{C}\)

Is the thermal conductivity of a medium, in general, constant or does it vary with temperature?

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