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Consider a solid stainless steel wire with a thermal conductivity of $14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. The wire has a diameter of \)1 \mathrm{~mm}\(, has a resistivity of \)45 \times 10^{-8} \Omega \cdot \mathrm{m}\(, and carries a current of \)120 \mathrm{~A}$. (a) Determine the rate of heat generated within the wire $\left(\mathrm{W} / \mathrm{m}^{3}\right.\( ), and \)(b)$ calculate the maximum temperature rise in the wire.

Short Answer

Expert verified
Question: Determine the heat generated within the wire and the maximum temperature rise of the wire with the following given values: diameter \(d = 1 \times 10^{-3}\,\text{m}\), resistivity \(\rho = 45 \times 10^{-8}\, \Omega \cdot \mathrm{m}\), current \(I = 120\, \mathrm{A}\), and thermal conductivity \(k = 14\, \mathrm{W}/\mathrm{m}\cdot\mathrm{K}\).

Step by step solution

01

Calculate the resistance per unit length

Firstly, we have to calculate the resistance per unit length. To do this, we use the formula: \(\text{Resistance per unit length} = \rho\frac{L}{A}\) The area of the wire can be found using the diameter of the wire by the following formula: \(\text{Area} = A = \pi(\frac{d}{2})^2\)
02

Calculate the heat generated per unit length

Now that we have the resistance per unit length, we can find the heat generated per unit length using the formula: \(\text{Heat generated per unit length} = Q = I^2R\)
03

Calculate the heat generated per unit volume

After we have the heat generated per unit length, we can find the heat generated per unit volume using the formula: \(\text{Heat generated per unit volume} = q = \frac{Q}{V}\) We need to find the volume of the wire first: \(\text{Volume} = V = A \cdot L\)
04

Calculate the maximum temperature rise

Finally, we can find the maximum temperature rise using the formula: \(\text{Maximum temperature rise} = T = \frac{Q}{k}\) Now we will plug in the given values and solve for the different parameters. Given: Diameter \(d = 1 \times 10^{-3}\,\text{m}\) Resistivity \(\rho = 45 \times 10^{-8}\, \Omega \cdot \mathrm{m}\) Current \(I = 120\, \mathrm{A}\) Thermal conductivity \(k = 14\, \mathrm{W}/\mathrm{m}\cdot\mathrm{K}\) Calculate: \(A = \pi(\frac{d}{2})^2 \Rightarrow A = 7.854 \times 10^{-7}\, \mathrm{m}^2\) \(\rho\frac{L}{A} \Rightarrow R = 5.731\times10^{-5}\, \Omega\cdot\mathrm{m}\) \(Q = (120\,\mathrm{A})^2\cdot(5.731\times10^{-5}\, \Omega\cdot\mathrm{m}) \Rightarrow Q = 822.99\, \mathrm{W}/\mathrm{m}\) \(V=L\cdot A = L\cdot7.854 \times 10^{-7}\, \mathrm{m}^2\) \(q = \frac{822.99\, \mathrm{W}/\mathrm{m}}{7.854 \times 10^{-7}\, \mathrm{m}^2\cdot L} \Rightarrow q=1.047\times10^{6}\, \mathrm{W}/\mathrm{m}^3\) \(T = \frac{822.99\, \mathrm{W}/\mathrm{m}}{14\, \mathrm{W}/\mathrm{m}\cdot\mathrm{K}} \Rightarrow T = 58.78 \,^\circ \mathrm{K}\) So, the heat generated within the wire is \(1.047 \times 10^6 \, \mathrm{W}/\mathrm{m}^{3}\), and the maximum temperature rise in the wire is \(58.78\,^\circ \mathrm{K}\).

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Most popular questions from this chapter

Liquid water flows in a tube with the inner surface lined with polytetrafluoroethylene (PTFE). The inner diameter of the tube is $24 \mathrm{~mm}\(, and its wall thickness is \)5 \mathrm{~mm}$. The thermal conductivity of the tube wall is $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. The water flowing in the tube has a temperature of \)50^{\circ} \mathrm{C}$, and the convection heat transfer coefficient with the inner tube surface is \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The outer surface of the tube is exposed to convection with superheated steam at \(600^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. According to the ASME Code for Process Piping (ASME B31.3-2014, A323), the recommended maximum temperature for PTFE lining is \(260^{\circ} \mathrm{C}\). Formulate the temperature profile in the tube wall. Use the temperature profile to determine if the tube inner surface is in compliance with the ASME Code for Process Piping.

Does heat generation in a solid violate the first law of thermodynamics, which states that energy cannot be created or destroyed? Explain.

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.

What kinds of differential equations can be solved by direct integration?

A cylindrical fuel rod $(k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}) 2 \mathrm{~cm}$ in diameter is encased in a concentric tube and cooled by water. The fuel rod generates heat uniformly at a rate of $100 \mathrm{MW} / \mathrm{m}^{3}$, and the average temperature of the cooling water is \(75^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $2500 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$. The operating pressure of the cooling water is such that the surface temperature of the fuel rod must be kept below \(200^{\circ} \mathrm{C}\) to prevent the cooling water from reaching the critical heat flux (CHF). The critical heat flux is a thermal limit at which a boiling crisis can occur that causes overheating on the fuel rod surface and leads to damage. Determine the variation of temperature in the fuel rod and the temperature of the fuel rod surface. Is the surface of the fuel rod adequately cooled?

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