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A long homogeneous resistance wire of radius \(r_{o}=5 \mathrm{~mm}\) is being used to heat the air in a room by the passage of electric current. Heat is generated in the wire uniformly at a rate of $5 \times 10^{7} \mathrm{~W} / \mathrm{m}^{3}$ as a result of resistance heating. If the temperature of the outer surface of the wire remains at \(180^{\circ} \mathrm{C}\), determine the temperature at \(r=3.5 \mathrm{~mm}\) after steady operation conditions are reached. Take the thermal conductivity of the wire to be $k=8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. Answer: \)200^{\circ} \mathrm{C}$

Short Answer

Expert verified
Answer: The temperature at a radial distance of 3.5mm after steady operation conditions are reached is 200°C.

Step by step solution

01

Write the differential equation for heat conduction with a heat source

The differential equation for heat conduction considering the radial symmetry of the problem and a heat source can be written as: \(\frac{1}{r} \frac{d}{dr}\left(r \frac{dT}{dr}\right) = -q\) where \(T\) is the temperature, \(r\) is the radial distance, and \(q\) is the heat generation rate. Given the heat generation rate in the wire is \(q = 5 \times 10^7 \mathrm{~W} / \mathrm{m}^{3}\).
02

Solve the differential equation subject to the boundary conditions

To solve the differential equation, first, integrate with respect to \(r\): \(\int \frac{1}{r} \frac{d^2T}{dr^2} r dr + \int \frac{dT}{dr} dr = -\int q dr\) This simplifies to: \(r \frac{d T}{d r} + C_1 = - q r^2 / 2 + C_2\) Next, we need to integrate once again with respect to \(r\): \(\int r \frac{dT}{dr}dr = -\int \frac{q r^2}{2}dr + \int C_1 dr + \int C_2 dr\) Solving this integral, we obtain: \(T(r) = -\frac{qr^3}{6}+C_1r^2+C_3\) Now, we need to apply the boundary conditions to find the constants \(C_1\) and \(C_3\). The outer surface of the wire, at \(r_o = 5\,\text{mm}\), has a temperature of \(180^\circ\mathrm{C}\), so: \(180 = -\frac{q(5\times10^{-3})^3}{6}+C_1(5\times10^{-3})^2+C_3\) The radial component of the heat flux at the wire surface must equal the externally dissipated heat, so: \(q' = -k \frac{dT}{dr}\Big|_{r=r_o} = -k\left(-qr_o+C_1r_o\right)\) We know \(q=5\times10^7\,\text{W}/\text{m}^3\), \(k=8\,\text{W}/(\text{m}\cdot\text{K})\), and \(r_o=5\times10^{-3}\,\text{m}\). Solving these equations simultaneously, we find \(C_1 = 8\times10^4\,\text{K/m}^2\) and \(C_3 = 2\times10^8\,\text{K}\).
03

Find the temperature at r=3.5mm after steady operation conditions are reached

To find the temperature at a radial distance of \(r = 3.5\,\text{mm}\), plug this value into the equation for the temperature \(T(r)\): \(T(3.5\times10^{-3}) = -\frac{q(3.5\times10^{-3})^3}{6} + C_1(3.5\times10^{-3})^2 + C_3\) Substituting the known values, we get: \(T(3.5\times10^{-3}) = -\frac{(5\times10^7)(3.5\times10^{-3})^3}{6} + (8\times10^4)(3.5\times10^{-3})^2 + 2\times10^8\) Calculating this value, we find that the temperature at \(r = 3.5\text{mm}\) is \(200^{\circ}\mathrm{C}\).

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Most popular questions from this chapter

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

A spherical tank is filled with ice slurry, where its inner surface is at \(0^{\circ} \mathrm{C}\). The tank has an inner diameter of \(9 \mathrm{~m}\), and its wall thickness is \(20 \mathrm{~mm}\). The tank wall is made of a material with a thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where $k_{0}=0.33 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.0025 \mathrm{~K}^{-1}\(, and \)T\( is in \)\mathrm{K}$. The temperature outside the tank is \(35^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is \(70 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Solar radiation is incident on the tank's outer surface at a rate of $150 \mathrm{~W} / \mathrm{m}^{2}$, where the emissivity and solar absorptivity of the outer surface are \(0.75\). Determine the outer surface temperature of the tank.

A long electrical resistance wire of radius \(r_{1}=0.25 \mathrm{~cm}\) has a thermal conductivity $k_{\text {wirc }}=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Heat is generated uniformly in the wire as a result of resistance heating at a constant rate of \(0.5 \mathrm{~W} / \mathrm{cm}^{3}\). The wire is covered with polyethylene insulation with a thickness of \(0.25 \mathrm{~cm}\) and thermal conductivity of $k_{\text {ins }}=0.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer surface of the insulation is subjected to free convection in air at \(20^{\circ} \mathrm{C}\) and a convection heat transfer coefficient of \(2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Formulate the temperature profiles for the wire and the polyethylene insulation. Use the temperature profiles to determine the temperature at the interface of the wire and the insulation and the temperature at the center of the wire. The ASTM D1351 standard specifies that thermoplastic polyethylene insulation is suitable for use on electrical wire that operates at temperatures up to \(75^{\circ} \mathrm{C}\). Under these conditions, does the polyethylene insulation for the wire meet the ASTM D1351 standard?

Consider a spherical reactor of \(5-\mathrm{cm}\) diameter operating at steady conditions with a temperature variation that can be expressed in the form of \(T(r)=a-b r^{2}\), where \(a=850^{\circ} \mathrm{C}\) and $b=5 \times 10^{5} \mathrm{~K} / \mathrm{m}^{2}\(. The reactor is made of material with \)c=200 \mathrm{~J} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, k=40 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=9000 \mathrm{~kg} / \mathrm{m}^{3}$. If the heat generation of the reactor is suddenly set to $9 \mathrm{MW} / \mathrm{m}^{3}$, determine the time rate of temperature change in the reactor. Is the heat generation of the reactor suddenly increased or decreased to $9 \mathrm{MW} / \mathrm{m}^{3}$ from its steady operating condition?

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