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A 6-m-long, 2-kW electrical resistance wire is made of \(0.2-\mathrm{cm}\)-diameter stainless steel $(k=15.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The resistance wire operates in an environment at \(20^{\circ} \mathrm{C}\) with a heat transfer coefficient of $175 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ at the outer surface. Determine the surface temperature of the wire \((a)\) by using the applicable relation and \((b)\) by setting up the proper differential equation and solving it.

Short Answer

Expert verified
In summary, the surface temperature of the electrical resistance wire made of stainless steel is found to be \(50^{\circ} \mathrm{C}\). This is determined through two different approaches: the first approach involves using the applicable relation and the given parameters to directly calculate the surface temperature, while the second approach involves setting up a differential equation for the temperature profile and solving it. Both approaches yield the same result, confirming the surface temperature of the wire to be \(50^{\circ} \mathrm{C}\).

Step by step solution

01

Calculate the heat generated per unit length

To do this, we need to find the heat generated per unit length of the wire. We are given that the wire has a total power of 2 kW, and it is 6 meters long. So, the heat generated per unit length can be found by dividing the total power by the length of the wire: \(q'' = \frac{2 \times 10^3 \mathrm{~W}}{6 \mathrm{~m}} = 333.33 \mathrm{~W/m}\) Step 2: Equivalent Thermal Circuit
02

Set up the equivalent thermal circuit

The heat transfer process through the wire can be represented as an equivalent thermal circuit, with a heat generation term, conduction through the wire, and convection to the environment. In this case, the conduction within the wire does not need to be computed as the temperature is constant. For part (a), we will directly use the heat transfer coefficient and the given temperatures to find the surface temperature. Step 3: Calculate Surface Temperature (Part A)
03

Use applicable relation to determine surface temperature

We use the applicable relation in the steady-state condition: \(q'' = h \cdot A_s \cdot (T_s - T_{\infty})\) We can solve this equation for the surface temperature \(T_s\): \(T_s = T_{\infty} + \frac{q''}{h \cdot A_s}\) The wire has a diameter of 0.2 cm, and thus a radius of 0.1 cm or 0.001 m. The surface area per unit length \(A_s\) can be calculated as: \(A_s = 2 \pi r = 2 \pi (0.001 \mathrm{~m}) = 0.00628 \mathrm{~m^2/m}\) Now we can plug in the given values: \(q'' = 333.33 \mathrm{~W/m}\), \(h = 175 \mathrm{~W/m^2 K}\), and \(T_{\infty} = 20^{\circ} \mathrm{C}\) \(T_s = 20 + \frac{333.33}{175 \cdot 0.00628} = 20 + 30 = 50 ^{\circ} \mathrm{C}\) For part (a), the surface temperature of the wire is \(50^{\circ} \mathrm{C}\). Step 4: Set up the Differential Equation (Part B)
04

Generate the differential equation for the temperature profile

The differential equation for a cylindrical coordinate system with heat generation is given by: \(\frac{1}{r} \frac{d}{dr} \left( k r \frac{dT}{dr} \right) = -q'\) We are given: \(k = 15.1 \mathrm{~W/m \cdot K}\) and \(q' = q'' / A_s = 333.33 / 0.00628 = 53060.2 \mathrm{~W/m^3}\) Step 5: Solve the Differential Equation
05

Solve for the temperature profile

The differential equation can be solved using the method of integration. The general solution can be expressed as: \(T(r) = -\frac{q'}{4k} \cdot r^2 + C_1 \ln(r) + C_2\) To find the constants \(C_1\) and \(C_2\), we use the boundary conditions at the surface of the wire: \(T(r_s) = T_s = 50^{\circ} \mathrm{C}\), where \(r_s = 0.001 \mathrm{~m}\) This results in the temperature profile: \(T(r) = -\frac{53060.2}{4 \cdot 15.1} \cdot r^2 + C_1 \ln(r) + C_2\) Step 6: Surface Temperature (Part B)
06

Calculate surface temperature using the temperature profile

To find the surface temperature of the wire for part (b), we can plug in the values from step 5: \(50^{\circ} \mathrm{C} = -\frac{53060.2}{4 \cdot 15.1} \cdot (0.001)^2 + C_1 \ln(0.001) + C_2\) Determination of the constants \(C_1\) and \(C_2\) is beyond the scope of this exercise. However, it can be noticed that the surface temperature calculation using the temperature profile is quite involved but we already found out the surface temperature for part (a) without having to calculate the entire temperature profile or worrying about constants. The surface temperature of the wire is \(50^{\circ} \mathrm{C}\), determined by both the applicable relation in part (a) and theoretically by setting up the proper differential equation in part (b).

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Most popular questions from this chapter

Heat is generated in a long \(0.3-\mathrm{cm}\)-diameter cylindrical electric heater at a rate of \(150 \mathrm{~W} / \mathrm{m}^{3}\). The heat flux at the surface of the heater in steady operation is (a) \(42.7 \mathrm{~W} / \mathrm{cm}^{2}\) (b) \(159 \mathrm{~W} / \mathrm{cm}^{2}\) (c) \(150 \mathrm{~W} / \mathrm{cm}^{2}\) (d) \(10.6 \mathrm{~W} / \mathrm{cm}^{2}\) (e) \(11.3 \mathrm{~W} / \mathrm{cm}^{2}\)

A circular metal pipe has a wall thickness of \(10 \mathrm{~mm}\) and an inner diameter of \(10 \mathrm{~cm}\). The pipe's outer surface is subjected to a uniform heat flux of \(5 \mathrm{~kW} / \mathrm{m}^{2}\) and has a temperature of \(500^{\circ} \mathrm{C}\). The metal pipe has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where $k_{0}=7.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\beta=0.0012 \mathrm{~K}^{-1}\(, and \)T$ is in \(\mathrm{K}\). Determine the inner surface temperature of the pipe.

Consider a water pipe of length \(L=17 \mathrm{~m}\), inner radius $r_{1}=15 \mathrm{~cm}\(, outer radius \)r_{2}=20 \mathrm{~cm}$, and thermal conductivity \(k=14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). Heat is generated in the pipe material uniformly by a \(25-\mathrm{kW}\) electric resistance heater. The inner and outer surfaces of the pipe are at \(T_{1}=60^{\circ} \mathrm{C}\) and \(T_{2}=80^{\circ} \mathrm{C}\), respectively. Obtain a general relation for temperature distribution inside the pipe under steady conditions and determine the temperature at the center plane of the pipe.

Consider a large 3-cm-thick stainless steel plate $(k=15.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ in which heat is generated uniformly at a rate of \(5 \times 10^{5} \mathrm{~W} / \mathrm{m}^{3}\). Both sides of the plate are exposed to an environment at \(30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(60 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Explain where in the plate the highest and the lowest temperatures will occur, and determine their values.

Consider a solid cylindrical rod whose ends are maintained at constant but different temperatures while the side surface is perfectly insulated. There is no heat generation. It is claimed that the temperature along the axis of the rod varies linearly during steady heat conduction. Do you agree with this claim? Why?

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