A two-layer wall is made of two metal plates, with surface roughness of about \(25 \mu \mathrm{m}\), pressed together at an average pressure of \(10 \mathrm{MPa}\). The first layer is a stainless steel plate with a thickness of \(5 \mathrm{~mm}\) and a thermal conductivity of \(14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The second layer is an aluminum plate with a thickness of \(15 \mathrm{~mm}\) and a thermal conductivity of \(237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). On the stainless steel side of the wall, the surface is subjected to a heat flux of \(800 \mathrm{~W} / \mathrm{m}^{2}\). On the aluminum side of the wall, the surface experiences convection heat transfer at an ambient temperature of \(20^{\circ} \mathrm{C}\), where the convection coefficient is \(12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the surface temperature of the stainless steel plate.

Short Answer

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Based on the given information and the four-step solution, calculate the surface temperature of the stainless steel plate. Given: Thickness of Stainless Steel: 5 mm Thermal Conductivity of Stainless Steel: 14 W/m·K Thickness of Aluminum: 15 mm Thermal Conductivity of Aluminum: 237 W/m·K Heat Flux: 800 W/m² Convective Heat Transfer Coefficient: 12 W/m²·K Ambient Temperature: 20°C

Step by step solution

01

Calculate the resistance of each layer

Start by calculating the thermal resistance of each layer. This can be found using the equation: \(R = \dfrac{L}{k A}\) where \(R\) is the thermal resistance, \(L\) is the thickness of the layer, \(k\) is the thermal conductivity, and \(A\) is the surface area. In this case, we will assume the surface area is the same for both layers. The resistance of stainless steel, \(R_1\), and aluminum, \(R_2\), can be calculated as follows: \(R_1 = \dfrac{5 \times 10^{-3}~\mathrm{m}}{14~\mathrm{W/m \cdot K} A}\) \(R_2 = \dfrac{15 \times 10^{-3}~\mathrm{m}}{237~\mathrm{W/m \cdot K} A}\)
02

Calculate total resistance of the system

To find the total thermal resistance of the system, add the resistance of the stainless steel layer, the resistance of the aluminum layer, and the convective resistance: \(R_{total} = R_1 + R_2 + R_{conv}\) The convective resistance, \(R_{conv}\), can be calculated as: \(R_{conv} = \dfrac{1}{h A}\) where \(h\) is the convection heat transfer coefficient. Thus, we get: \(R_{conv} = \dfrac{1}{12~\mathrm{W/m^2 \cdot K} A}\) Now, we can calculate the total resistance: \(R_{total} = \dfrac{5 \times 10^{-3}~\mathrm{m}}{14~\mathrm{W/m \cdot K} A} + \dfrac{15 \times 10^{-3}~\mathrm{m}}{237~\mathrm{W/m \cdot K} A} + \dfrac{1}{12~\mathrm{W/m^2 \cdot K} A}\)
03

Determine the heat flux through the system

The heat flux, \(q\), through the system is given, which is \(800 \mathrm{~W} / \mathrm{m}^{2}\). To find the temperature difference between the surface of the stainless steel plate and the ambient temperature, we can use the following equation: \(\Delta T = q \times R_{total}\) Substitute \(q\) and \(R_{total}\) in the equation to get the temperature difference: \(\Delta T = 800~\mathrm{W/m^2} \left(\dfrac{5 \times 10^{-3}~\mathrm{m}}{14~\mathrm{W/m \cdot K} A} + \dfrac{15 \times 10^{-3}~\mathrm{m}}{237~\mathrm{W/m \cdot K} A} + \dfrac{1}{12~\mathrm{W/m^2 \cdot K} A}\right)\) Solve for \(\Delta T\): \(\Delta T = 9.52~\mathrm{K}\)
04

Determine the surface temperature of the stainless steel plate

Since we know the temperature difference \(\Delta T\) between the stainless steel surface and the aluminum surface and the ambient temperature is given as \(20^{\circ} \mathrm{C}\), we can find the surface temperature of the stainless steel plate. The heat flux through the wall is in the direction of aluminum to stainless steel plate, so to find the surface temperature of the stainless steel plate, we will subtract the temperature difference from the ambient temperature: \(T_{stainless~steel} = 20^{\circ} \mathrm{C} - 9.52~\mathrm{K}\) \(T_{stainless~steel} = 10.48^{\circ} \mathrm{C}\) Thus, the surface temperature of the stainless steel plate is \(10.48^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

Consider a \(1.5\)-m-high and 2 -m-wide triple pane window. The thickness of each glass layer \((k=0.80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(0.5 \mathrm{~cm}\), and the thickness of each air space \((k=0.025 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(1 \mathrm{~cm}\). If the inner and outer surface temperatures of the window are \(10^{\circ} \mathrm{C}\) and \(0^{\circ} \mathrm{C}\), respectively, the rate of heat loss through the window is (a) \(75 \mathrm{~W}\) (b) \(12 \mathrm{~W}\) (c) \(46 \mathrm{~W}\) (d) \(25 \mathrm{~W}\) (e) \(37 \mathrm{~W}\)

A plane brick wall \((k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(10 \mathrm{~cm}\) thick. The thermal resistance of this wall per unit of wall area is (a) \(0.143 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (b) \(0.250 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (c) \(0.327 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (d) \(0.448 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (e) \(0.524 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\)

A 1.4-m-diameter spherical steel tank filled with iced water at \(0^{\circ} \mathrm{C}\) is buried underground at a location where the thermal conductivity of the soil is \(k=0.55 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The distance between the tank center and the ground surface is \(2.4 \mathrm{~m}\). For ground surface temperature of \(18^{\circ} \mathrm{C}\), determine the rate of heat transfer to the iced water in the tank. What would your answer be if the soil temperature were \(18^{\circ} \mathrm{C}\) and the ground surface were insulated?

Steam at \(450^{\circ} \mathrm{F}\) is flowing through a steel pipe \(\left(k=8.7 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\) whose inner and outer diameters are \(3.5\) in and \(4.0\) in, respectively, in an environment at \(55^{\circ} \mathrm{F}\). The pipe is insulated with 2 -in-thick fiberglass insulation \((k=\) \(\left.0.020 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\). If the heat transfer coefficients on the inside and the outside of the pipe are 30 and \(5 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\), respectively, determine the rate of heat loss from the steam per foot length of the pipe. What is the error involved in neglecting the thermal resistance of the steel pipe in calculations?

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