Heat is to be conducted along a circuit board that has a copper layer on one side. The circuit board is \(15 \mathrm{~cm}\) long and \(15 \mathrm{~cm}\) wide, and the thicknesses of the copper and epoxy layers are \(0.1 \mathrm{~mm}\) and \(1.2 \mathrm{~mm}\), respectively. Disregarding heat transfer from side surfaces, determine the percentages of heat conduction along the copper \((k=386 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) and epoxy \((k=0.26 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) layers. Also determine the effective thermal conductivity of the board.

Short Answer

Expert verified
Answer: The percentage of heat conduction along the copper layer is approximately 99.93% and along the epoxy layer is approximately 0.067%. The effective thermal conductivity of the board is approximately 385.7 W/m·K.

Step by step solution

01

Calculate the area of the board

To calculate the area of the board, we have the length and the width. The area can be calculated using the formula: $$A = length \times width$$ Given length and width are both \(15 cm\), converting to meters: $$A = 0.15 \mathrm{~m} \times 0.15 \mathrm{~m} = 0.0225 \mathrm{~m}^2$$
02

Calculate heat transfer rates for copper and epoxy layers

We will use Fourier's Law of heat conduction to calculate the heat transfer rate for both the copper and epoxy layers. We will assume the same temperature gradient for both layers since we are disregarding heat transfer from side surfaces. For copper: $$q_{Cu} = -k_{Cu} \cdot A \frac{dT}{dx}$$ For epoxy: $$q_{Epoxy} = -k_{Epoxy} \cdot A \frac{dT}{dx}$$ Dividing \(q_{Cu}\) by \(q_{Epoxy}\): $$\frac{q_{Cu}}{q_{Epoxy}} = \frac{k_{Cu}}{k_{Epoxy}}$$ Given values of \(k_{Cu} = 386 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(k_{Epoxy} = 0.26 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\): $$\frac{q_{Cu}}{q_{Epoxy}} = \frac{386}{0.26} = 1484.62$$ Since \(q_{Cu} + q_{Epoxy} = 1\), the fraction of heat conduction along copper and epoxy layers is given by: $$q_{Cu} = \frac{1484.62}{1484.62 + 1} \times 100\%$$ $$q_{Epoxy} = \frac{1}{1484.62 + 1} \times 100\%$$
03

Calculate the percentage of heat conduction

With the calculated values for \(q_{Cu}\) and \(q_{Epoxy}\), we can find the percentages for heat conduction along the copper and epoxy layers: $$q_{Cu} \approx 99.93\%$$ $$q_{Epoxy} \approx 0.067\%$$
04

Calculate the effective thermal conductivity

To find the effective thermal conductivity of the board, we use the formula for heat transfer rates: $$q_{eff} = -k_{eff} \cdot A \frac{dT}{dx}$$ Since \(q_{eff} = q_{Cu} + q_{Epoxy}\): $$q_{eff} = -k_{Cu} \cdot A \frac{dT}{dx} + -k_{Epoxy} \cdot A \frac{dT}{dx}$$ $$k_{eff} = \frac{q_{eff}}{A \frac{dT}{dx}}$$ Using the values found in the previous steps: $$k_{eff} \approx \frac{q_{Cu} \times k_{Cu} + q_{Epoxy} \times k_{Epoxy}}{A \frac{dT}{dx}}$$ However, the term \(A \frac{dT}{dx}\) is the same for both copper and epoxy layers, so it cancels out in the equation leaving: $$k_{eff} \approx q_{Cu} \times k_{Cu} + q_{Epoxy} \times k_{Epoxy}$$ Using the previously calculated values: $$k_{eff} \approx 0.9993 \times 386 + 0.00067 \times 0.26$$ $$k_{eff} \approx 385.7 \,\mathrm{W} / \mathrm{m} \cdot \mathrm{K}$$ Therefore, the effective thermal conductivity of the board is approximately \(385.7 \,\mathrm{W} / \mathrm{m} \cdot \mathrm{K}\).

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Most popular questions from this chapter

We are interested in steady state heat transfer analysis from a human forearm subjected to certain environmental conditions. For this purpose consider the forearm to be made up of muscle with thickness \(r_{m}\) with a skin/fat layer of thickness \(t_{s f}\) over it, as shown in the Figure P3-138. For simplicity approximate the forearm as a one-dimensional cylinder and ignore the presence of bones. The metabolic heat generation rate \(\left(\dot{e}_{m}\right)\) and perfusion rate \((\dot{p})\) are both constant throughout the muscle. The blood density and specific heat are \(\rho_{b}\) and \(c_{b}\), respectively. The core body temperate \(\left(T_{c}\right)\) and the arterial blood temperature \(\left(T_{a}\right)\) are both assumed to be the same and constant. The muscle and the skin/fat layer thermal conductivities are \(k_{m}\) and \(k_{s f}\), respectively. The skin has an emissivity of \(\varepsilon\) and the forearm is subjected to an air environment with a temperature of \(T_{\infty}\), a convection heat transfer coefficient of \(h_{\text {conv }}\), and a radiation heat transfer coefficient of \(h_{\mathrm{rad}}\). Assuming blood properties and thermal conductivities are all constant, \((a)\) write the bioheat transfer equation in radial coordinates. The boundary conditions for the forearm are specified constant temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and temperature symmetry at the centerline of the forearm. \((b)\) Solve the differential equation and apply the boundary conditions to develop an expression for the temperature distribution in the forearm. (c) Determine the temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and the maximum temperature in the forearm \(\left(T_{\max }\right)\) for the following conditions: $$ \begin{aligned} &r_{m}=0.05 \mathrm{~m}, t_{s f}=0.003 \mathrm{~m}, \dot{e}_{m}=700 \mathrm{~W} / \mathrm{m}^{3}, \dot{p}=0.00051 / \mathrm{s} \\ &T_{a}=37^{\circ} \mathrm{C}, T_{\text {co }}=T_{\text {surr }}=24^{\circ} \mathrm{C}, \varepsilon=0.95 \\ &\rho_{b}=1000 \mathrm{~kg} / \mathrm{m}^{3}, c_{b}=3600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k_{m}=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\ &k_{s f}=0.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, h_{\text {conv }}=2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}, h_{\mathrm{rad}}=5.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \end{aligned} $$

What is the difference between the fin effectiveness and the fin efficiency?

Hot water is flowing at an average velocity of \(1.5 \mathrm{~m} / \mathrm{s}\) through a cast iron pipe \((k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) whose inner and outer diameters are \(3 \mathrm{~cm}\) and \(3.5 \mathrm{~cm}\), respectively. The pipe passes through a \(15-\mathrm{m}\)-long section of a basement whose temperature is \(15^{\circ} \mathrm{C}\). If the temperature of the water drops from \(70^{\circ} \mathrm{C}\) to \(67^{\circ} \mathrm{C}\) as it passes through the basement and the heat transfer coefficient on the inner surface of the pipe is \(400 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the combined convection and radiation heat transfer coefficient at the outer surface of the pipe. Answer: \(272.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

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) \(0.524 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\)

Heat is generated steadily in a 3-cm-diameter spherical ball. The ball is exposed to ambient air at \(26^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(7.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ball is to be covered with a material of thermal conductivity \(0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The thickness of the covering material that will maximize heat generation within the ball while maintaining ball surface temperature constant is (a) \(0.5 \mathrm{~cm}\) (b) \(1.0 \mathrm{~cm}\) (c) \(1.5 \mathrm{~cm}\) (d) \(2.0 \mathrm{~cm}\) (e) \(2.5 \mathrm{~cm}\)

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