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Consider a power transistor that dissipates \(0.15 \mathrm{~W}\) of power in an environment at \(30^{\circ} \mathrm{C}\). The transistor is \(0.4 \mathrm{~cm}\) long and has a diameter of \(0.5 \mathrm{~cm}\). Assuming heat to be transferred uniformly from all surfaces, determine \((a)\) the amount of heat this resistor dissipates during a \(24-\mathrm{h}\) period, in \(\mathrm{kWh} ;(b)\) the heat flux on the surface of the transistor, in \(\mathrm{W} / \mathrm{m}^{2}\); and \((c)\) the surface temperature of the resistor for a combined convection and radiation heat transfer coefficient of $18 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.

Short Answer

Expert verified
a) Heat Dissipated in 24 hours: Approximately 3.6 x 10^-3 kWh b) Heat Flux on the surface of the transistor: Approximately 2.31 x 10^4 W/m² c) Surface Temperature of the transistor: Approximately 1286 K

Step by step solution

01

Calculate the Surface Area of the Transistor

Given the dimensions of the transistor, we can model it as a cylinder. The surface area of a cylinder can be calculated as follows: Surface Area = Area of top surface + Area of bottom surface + Area of side \(r = \frac{d}{2} = \frac{0.5 \mathrm{~cm}}{2} = 0.25 \mathrm{~cm}\) (radius) \(h = 0.4 \mathrm{~cm}\) (height) Surface Area \(= 2\pi r^{2} + 2\pi rh\) Convert cm to meters: \(r = 0.0025 \mathrm{~m}\) \(h = 0.004 \mathrm{~m}\) Surface Area \(= 2\pi (0.0025)^{2} + 2\pi (0.0025)(0.004)\) Surface Area \(\approx 6.50 \times 10^{-6} \mathrm{~m}^2\)
02

Calculate the Amount of Heat Dissipated in 24 Hours

We are given the power dissipated as 0.15 W. To find the total heat dissipated in 24 hours, we can use: Heat Dissipated (kWh) \( = \frac{Power (W) \times Time (h)}{1000}\) Heat Dissipated (kWh) \( = \frac{0.15 \times 24}{1000}\approx 3.6 \times 10^{-3} \mathrm{~kWh}\)
03

Calculate the Heat Flux on the Surface of the Transistor

The heat flux can be calculated using the formula: Heat Flux (W/m²) \(=\frac{Power (W)}{Surface Area (m^2)}\) Heat Flux (W/m²) \(= \frac{0.15}{6.50 \times 10^{-6}} \approx 2.31 \times 10^{4} \mathrm{ \frac{W}{m^2}}\)
04

Calculate the Surface Temperature of the Resistor

Finally, we can determine the surface temperature of the resistor using the heat transfer coefficient: Heat Flux (W/m²) \(= h(T_{surface} - T_{environment})\) \(2.31 \times 10^{4} = 18(T_{surface} - 30)\) \(T_{surface} = \frac{2.31 \times 10^{4}}{18} + 30 \approx 1286 \mathrm{~K}\) The surface temperature of the resistor is approximately 1286 K.

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Most popular questions from this chapter

A \(2.5\)-m-high, 4-m-wide, and 20 -cm-thick wall of a house has a thermal resistance of \(0.025^{\circ} \mathrm{C} / \mathrm{W}\). The thermal conductivity of the wall is (a) \(0.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (b) \(1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (c) \(3.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (d) \(5.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (e) \(8.0 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\)

A 25-cm-diameter, 2.4-m-long vertical cylinder containing ice at $0^{\circ} \mathrm{C}$ is buried right under the ground. The cylinder is thin-shelled and is made of a high-thermal-conductivity material. The surface temperature and the thermal conductivity of the ground are \(18^{\circ} \mathrm{C}\) and $0.85 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, respectively. The rate of heat transfer to the cylinder is (a) \(37.2 \mathrm{~W}\) (b) \(63.2 \mathrm{~W}\) (c) \(158 \mathrm{~W}\) (d) \(480 \mathrm{~W}\) (e) \(1210 \mathrm{~W}\)

A 12 -m-long and 8-cm-diameter hot-water pipe of a district heating system is buried in the soil \(80 \mathrm{~cm}\) below the ground surface. The outer surface temperature of the pipe is \(60^{\circ} \mathrm{C}\). Taking the surface temperature of the earth to be \(2^{\circ} \mathrm{C}\) and the thermal conductivity of the soil at that location to be $0.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, determine the rate of heat loss from the pipe.

A mixture of chemicals is flowing in a pipe $\left(k=14 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, D_{i}=2.5 \mathrm{~cm}, D_{\rho}=3 \mathrm{~cm}\right.\(, and \)L=10 \mathrm{~m}$ ). During the transport, the mixture undergoes an exothermic reaction having an average temperature of \(135^{\circ} \mathrm{C}\) and a convection heat transfer coefficient of $150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. To prevent any incident of thermal burn, the pipe needs to be insulated. However, due to the vicinity of the pipe, there is only enough room to fit a \(2.5\)-cm-thick layer of insulation over the pipe. The pipe is situated in a plant where the average ambient air temperature is \(20^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the insulation for the pipe such that the thermal conductivity of the insulation is sufficient to maintain the outside surface temperature at \(45^{\circ} \mathrm{C}\) or lower.

Hot water is to be cooled as it flows through the tubes exposed to atmospheric air. Fins are to be attached in order to enhance heat transfer. Would you recommend attaching the fins inside or outside the tubes? Why?

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