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Four power transistors, each dissipating \(10 \mathrm{~W}\), are mounted on a thin vertical aluminum plate $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( \)22 \mathrm{~cm} \times 22 \mathrm{~cm}$ in size. The heat generated by the transistors is to be dissipated by both surfaces of the plate to the surrounding air at \(20^{\circ} \mathrm{C}\), which is blown over the plate by a fan at a velocity of \(5 \mathrm{~m} / \mathrm{s}\). The entire plate can be assumed to be nearly isothermal, and the exposed surface area of the transistor can be taken to be equal to its base area. Determine the temperature of the aluminum plate. Evaluate the air properties at a film temperature of \(40^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\).

Short Answer

Expert verified
Answer: The temperature of the aluminum plate is approximately 30.76°C.

Step by step solution

01

Calculate the total heat dissipation

The total heat dissipation of the four power transistors can be calculated as follows: $$Q_{total} = N \cdot Q_{transistor}$$ Where, \(Q_{total}\) is the total heat dissipation, \(N\) is the number of transistors, and \(Q_{transistor}\) is the heat dissipation per transistor. Plugging in the given values: $$Q_{total} = 4 \cdot 10 \mathrm{~W} = 40 \mathrm{~W}$$
02

Determine the air properties

Evaluate the air properties at a film temperature of \(40^{\circ} \mathrm{C}\) and a pressure of \(1 \mathrm{~atm}\). For the given conditions, the following properties can be obtained from the air property tables: - Density, \(\rho = 1.127 \mathrm{~kg} / \mathrm{m}^{3}\) - Specific heat capacity, \(c_p = 1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\) - Thermal conductivity, \(k_a = 0.0271 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) - Dynamic viscosity, \(\mu = 1.966 \times 10^{-5} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\)
03

Calculate the convective heat transfer coefficient

We will first calculate the Reynolds number \(Re\) to determine the flow regime, and then use an appropriate correlation to find the convective heat transfer coefficient \(h\). Since the airflow is forced convection, we will use the Dittus-Boelter correlation for forced convections. Reynolds number is given by: $$Re = \frac{\rho V d_h}{\mu}$$ Where, - \(d_h\) is characteristic length for the forced convection over a flat plate, which can be taken as the length of the plate, given here as \(0.22 \mathrm{~m}\). - \(V\) is the air velocity of \(5 \mathrm{~m}/\mathrm{s}\). Plugging in the values, we calculate \(Re\): $$Re = \frac{1.127 \cdot 5 \cdot 0.22}{1.966 \times 10^{-5}} = 63357$$ Since \(Re > 4000\), the flow is turbulent. Next, we'll calculate the Nusselt number, which is given by the Dittus-Boelter correlation: $$Nu = 0.027 \cdot Re^{4/5} \cdot Pr^{1/3}$$ Where, \(Pr\) is the Prandtl number, which can be calculated as: $$Pr = \frac{c_p \mu}{k_a}$$ $$Pr = \frac{1007 \cdot 1.966 \times 10^{-5}}{0.0271} = 0.727$$ Plugging in the values obtained, we calculate \(Nu\): $$Nu = 0.027 \cdot 63357^{4/5} \cdot 0.727^{1/3} = 324.5$$ Now, the convective heat transfer coefficient, \(h\) can be found as follows: $$h = \frac{k_a \cdot Nu}{d_h}$$ $$h = \frac{0.0271 \cdot 324.5}{0.22} = 40.3 \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}$$
04

Calculate the temperature of the aluminum plate

We are now able to calculate the temperature of the aluminum plate, knowing the heat transfer rate and convective heat transfer coefficient. The heat transfer rate can be found by using the heat balance equation: $$Q_{total} = h \cdot A_p \cdot (T_p - T_\infty)$$ Where, \(A_p\) is the plate area, which can be calculated as \(A_p = 2 \times (0.22 \mathrm{~m} \times 0.22 \mathrm{~m}) = 0.0968 \mathrm{~m}^2\) (we consider both sides of the plate), \(T_p\) is the temperature of the plate, and \(T_\infty\) is the air temperature, given as \(20^{\circ} \mathrm{C}\). Now, solve for \(T_p\): $$T_p = T_\infty + \frac{Q_{total}}{h \cdot A_p}$$ $$T_p = 20 + \frac{40}{40.3 \cdot 0.0968}$$ $$T_p = 20 + 10.76 = 30.76^{\circ} \mathrm{C}$$ The aluminum plate's temperature is approximately \(30.76^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

In the effort to increase the removal of heat from a hot surface at \(120^{\circ} \mathrm{C}\), a cylindrical pin fin $\left(k_{f}=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right)\( with a diameter of \)5 \mathrm{~mm}$ is attached to the hot surface. Air at \(20^{\circ} \mathrm{C}\) (1 atm) is flowing across the pin fin with a velocity of \(10 \mathrm{~m} / \mathrm{s}\).

In an experiment, the local heat transfer over a flat plate was correlated in the form of the local Nusselt number as expressed by the following correlation $$ \mathrm{Nu}_{x}=0.035 \mathrm{Re}_{x}^{0.8} \mathrm{Pr}^{1 / 3} $$ Determine the ratio of the average convection heat transfer coefficient \((h)\) over the entire plate length to the local convection heat transfer coefficient \(\left(h_{x}\right)\) at \(x=L\).

Wind at \(30^{\circ} \mathrm{C}\) flows over a \(0.5\)-m-diameter spherical tank containing iced water at \(0^{\circ} \mathrm{C}\) with a velocity of $25 \mathrm{~km} / \mathrm{h}$. If the tank is thin-shelled with a high thermal conductivity material, the rate at which ice melts is (a) \(4.78 \mathrm{~kg} / \mathrm{h}\) (b) \(6.15 \mathrm{~kg} / \mathrm{h}\) (c) \(7.45 \mathrm{~kg} / \mathrm{h}\) (d) \(11.8 \mathrm{~kg} / \mathrm{h}\) (e) \(16.0 \mathrm{~kg} / \mathrm{h}\) (Take \(h_{i f}=333.7 \mathrm{~kJ} / \mathrm{kg}\), and use the following for air: $k=0.02588 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \quad \operatorname{Pr}=0.7282, \quad \nu=1.608 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\(, \)\left.\mu_{\infty}=1.872 \times 10^{-5} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, \mu_{s}=1.729 \times 10^{-5} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\right)$

Kitchen water at \(10^{\circ} \mathrm{C}\) flows over a 10 -cm-diameter pipe with a velocity of \(1.1 \mathrm{~m} / \mathrm{s}\). Geothermal water enters the pipe at \(90^{\circ} \mathrm{C}\) at a rate of \(1.25 \mathrm{~kg} / \mathrm{s}\). For calculation purposes, the surface temperature of the pipe may be assumed to be \(70^{\circ} \mathrm{C}\). If the geothermal water is to leave the pipe at \(50^{\circ} \mathrm{C}\), the required length of the pipe is (a) $1.1 \mathrm{~m}$ (b) \(1.8 \mathrm{~m}\) (c) \(2.9 \mathrm{~m}\) (d) \(4.3 \mathrm{~m}\) (e) \(7.6 \mathrm{~m}\) (For both water streams, use $k=0.631 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=4.32\(, \)\left.\nu=0.658 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}, c_{p}=4179 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$

An automotive engine can be approximated as a \(0.4\)-m-high, \(0.60\)-m-wide, and \(0.7-\mathrm{m}\)-long rectangular block. The bottom surface of the block is at a temperature of \(75^{\circ} \mathrm{C}\) and has an emissivity of \(0.92\). The ambient air is at \(5^{\circ} \mathrm{C}\), and the road surface is at \(10^{\circ} \mathrm{C}\). Determine the rate of heat transfer from the bottom surface of the engine block by convection and radiation as the car travels at a velocity of \(60 \mathrm{~km} / \mathrm{h}\). Assume the flow to be turbulent over the entire surface because of the constant agitation of the engine block. How will the heat transfer be affected when a 2 -mm-thick layer of gunk $(k=3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ has formed at the bottom surface as a result of the dirt and oil collected at that surface over time? Assume the metal temperature under the gunk is still \(75^{\circ} \mathrm{C}\).

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