Chapter 9: Problem 82
Why are heat sinks with closely packed fins not suitable for natural convection heat transfer, although they increase the heat transfer surface area more?
Chapter 9: Problem 82
Why are heat sinks with closely packed fins not suitable for natural convection heat transfer, although they increase the heat transfer surface area more?
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Get started for freeA spherical tank \((k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) with an inner diameter of \(3 \mathrm{~m}\) and a wall thickness of \(10 \mathrm{~mm}\) is used for storing hot liquid. The hot liquid inside the tank causes the inner surface temperature to be as high as \(100^{\circ} \mathrm{C}\). To prevent thermal burns to the people working near the tank, the tank is covered with a \(7-\mathrm{cm}\)-thick layer of insulation $(k=0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$, and the outer surface is painted to give an emissivity of \(0.35\). The tank is located in surroundings with air at $16^{\circ} \mathrm{C}$. Determine whether or not the insulation layer is sufficient to keep the outer surface temperature below \(45^{\circ} \mathrm{C}\) to prevent thermal burn hazards. Discuss ways to further decrease the outer surface temperature. Evaluate the air properties at \(30^{\circ} \mathrm{C}\) and $1 \mathrm{~atm}$ pressure. Is this a good assumption?
Contact a manufacturer of aluminum heat sinks and obtain its product catalog for cooling electronic components by natural convection and radiation. Write an essay on how to select a suitable heat sink for an electronic component when its maximum power dissipation and maximum allowable surface temperature are specified.
An average person generates heat at a rate of \(240 \mathrm{Btu} / \mathrm{h}\) while resting in a room at \(70^{\circ} \mathrm{F}\). Assuming one-quarter of this heat is lost from the head and taking the emissivity of the skin to be \(0.9\), determine the average surface temperature of the head when it is not covered. The head can be approximated as a 12 -in-diameter sphere, and the interior surfaces of the room can be assumed to be at the room temperature.
Water is boiling in a 12 -cm-deep pan with an outer diameter of $25 \mathrm{~cm}$ that is placed on top of a stove. The ambient air and the surrounding surfaces are at a temperature of \(25^{\circ} \mathrm{C}\), and the emissivity of the outer surface of the pan is \(0.80\). Assuming the entire pan to be at an average temperature of \(98^{\circ} \mathrm{C}\), determine the rate of heat loss from the cylindrical side surface of the pan to the surroundings by \((a)\) natural convection and \((b)\) radiation. (c) If water is boiling at a rate of \(1.5\) \(\mathrm{kg} / \mathrm{h}\) at \(100^{\circ} \mathrm{C}\), determine the ratio of the heat lost from the side surfaces of the pan to that by the evaporation of water. The enthalpy of vaporization of water at \(100^{\circ} \mathrm{C}\) is 2257 \(\mathrm{kJ} / \mathrm{kg}\). Answers: $46.2 \mathrm{~W}, 47.3 \mathrm{~W}, 0.099$
Consider three similar double-pane windows with air gap widths of 5,10 , and \(20 \mathrm{~mm}\). For which case will the heat transfer through the window be a minimum?
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