Chapter 3: Problem 7
Why are the convection and the radiation resistances at a surface in parallel instead of being in series?
Chapter 3: Problem 7
Why are the convection and the radiation resistances at a surface in parallel instead of being in series?
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Get started for freeSteam at \(280^{\circ} \mathrm{C}\) flows in a stainless steel pipe $(k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ whose inner and outer diameters are \(5 \mathrm{~cm}\) and \(5.5 \mathrm{~cm}\), respectively. The pipe is covered with \(3-\mathrm{cm}\)-thick glass wool insulation $(k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(. Heat is lost to the surroundings at \)5^{\circ} \mathrm{C}$ by natural convection and radiation, with a combined natural convection and radiation heat transfer coefficient of $22 \mathrm{~W} / \mathrm{m}^{2}$. . Taking the heat transfer coefficient inside the pipe to be \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drops across the pipe shell and the insulation.
A 2.2-mm-diameter and 14-m-long electric wire is tightly wrapped with a \(1-\mathrm{mm}\)-thick plastic cover whose thermal conductivity is $k=0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Electrical measurements indicate that a current of \(13 \mathrm{~A}\) passes through the wire, and there is a voltage drop of \(8 \mathrm{~V}\) along the wire. If the insulated wire is exposed to a medium at \(T_{\infty}=30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=24 \mathrm{~W} / \mathrm{m}^{2}\), \(\mathrm{K}\), determine the temperature at the interface of the wire and the plastic cover in steady operation. Also determine if doubling the thickness of the plastic cover will increase or decrease this interface temperature.
A 5 -m-diameter spherical tank is filled with liquid oxygen $\left(\rho=1141 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=1.71 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\right)\( at \)-184^{\circ} \mathrm{C}$. It is observed that the temperature of oxygen increases to \(-183^{\circ} \mathrm{C}\) in a 144-hour period. The average rate of heat transfer to the tank is (a) \(124 \mathrm{~W}\) (b) \(185 \mathrm{~W}\) (c) \(246 \mathrm{~W}\) (d) \(348 \mathrm{~W}\) (e) \(421 \mathrm{~W}\)
Consider a very long rectangular fin attached to a flat surface such that the temperature at the end of the fin is essentially that of the surrounding air, i.e., \(20^{\circ} \mathrm{C}\). Its width is \(5.0 \mathrm{~cm}\); thickness is \(1.0 \mathrm{~mm}\); thermal conductivity is $200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(; and base temperature is \)40^{\circ} \mathrm{C}$. The heat transfer coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2}\). . Estimate the fin temperature at a distance of \(5.0 \mathrm{~cm}\) from the base and the rate of heat loss from the entire fin.
Consider a house with a flat roof whose outer dimensions are $12 \mathrm{~m} \times 12 \mathrm{~m}\(. The outer walls of the house are \)6 \mathrm{~m}$ high. The walls and the roof of the house are made of 20 -cm-thick concrete $(k=0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The temperatures of the inner and outer surfaces of the house are \(15^{\circ} \mathrm{C}\) and $3^{\circ} \mathrm{C}$, respectively. Accounting for the effects of the edges of adjoining surfaces, determine the rate of heat loss from the house through its walls and the roof. What is the error involved in ignoring the effects of the edges and corners and treating the roof as a $12-\mathrm{m} \times 12-\mathrm{m}\( surface and the walls as \)6-\mathrm{m} \times 12-\mathrm{m}$ surfaces for simplicity?
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