Chapter 4: Problem 3
In what medium is the lumped system analysis more likely to be applicable: in water or in air? Why?
Chapter 4: Problem 3
In what medium is the lumped system analysis more likely to be applicable: in water or in air? Why?
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Get started for freeA 30-cm-diameter, 4-m-high cylindrical column of a house made of concrete $\left(k=0.79 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=5.94 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right.\(, \)\rho=1600 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=0.84 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}$ ) cooled to \(14^{\circ} \mathrm{C}\) during a cold night is heated again during the day by being exposed to ambient air at an average temperature of \(28^{\circ} \mathrm{C}\) with an average heat transfer coefficient of $14 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$. Using the analytical one-term approximation method, determine \((a)\) how long it will take for the column surface temperature to rise to \(27^{\circ} \mathrm{C}\), (b) the amount of heat transfer until the center temperature reaches to \(28^{\circ} \mathrm{C}\), and \((c)\) the amount of heat transfer until the surface temperature reaches \(27^{\circ} \mathrm{C}\).
The Biot number can be thought of as the ratio of (a) the conduction thermal resistance to the convective thermal resistance (b) the convective thermal resistance to the conduction thermal resistance (c) the thermal energy storage capacity to the conduction thermal resistance (d) the thermal energy storage capacity to the convection thermal resistance (e) none of the above
In a production facility, 3-cm-thick large brass plates $\left(k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.$, and \(\alpha=33.9 \times\) \(10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) that are initially at a uniform temperature of \(25^{\circ} \mathrm{C}\) are heated by passing them through an oven maintained at \(700^{\circ} \mathrm{C}\). The plates remain in the oven for a period of \(10 \mathrm{~min}\). Taking the convection heat transfer coefficient to be $h=80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the surface temperature of the plates when they come out of the oven. Solve this problem using the analytical one-term approximation method. Can this problem be solved using lumped system analysis? Justify your answer.
A large cast iron container \((k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=1.70 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\) ) with \(4-\mathrm{cm}\)-thick walls is initially at a uniform temperature of \(0^{\circ} \mathrm{C}\) and is filled with ice at \(0^{\circ} \mathrm{C}\). Now the outer surfaces of the container are exposed to hot water at $55^{\circ} \mathrm{C}$ with a very large heat transfer coefficient. Determine how long it will be before the ice inside the container starts melting. Also, taking the heat transfer coefficient on the inner surface of the container to be $250 \mathrm{~W} / \mathrm{m}^{2}\(, \)\mathrm{K}$, determine the rate of heat transfer to the ice through a \(1.2-\mathrm{m}\)-wide and \(2-\mathrm{m}\)-high section of the wall when steady operating conditions are reached. Assume the ice starts melting when its inner surface temperature rises to $0.1^{\circ} \mathrm{C}$.
How can we use the one-term approximate solutions when the surface temperature of the geometry is specified instead of the temperature of the surrounding medium and the convection heat transfer coefficient?
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