Chapter 9: Problem 111
When neither natural nor forced convection is negligible, is it correct to calculate each independently and add them to determine the total convection heat transfer?
Chapter 9: Problem 111
When neither natural nor forced convection is negligible, is it correct to calculate each independently and add them to determine the total convection heat transfer?
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Get started for freeA 4 -m-long section of a 5-cm-diameter horizontal pipe in which a refrigerant flows passes through a room at \(20^{\circ} \mathrm{C}\). The pipe is not well insulated, and the outer surface temperature of the pipe is observed to be \(-10^{\circ} \mathrm{C}\). The emissivity of the pipe surface is \(0.85\), and the surrounding surfaces are at \(15^{\circ} \mathrm{C}\). The fraction of heat transferred to the pipe by radiation is (a) \(0.24\) (b) \(0.30\) (c) \(0.37\) (d) \(0.48\) (e) \(0.58\) (For air, use $k=0.02401 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \mathrm{Pr}=0.735$, $$ \left.\nu=1.382 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right) $$
A \(0.6-\mathrm{m} \times 0.6-\mathrm{m}\) horizontal ASTM A203 B steel plate has its lower surface subjected to convection with cold, quiescent hydrogen gas at \(-70^{\circ} \mathrm{C}\). The minimum temperature suitable for the steel plate is \(-30^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A-1M). The lower plate surface has an emissivity of \(0.3\), and thermal radiation exchange occurs between the lower plate surface and the surroundings at \(-70^{\circ} \mathrm{C}\). Determine the heat addition rate necessary for keeping the lower plate surface temperature from dropping below the minimum suitable temperature.
Hot water is flowing at an average velocity of \(4 \mathrm{ft} / \mathrm{s}\) through a cast iron pipe $\left(k=30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)$ whose inner and outer diameters are \(1.0\) in and \(1.2\) in, respectively. The pipe passes through a 50 -ft-long section of a basement whose temperature is $60^{\circ} \mathrm{F}\(. The emissivity of the outer surface of the pipe is \)0.5$, and the walls of the basement are also at about \(60^{\circ} \mathrm{F}\). If the inlet temperature of the water is \(150^{\circ} \mathrm{F}\) and the heat transfer coefficient on the inner surface of the pipe is $30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$, determine the temperature drop of water as it passes through the basement. Evaluate air properties at a film temperature of \(105^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?
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?
A room is to be heated by a coal-burning stove, which is a cylindrical cavity with an outer diameter of \(50 \mathrm{~cm}\) and a height of $120 \mathrm{~cm}\(. The rate of heat loss from the room is estimated to be \)1.5 \mathrm{~kW}$ when the air temperature in the room is maintained constant at \(24^{\circ} \mathrm{C}\). The emissivity of the stove surface is \(0.85\), and the average temperature of the surrounding wall surfaces is $14^{\circ} \mathrm{C}$. Determine the surface temperature of the stove. Neglect the heat transfer from the bottom surface and take the heat transfer coefficient at the top surface to be the same as that on the side surface. The heating value of the coal is \(30,000 \mathrm{~kJ} / \mathrm{kg}\), and the combustion efficiency is 65 percent. Determine the amount of coal burned in a day if the stove operates \(14 \mathrm{~h}\) a day. Evaluate air properties at a film temperature of \(77^{\circ} \mathrm{C}\) and 1 atm pressure. Is this a good assumption?
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