Chapter 9: Problem 5
What is buoyancy force? Compare the relative magnitudes of the buoyancy force acting on a body immersed in these mediums: \((a)\) air, \((b)\) water, \((c)\) mercury, and \((d)\) an evacuated chamber.
Chapter 9: Problem 5
What is buoyancy force? Compare the relative magnitudes of the buoyancy force acting on a body immersed in these mediums: \((a)\) air, \((b)\) water, \((c)\) mercury, and \((d)\) an evacuated chamber.
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Get started for freeConsider a horizontal \(0.7\)-m-wide and \(0.85\)-m-long plate in a room at \(30^{\circ} \mathrm{C}\). Top side of the plate is insulated while the bottom side is maintained at \(0^{\circ} \mathrm{C}\). The rate of heat transfer from the room air to the plate by natural convection is (a) \(36.8 \mathrm{~W}\) (b) \(43.7 \mathrm{~W}\) (c) \(128.5 \mathrm{~W}\) (d) \(92.7 \mathrm{~W}\) (e) \(69.7 \mathrm{~W}\) (For air, use \(k=0.02476 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7323, v=\) \(\left.1.470 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\)
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 \(30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\), 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?
What does the effective conductivity of an enclosure represent? How is the ratio of the effective conductivity to thermal conductivity related to the Nusselt number?
During a plant visit, it was observed that a \(1.5-\mathrm{m}\)-high and \(1-m\)-wide section of the vertical front section of a natural gas furnace wall was too hot to touch. The temperature measurements on the surface revealed that the average temperature of the exposed hot surface was \(110^{\circ} \mathrm{C}\), while the temperature of the surrounding air was \(25^{\circ} \mathrm{C}\). The surface appeared to be oxidized, and its emissivity can be taken to be \(0.7\). Taking the temperature of the surrounding surfaces to be \(25^{\circ} \mathrm{C}\) also, determine the rate of heat loss from this furnace. The furnace has an efficiency of 79 percent, and the plant pays \(\$ 1.20\) per therm of natural gas. If the plant operates \(10 \mathrm{~h}\) a day, 310 days a year, and thus \(3100 \mathrm{~h}\) a year, determine the annual cost of the heat loss from this vertical hot surface on the front section of the furnace wall.
A 15 -cm-wide and 18-cm-high vertical hot surface in \(20^{\circ} \mathrm{C}\) air is to be cooled by a heat sink with equally spaced fins of rectangular profile. The fins are \(0.1 \mathrm{~cm}\) thick, \(4 \mathrm{~cm}\) wide, and \(18 \mathrm{~cm}\) long in the vertical direction. Determine the optimum fin spacing and the rate of heat transfer by natural convection from the heat sink if the base temperature is \(85^{\circ} \mathrm{C}\).
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