Chapter 1: Problem 3
How do rating problems in heat transfer differ from the sizing problems?
Chapter 1: Problem 3
How do rating problems in heat transfer differ from the sizing problems?
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Get started for freeIn the metal processing industry, heat treatment of metals is commonly done using electrically heated draw batch furnaces. Consider a furnace that is situated in a room with surrounding air temperature of \(30^{\circ} \mathrm{C}\) and an average convection heat transfer coefficient of $12 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$. The furnace front is made of a steel plate with thickness of \(20 \mathrm{~mm}\) and a thermal conductivity of $25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer furnace front surface has an emissivity of \(0.23\), and the inside surface is subjected to a heat flux of $8 \mathrm{~kW} / \mathrm{m}^{2}$. Determine the outside surface temperature of the furnace front.
An electronic package in the shape of a sphere with an outer diameter of $100 \mathrm{~mm}$ is placed in a large laboratory room. The surface emissivity of the package can assume three different values \((0.2,0.25\), and \(0.3)\). The walls of the room are maintained at a constant temperature of $77 \mathrm{~K}$. The electronics in this package can only operate in the surface temperature range of $40^{\circ} \mathrm{C} \leq T_{s} \leq 85^{\circ} \mathrm{C}\(. Determine the range of power dissipation \)(\dot{W})$ for the electronic package over this temperature range for the three surface emissivity values \((\varepsilon)\). Plot the results in terms of \(\dot{W}(\mathrm{~W})\) vs. \(T_{s}\left({ }^{\circ} \mathrm{C}\right)\) for the three different values of emissivity over a surface temperature range of 40 to \(85^{\circ} \mathrm{C}\) with temperature increments of \(5^{\circ} \mathrm{C}\) (total of 10 data points for each \(\varepsilon\) value). Provide a computer- generated graph for the display of your results, and tabulate the data used for the graph. Comment on the results obtained.
An electric current of 1 A passing through a cable The cable is covered with polyethylene insulation, and convection occurs at the outer surface of the insulation. The ambient temperature is \(20^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and the surface area subjected to the convection is \)0.1 \mathrm{~m}^{2}$. The ASTM D1351 standard specifies that thermoplastic polyethylene insulation is suitable for use on electrical cable with operation at temperatures up to \(75^{\circ} \mathrm{C}\). Under these conditions, will the polyethylene insulation for the cable meet the ASTM D1351 standard? If the polyethylene insulation does not meet the ASTM D1351 standard, then discuss possible solutions to meet the standard.
A 2-kW electric resistance heater submerged in 30-kg water is turned on and kept on for \(10 \mathrm{~min}\). During the process, \(500 \mathrm{~kJ}\) of heat is lost from the water. The temperature rise of the water is (a) \(5.6^{\circ} \mathrm{C}\) (b) \(9.6^{\circ} \mathrm{C}\) (c) \(13.6^{\circ} \mathrm{C}\) (d) \(23.3^{\circ} \mathrm{C}\) (e) \(42.5^{\circ} \mathrm{C}\)
What is a blackbody? How do real bodies differ from blackbodies?
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