Elements Of Electromagnetics
7th Edition
ISBN: 9780190698614
Author: Sadiku, Matthew N. O.
Publisher: Oxford University Press
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Write down the total thermal resistance for a double-pipe heat exchanger. Show how to convert from total resistance to an overall heat-transfer coefficient. Explain how flow regime may affect overall heat transfer rate.
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- based on a double-pipe counter flow heat exchanger to be used to cool oil that enters the heat exchanger at 300°F to 105°F at a rate of 5 lbm/s by water that enters at 70°F at a rate of 3 Ibm/s. The diameter of the tube is 1 in. and the length is 20 ft. The measured overall heat transfer coefficient of this heat exchanger is 2.14 Btu/s-ft2-°F. [Oil, c, = 0.525 Btu/lbm°F, Water, c, = 1.0 %3D Btu/lbm°F] The logarithmic mean temperature difference in °C is 46.1 cannot be determined 35.0 59.4arrow_forwardSingle - shell, two - tube pass heat exchanger with surface area 0.4 m² and overall heat transfer coefficient of 1800 W / m°K; saturated steam at 110° C condenses on one side while water at a flow rate of 0.35 kg / s enters at 17° C. Calculate ( a ) Outlet temperature of the water (b) Rate of condensation of steam . cp ( water ) = 4179 J / kg . K.arrow_forwardI am reviewing methods of assessing systems in heat transfer. One of the method I have run across for looking at single pass heat exchangers is log mean temperature difference (LMTD). What is the advantage of using LMTD instead of the basic/arithmetic difference in temperatures?arrow_forward
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