A tiny reheating furnace wall contains 200 mm of firebrick. The internal surface of the wall is at a temperature of 320 ℃ and the out of doorways temperature is 25 ℃ Calculate the drag at which the warmth is transferred, by conduction, thru a unit residing of the wall. The thermal conductivity of the firebrick worn can even be taken as 1.4 W m-1K-1. If the out of doorways surface residing of the furnace is 80 m2 estimate the warmth losses thru the furnace wall per hour. A pipe carrying superheated steam at 300 °C has an exterior diameter of 150 mm and is lagged with two layers of insulating topic cloth. The foremost layer (adjoining to the outer pipe wall) is 20 mm thick and has a thermal conductivity of 0.049 W m-1 K-1. The second layer (covering the foremost layer) is 25 mm thick, has a thermal conductivity of 0.063 W m-1 K-1 and an exterior temperature of 25 °C. Estimate the drag of heat loss per metre dimension of pipe (mediate the thermal resistance of the pipe wall is negligible). The Grashof and Reynolds numbers appear in most correlations of experimental recordsdata for convective warmth transfer. Display veil, in a most of 150 phrases, the mechanisms of pure and compelled convection with particular reference to the above nondimensional teams.
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