(1) Consider a large plane wall of thickness L = 0.3, thermal conductivity k = 2.5...

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(1) Consider a large plane wall of thickness L = 0.3, thermal conductivity k = 2.5 W/m C, and surface area A = 1 m. (6) Saturated steam at 365 K condenses on a 2-cm tube whose surface is maintained at 340 K. Determine the rate of condensation and the heat transfer coefficient for the case of a 3-m-long tube oriented horizontally. If seven tubes of the same size and surface temperature are arranged in a vertical bank and the flow is assumed laminar, determine the individual heat transfer coefficient of the 6th tube (counted from the top) for a 7-pipe network. The following properties of steam and water may be used in your calculations. At T = 365 K, hfg = 2250000 J/kg, p = 0.586 kg/m. At T = 352.5 K, p = 971 kg/m, k = 0.673 W/mK, C = 4194 J/kgK, = 0.000352 Pa's. State your assumptions, if any. Startyour answerfor part(1) here (1) Consider a large plane wall of thickness L = 0.3, thermal conductivity k = 2.5 W/m C, and surface area A = 1 m. (6) Saturated steam at 365 K condenses on a 2-cm tube whose surface is maintained at 340 K. Determine the rate of condensation and the heat transfer coefficient for the case of a 3-m-long tube oriented horizontally. If seven tubes of the same size and surface temperature are arranged in a vertical bank and the flow is assumed laminar, determine the individual heat transfer coefficient of the 6th tube (counted from the top) for a 7-pipe network. The following properties of steam and water may be used in your calculations. At T = 365 K, hfg = 2250000 J/kg, p = 0.586 kg/m. At T = 352.5 K, p = 971 kg/m, k = 0.673 W/mK, C = 4194 J/kgK, = 0.000352 Pa's. State your assumptions, if any. Startyour answerfor part(1) here