12-17 12-46 Water flows over a large plate. The rate of heat transfer per unit width of the plate is to be determined. Assumptions 1 Steady operating conditions exist. 2 The critical Reynolds number is Recr = 5u105. 3 Radiation effects are negligible. Properties The properties of water at the film temperature of (Ts + Tf)/2 = (10+43.3)/2 = 27qC are (Table A-15) U k P Pr 996.6 kg/m 3 0.610 W/m.qC Water V =30 cm/s Tf =43.3qC 0.854 u 10 3 kg//m s 5.85 Ts = 10qC L=1m Analysis (a) The Reynolds number is Re L VLU (0.3 m/s)(1.0 m)(996.6 kg/m 3 ) P 0.854 u 10 3 2 m /s 3.501u 10 5 which is smaller than the critical Reynolds number. Thus we have laminar flow for the entire plate. The Nusselt number and the heat transfer coefficient are Nu h 0.664 Re L 1 / 2 Pr 1 / 3 k Nu L 0.664(3.501u 10 5 )1 / 2 (5.85)1 / 3 0.610 W/m.qC (707.9) 1.0 m 707.9 431.8 W/m 2 .qC Then the rate of heat transfer per unit width of the plate is determined to be Q hAs (Ts Tf ) ( 431 .8 W/m 2 .qC)(1 m)(1 m)](43.3 10) qC = 14,400 W PROPRIETARY MATERIAL. © 2008 The McGraw-Hill Companies, Inc. Limited distribution permitted only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.