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+clear;
+clc;
+printf('FUNDAMENTALS OF HEAT AND MASS TRANSFER \n Incropera / Dewitt / Bergman / Lavine \n EXAMPLE 9.2 Page 572 \n'); //Example 9.2
+// Heat transfer by convection between screen and room air.
+
+//Operating Conditions
+Ts = 232+273; //[K] Surface Temperature
+Tsurr = 23+273; //[K] Surrounding Temperature
+L = .71; //[m] length
+w = 1.02; //[m] Width
+
+//Table A.4 Air Properties T = 400 K
+k = 33.8*10^-3 ;//[W/m.K]
+uv = 26.4*10^-6 ;//[m^2/s] Kinematic Viscosity
+al = 38.3*10^-6 ;//[m^2/s]
+be = 2.5*10^-3 ;//[K^-1] Tf^-1
+Pr = .69 ;// Prandtl number
+g = 9.81 ;//[m^2/s] gravitational constt
+
+Ra = g*be*(Ts-Tsurr)/al*L^3/uv;
+printf("\n\n As the Rayleigh Number is %.2e the free convection boundary layer is turbulent",Ra);
+//From equatiom 9.23
+Nu = [.825 + .387*Ra^.16667/[1+(.492/Pr)^(9/16)]^(8/27)]^2;
+h = Nu*k/L;
+q = h*L*w*(Ts-Tsurr);
+
+printf("\n Heat transfer by convection between screen and room air is %i W",q);
+//END \ No newline at end of file