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+clear;
+clc;
+printf('FUNDAMENTALS OF HEAT AND MASS TRANSFER \n Incropera / Dewitt / Bergman / Lavine \n EXAMPLE 7.2 Page 417 \n'); //Example 7.2
+// Maximum Heater Power Requirement
+
+//Operating Conditions
+v = 60; //[m/s] Air velocity
+Tsurr = 25+273; //[K] Surrounding Air Temperature
+w = 1; //[m] Width of plate
+L = .05; //[m] Length of stripper
+Ts = 230+273; //[K] Surface Temp
+
+//Table A.4 Air Properties at T = 400K
+uv = 26.41*10^-6; //[m^2/s] Kinematic Viscosity
+k = .0338; //[W/m.K] Thermal COnductivity
+Pr = .690; //Prandtl number
+
+Re = v*L/uv; //Reynolds number
+
+Rexc = 5*10^5; //Transition Reynolds Number
+xc = uv*Rexc/v; //Transition Length
+printf("\n Reynolds Number based on length L = .05m is %i. \n And the transition occur at xc = %.2f m ie fifth plate",Re,xc);
+
+//For first heater
+//Correlation 7.30
+Nu1 = .664*Re^.5*Pr^.3334; //Nusselt Number
+h1 = Nu1*k/L; // Average Convection Coefficient
+q1 = h1*(L*w)*(Ts-Tsurr); // Convective Heat exchange
+
+//For first four heaters
+Re4 = 4*Re;
+L4 = 4*L;
+Nu4 = .664*Re4^.5*Pr^.3334; //Nusselt Number
+h4 = Nu4*k/L4; // Average Convection Coefficient
+
+//For Fifth heater from Eqn 7.38
+Re5 = 5*Re;
+A = 871;
+L5 = 5*L;
+Nu5 = (.037*Re5^.8-A)*Pr^.3334; //Nusselt Number
+h5 = Nu5*k/L5; // Average Convection Coefficient
+q5 = (h5*L5-h4*L4)*w*(Ts-Tsurr);
+
+//For Sixth heater from Eqn 7.38
+Re6 = 6*Re;
+L6 = 6*L;
+Nu6 = (.037*Re6^.8-A)*Pr^.3334 ; //Nusselt Number
+h6 = Nu6*k/L6 ; // Average Convection Coefficient
+q6 = (h6*L6-h5*L5)*w*(Ts-Tsurr);
+
+printf("\n\n Power requirement are \n qconv1 = %i W qconv5 = %i W qconv6 = %i W", q1,q5,q6);
+printf("\n Hence %i > %i > %i and the sixth plate has largest power requirement", q6,q1,q5);
+//END \ No newline at end of file