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+clc;
+clear all;
+disp("HT coefficient from tube")
+D=0.06;//m diameter of tube
+U=12;//m/s
+ti=15;//degree C
+to=45;//degree C
+ts=70;// degree C
+k=61.714/100;//W/m.C
+cp=4174;//J/kg.K
+v=0.805*10^(-6);// m^2/s
+rho=995.7;//kg/m^3
+Pr=5.42;
+ReL=U*D/v
+Nu=0.023*(ReL^0.8)*Pr^(1/3)
+h=Nu*k/D;
+disp("W/m^2.C",h,"heat transfer coefficiet from tube surface h =")
+m=rho*%pi/4*D^2*U;// kg/s
+Q=m*cp*(to-ti);//W
+tb=(ti+to)/2;
+disp("W",Q,"The heat transferred Q =")
+L=Q/(h*%pi*D*(ts-tb));
+disp("m",L,"The length of tube is L =")