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+clc;
+clear all;
+disp("heat transfer coefficient")
+n=625;// number of tubes
+N=n^0.5;
+d=0.006;//m diameter
+ts=25;// degree C
+tsat=54;//degree C
+rhol=992;//kg/m^3
+mu=663*10^(-6);// Ns/m^2
+k=0.631;// W/m.C
+rhov=0.098;// kg/m^3
+hfg=2373*10^3;// J/kg
+g=9.81;//m/s
+h=0.725*(rhol*(rhol-rhov)*k^3*g*hfg/(N*mu*d*(tsat-ts)))^0.25;
+disp("W/m^2.C",h,"The heat transfer coefficient =")
+ml=h*%pi*d*(tsat-ts)/hfg;//kg/s
+m=n*ml;
+disp("kg/s.m",m,"rate of condensation of steam for complete array =")