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+clc;
+clear all;
+disp("heat loss per meter")
+r1=150/2;//mm inner radius of a steam pipe
+r2=160/2;//mm layer 1 radius of a steam pipe
+r3=r2+30;// mm layer 2 radius of steam pipe
+r4=r3+50;// mm outer radius of pipe
+t1=320;// degree C
+t4=40;// degree C
+kA=58;//W/(m*C)
+kB=0.18;//W/(m*C)
+kC=0.09;//W/(m*C)
+
+Q=2*3.1416*(t1-t4)/(log (r2/r1)/kA+log (r3/r2)/kB+log (r4/r3)/kC);
+disp("W",Q,"heat lost per meter =")
+
+//Q=2*3.1416*(t1-t2)/(log (r2/r1)/kA);
+X=2*3.1416/(log (r2/r1)/kA);
+t2=t1-Q/X;
+disp("degree C",t2,"temperature t2 =")
+
+//Q=2*3.1416*(t2-t3)/(log (r3/r2)/kB);
+X=2*3.1416/(log (r3/r2)/kB);
+t3=t2-Q/X;
+disp("degree C",t3,"temperature t3 =")
+
+hsteam=2703;//kJ/kg total heat pf steam when it is saturated at 320 degree C
+m=0.32;//kg/min
+Qsteam=m*hsteam-Q*60/1000;// kJ/min
+disp("kJ/min",Qsteam,"steam carried by steam per minute after losing heat in the pipe = ")
+
+//Qsteam=m*(hf+x*hfg)
+hf=1463;//kJ/kg
+hfg=1240;//kJ/kg
+x=((Qsteam/m)-hf)/hfg;
+disp(x,"amount of steam coming out of one meter pipe =")
+