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+
+clc
+clear
+//Input data
+ws=64;//The steam flow rate in kg/s
+p=60;//The pressure at which steam leaves the boiler in bar
+m=0.02;//Moisture contant in the steam
+wf=62;//The feedwater flow rate in kg/s
+Pf=3;//concentration of feedwater in ppm
+wm=2;//The flow rate of makeup water
+Pm=50;//concentration of makeup water in ppm
+Ps=5;//Leaving the drum water in ppm
+Pw=1000;//The concentration in the drum water in ppm
+mf=7;//The fuel burning rate in kg/m
+CV=23;//The heating value in MJ/kg
+ta=30;//The room temperature in degree centigrade
+hf=1213.35;//Enthalpy of saturated liquid at 60 bar in kJ/kg
+ha=125.79;//Enthalpy at ambient temperature in kJ/kg
+
+//Calculations
+BD=[(wf*Pf)+(wm*Pm)-(m*ws*Ps)]/1000;//The rate of blowdown in kg/s
+E=[(BD*(hf-ha))/(mf*CV*1000)]*100;//The energy loss in blowdown in percentage
+S=m*ws*Ps*10^-6*3600*24;//Scale deposition in superheater tubes
+
+//Output
+printf('(a)The blowdown required = %3.4f kg/s \n (b) Heat loss in blowdown as a percentage of total heat released in the furnace = %3.2f percentage \n (c) The deposition of scale in superheater tube = %3.3f kg/day ',BD,E,S)