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diff --git a/1808/CH3/EX3.32/Chapter3_Exampl32.sce b/1808/CH3/EX3.32/Chapter3_Exampl32.sce
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+clc
+clear
+//INPUT DATA
+cp=1.005;//specific pressure
+cv=0.718;//specific volume
+R=0.287;//gas constant
+p1=100;//pressure in kPa
+t1=300;//temperature in K
+t3=1500;//temperature in K
+g=1.4;//constant
+v1=6;//volume in m^3/s
+Rp=10;//compression ratio
+
+//CALCULATIONS
+wn=cp*(1-((1/(Rp^((g-1)/g)))))*(t3-t1*(Rp^((g-1)/g)));//Net work done in kJ/kg
+t2=t1*(Rp^((g-1)/g));//temperature in K
+ng=(wn/(cp*(t3-t2)))*100;//Thermal efficiency in percentage
+t4=t3/(Rp^((g-1)/g));//temperature in K
+Rw=((cp*(t2-t1))/(cp*(t3-t4)))*100;//back work ratio
+m=p1*v1/(R*t1);//mass flow rate in kg/s
+P=m*wn;//Power developed in kW
+
+//OUTPUT
+printf('(i))Thermal efficiency is %3.2f percentage \n(ii)The back work ratio is %3.1f percentage \n(iii)Power developed is %3.1f kW',ng,Rw,P)
+
+