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+//Example 2.10
+clear;
+clc;
+
+//Given
+R=8.314;// gas constant in J K^-1 mol^-1
+t1=298;// temperature in K
+p1=30000;// initial pressure in N m^-2
+p2=10000;// final pressure in N m^-2
+Cv=20.8;// heat capacity of CO at constant volume in J K^-1 mol^-1
+W=0.1;// weight of CO taken in kg
+
+// To determine t2,w,delH and delE
+Cp=Cv+R;//heat capacity at constant pressure
+n=W/0.028;//moles of CO
+t2=t1*((Cv+((p2/p1)*R))/Cp);//final temperature in K
+delE=n*Cv*(t2-t1);//change in internal energy in J
+w=delE;//work done in J
+delH=n*Cp*(t2-t1);//enthalpy change in J
+mprintf('Final Temperature = %f K',t2);
+mprintf('\n delE = %f J',delE);
+mprintf('\n delH = %f J',delH);
+mprintf('\n w = %f J',w);
+//end
+\ No newline at end of file