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+//ques5
+//calculating heat transfer per kilogram of dry air
+clear
+clc
+//1-inlet state
+//2-Exit state
+r1=0.80;//realtive humidity at state 1
+Pg1=4.246;//saturation pressure of vapour in kPa
+P1=105;//net pressure at state 1 in kPa
+P2=100;//net pressure at state 2 in kPa
+Pv1=r1*Pg1;//partial pressure of vapour in kPa
+w1=0.622*Pv1/(P1-Pv1);//humidity ratio at state 1
+r2=0.95;//relative humidity at state 2
+Pg2=1.7051;//saturation pressure of vapour in kPa
+Pv2=r2*Pg2;//partial pressure of vapour in kPa
+w2=0.622*Pv2/(P2-Pv2);//humidity ratio at state 2
+T1=30;//C
+T2=15;//C
+Cp=1.004;//specific heat of water vapour in kJ/kg
+hv2=2528.9;//enthalpy of vapourisation of vapour in kJ/kg
+hv1=2556.3;//enthalpy of vapourisation of vapour in kJ/kg
+hl2=62.99;//enthalpy of
+q=Cp*(T2-T1)+w2*hv2-w1*hv1+hl2*(w1-w2);//kJ/kg
+printf('Heat transferred per unit mass = %.2f kJ/kg of dry air',q); \ No newline at end of file