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authorpriyanka2015-06-24 15:03:17 +0530
committerpriyanka2015-06-24 15:03:17 +0530
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+clc;clear;
+//Example 3.5
+
+//given values
+m=4;
+V=80/1000;//converting into m^3
+P=160;
+
+//Values from Table A-12
+vf=0.0007437;
+vg=0.12348;
+T=-15.60;
+hf=31.21;
+hfg=209.90;
+
+//caluclation
+v=V/m;
+//vg>v>vf therefore it is a saturated mix
+//hence temp will same as saturation temp
+disp(T,'the temperature in celcius')
+x=(v-vf)/(vg-vf);//x=vg/vfg i.e the dryness fraction
+disp(x,'the quality');
+h=hf+x*hfg;
+disp(h,'the enthalpy of the refrigerant in kJ/kg');
+mg=x*m;
+Vg=mg*vg;
+disp(Vg,'the volume occupied by the vapor phase in m^3')