To calculate the total entropy generation for the process you've described, we need to follow a series of steps. Let's start with the calculation and then move on to the qualitative drawing of the process in a p-v (pressure-volume) diagram.
### Calculation of Total Entropy Generation
- Determine Initial and Final States:
- Initial State: R-410A with a quality of x = 0.25% at Tinitial = -20oC So νinitial=0.013627 m3/Kg Hinitial=76.97 KJ/Kg and Sinitial=0.3079 KJ/kg-K and considering 0.1kg for the mass, the initial volume will be 0.001363 m3.
- Final State: R-410A with Tfinal = 20oC and the volume is 3 times the initial volume, so the final volume is 0.004088 m3 and specific volume of final will be 0.040881 m3/kg which is more than saturated specific volume, so R-410A is at superheat condition. Now, we need to interpolate and find the fluid condition by interpolation and find the final pressure and final entropy and final enthalpy of the fluid.
At saturation, pressure is 1444.2 kPa at T=20oC. and specific volume of saturated vapor is 0.01758 m3/kg. at T=20oC and pressure of 600kPa, the specific volume is 0.05106 m3/kg.
Our final specific volume is 0.040881 m3/kg and by linear interpolation we can find
Pfinal=(0.040881-0.01758)*((600-1444.2)/(0.05106-0.01758))+1444.2=856.664 kPa
This way we can find the final state enthalpy and entropy as
Hfinal=297.922
Sfinal=1.1069
So change in entropy is Mass*(Sfinal-Sinitial)=0.1*(1.1069-0.3079)=0.0799 kJ/kg
The total heat transferred is the change in enthalpy which is m*(Hfinal-Hinitial)=0.1*(297.922-76.97)=22.0952 kJ and the temperature of the heat source is 50oC or 323.15K.
so the generated entropy is delta S-Q/Tsource=0.0799-22.0952/323.15=0.011526 kJ/K
### Qualitative p-v Diagram