## 5 Results and Discussions
\begin{table}
\begin{tabular}{c c c c c c c c c c} \hline \hline
**State** & \(T\) & \(P\) & \(h\) & \(s\) & \(m\) & \(\epsilon_{\text{ph}}\) & \(\epsilon_{\text{ch}}\) & \(\dot{C}\) & \(c\) \\ \cline{2-10}
**Points** & **(\({}^{\circ}\)C)** & **(MPa)** & **(kJ/kg)** & **(kJ/(kg:K))** & **(kg/s)** & **(kJ/kg)** & **(kJ/kg)** & **(S/h)** & **(S/GJ)** \\ \hline
1 & 35.00 & 7.40 & 402.40 & 1.663 & 2309.66 & 216.60 & / & 26,077.65 & 14.480 \\
2 & 110.06 & 20.72 & 444.87 & 1.680 & 2309.66 & 254.09 & / & 33,328.11 & 15.775 \\
3 & 245.43 & 20.72 & 656.60 & 2.159 & 3099.68 & 322.95 & / & 57,628.04 & 15.991 \\
4 & 393.02 & 20.72 & 841.06 & 2.473 & 3099.68 & 413.97 & / & 73,239.23 & 15.855 \\
5 & 550.00 & 20.72 & 1034.63 & 2.734 & 3099.68 & 529.77 & / & 84,301.17 & 14.260 \\
6 & 433.11 & 7.40 & 906.74 & 2.763 & 3099.68 & 392.97 & / & 62,533.52 & 14.260 \\
7 & 271.71 & 7.40 & 722.28 & 2.467 & 3099.68 & 296.85 & / & 47,237.39 & 14.260 \\
8 & 132.69 & 7.40 & 564.63 & 2.133 & 3099.68 & 238.91 & / & 38,017.79 & 14.260 \\
9 & 106.60 & 7.40 & 532.82 & 2.052 & 2309.66 & 231.26 & / & 27,421.47 & 14.260 \\
10 & 50.00 & 7.40 & 447.38 & 1.806 & 2309.66 & 218.94 & / & 25,959.82 & 14.260 \\
11 & 25.00 & 0.1013 & 104.92 & 0.367 & 2485.38 & 0.00 & / & 0.00 & 0.000 \\
12 & 35.00 & 0.1013 & 146.72 & 0.505 & 2485.38 & 0.69 & / & 0.00 & 0.000 \\
13 & 35.00 & 0.1013 & 146.72 & 0.505 & 2287.10 & 0.69 & / & 0.00 & 0.000 \\
14 & 29.00 & 0.1013 & 121.64 & 0.423 & 2287.10 & 0.11 & / & 0.00 & 0.000 \\ A1 & 26.00 & 0.0034 & 2548.32 & 8.535 & 24.74 & 8.06 & 478.83 & 477.82 & 11.017 \\ A2 & 55.00 & 0.0034 & 119.31 & 0.353 & 157.07 & 2.92 & 490.90 & 3252.42 & 11.648 \\ A3 & 55.00 & 0.0158 & 119.31 & 0.353 & 157.07 & 2.92 & 490.90 & 3252.71 & 11.649 \\ A4 & 91.60 & 0.0158 & 197.37 & 0.578 & 157.07 & 13.76 & 509.19 & 3462.53 & 11.710 \\ A5 & 60.00 & 0.0034 & 190.79 & 0.387 & 132.32 & 3.41 & 628.81 & 3535.42 & 11.739 \\ A6 & 60.00 & 0.0158 & 190.79 & 0.386 & 132.32 & 3.42 & 628.81 & 3535.42 & 11.739 \\ A7 & 110.00 & 0.0158 & 283.45 & 0.646 & 132.32 & 18.84 & 649.17 & 3735.49 & 11.739 \\ A8 & 110.00 & 0.0158 & 2705.90 & 8.288 & 24.74 & 239.39 & 478.83 & 653.86 & 10.221 \\ A9 & 55.00 & 0.0158 & 230.26 & 0.768 & 24.74 & 5.83 & 478.83 & 441.23 & 10.221 \\ A10 & 26.00 & 0.0034 & 230.26 & 0.787 & 24.74 & 0.31 & 478.83 & 441.23 & 10.338 \\ H1 & 45.00 & 1.00 & 189.30 & 0.638 & 3329.79 & 3.58 & / & 0.00 & 0.000 \\ H2 & 50.00 & 1.00 & 210.19 & 0.703 & 3329.79 & 5.05 & / & 803.80 & 13.280 \\ H3 & 54.40 & 1.00 & 228.59 & 0.760 & 3329.79 & 6.59 & / & 1030.05 & 13.045 \\ H4 & 45.00 & 1.00 & 189.30 & 0.638 & 1903.60 & 3.58 & / & 0.00 & 0.000 \\ H5 & 69.79 & 1.00 & 292.97 & 0.952 & 1903.60 & 13.70 & / & 1726.18 & 18.385 \\ H6 & 60.00 & 1.00 & 252.00 & 0.831 & 5233.39 & 8.87 & / & 2756.23 & 16.495 \\ \hline \hline \end{tabular}
\end{table} 
Table 11: Thermodynamic properties and costs of exergy streams for the sCO\({}_{2}\)/ammonia-water AHP system. \begin{table}
\begin{tabular}{c c c c c c c c c} \hline \hline
**State** & \(T\) & \(P\) & \(h\) & \(s\) & \(m\) & \(\epsilon_{\text{ph}}\) & \(\epsilon_{\text{ch}}\) & \(\dot{C}\) & \(c\) \\ \cline{2-10}
**Points** & **(\({}^{\circ}\)C)** & **(MPa)** & **(kJ/kg)** & **(kJ/(kg:K))** & **(kg/s)** & **(kJ/kg)** & **(kJ/kg)** & **(S/h)** & **(S/GJ)** \\ \hline
1 & 35.00 & 7.40 & 402.40 & 1.663 & 2309.66 & 216.60 & / & 26,077.65 & 14.480 \\
2 & 110.06 & 20.72 & 444.87 & 1.680 & 2309.66 &Table 12 shows the thermodynamic properties and costs of exergy streams for the sCO\({}_{2}\)/DH system.