| No. | Temperature | Pressure | Mass flow | LHV |
| [K] | [bar] | [kg/s] | [kJ/kg] | |
| FUEL | 298.1 | 1 | 0.059 | 47,466.59 |
| 0 | 520.3 | 10 | 0.059 | 47,466.59 |
| 1 | 1019.5 | 10 | 0.443 | 8219.40 |
| 6 | 1173.2 | 10 | 0.25 | 2165.22 |
| AIR | 298.1 | 1 | 1.523 | 0.00 |
| 7 | 635.9 | 10 | 1.523 | 0.00 |
| 8 | 925.7 | 10 | 1.523 | 0.00 |
| 11 | 1173.2 | 10 | 1.332 | 0.00 |
| 13 | 1435.7 | 10 | 1.582 | 0.02 |
| 14 | 935.7 | 1 | 1.582 | 0.02 |
| 15 | 680.2 | 1 | 1.582 | 0.02 |
| 16 | 343.1 | 1 | 1.582 | 0.02 |
| NH3∙H2O | 298.15 | 9 | 0.242 | 13,022.53 |
| 01 | 299.10 | 72 | 0.242 | 13,022.53 |
| 02 | 649.10 | 72 | 0.242 | 13,022.53 |
| 03 | 373.70 | 3 | 0.242 | 13,022.53 |
| 06 | 291.10 | 3 | 0.369 | 9554.07 |
| 010 | 370.77 | 9 | 0.258 | 9554.07 |
| 011 | 370.78 | 9 | 0.132 | 15,939.16 |
| 012 | 370.78 | 9 | 0.127 | 2921.50 |
| 016 | 337.98 | 9 | 0.242 | 13,022.03 |