Vapour-liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15 K and pressures up to about 3 MPa Valtz, A.; Gicquel, L.; Coquelet, C.; Richon, D.; Fluid Phase Equilibria 2005, 230, 184-191
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Vapor pressure
- Methodology: CCELL:UFactor:2
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) |
| 277.22 | 339.5 |
| 295.30 | 610.8 |
| 297.32 | 649.3 |
| 299.21 | 685.5 |
| 299.31 | 688.7 |
| 299.34 | 689.4 |
| 301.19 | 726.7 |
| 301.30 | 730.0 |
| 303.06 | 767.0 |
| 303.19 | 769.8 |
| 303.31 | 773.5 |
| 279.24 | 364.0 |
| 305.33 | 819.1 |
| 307.34 | 866.6 |
| 309.35 | 916.0 |
| 311.35 | 967.3 |
| 313.31 | 1019.3 |
| 315.36 | 1076.9 |
| 317.32 | 1133.0 |
| 319.38 | 1195.5 |
| 321.34 | 1256.1 |
| 329.37 | 1532.3 |
| 281.25 | 389.7 |
| 335.39 | 1767.4 |
| 337.41 | 1851.9 |
| 339.41 | 1939.2 |
| 341.43 | 2029.5 |
| 343.43 | 2123.0 |
| 347.44 | 2319.8 |
| 349.46 | 2419.4 |
| 351.46 | 2530.3 |
| 353.48 | 2641.1 |
| 355.48 | 2755.4 |
| 283.24 | 416.7 |
| 360.48 | 3054.3 |
| 285.26 | 445.4 |
| 287.27 | 475.4 |
| 289.27 | 506.9 |
| 291.29 | 539.9 |
| 293.31 | 575.1 |
532; R-134a; 00219