Isobaric Vapor-Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa Ding, X.; Liu, H.; Li, N.; Wang, S.; Wang, G.; Zhao, X.; Wang, Y.; Journal of Chemical & Engineering Data 2015, 60, 541-544
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Mole fraction
- Methodology: Chromatography
- Phase(s): Gas' Liquid
- Substances:
Data
| T (K) | x (mol mol-1) | x (mol mol-1) | x (mol mol-1) | x (mol mol-1) |
| 341.1 | 0.778 | 0.108 | 0.046 | 0.946 |
| 349.2 | 0.376 | 0.362 | 0.115 | 0.869 |
| 351.5 | 0.324 | 0.385 | 0.127 | 0.858 |
| 390.6 | 0.060 | 0.29 | 0.303 | 0.61 |
| 352.9 | 0.296 | 0.397 | 0.135 | 0.846 |
| 355.2 | 0.259 | 0.411 | 0.147 | 0.832 |
| 357.4 | 0.229 | 0.42 | 0.159 | 0.819 |
| 360.0 | 0.200 | 0.426 | 0.174 | 0.8 |
| 362.3 | 0.179 | 0.428 | 0.187 | 0.785 |
| 363.9 | 0.166 | 0.426 | 0.197 | 0.774 |
| 366.5 | 0.148 | 0.421 | 0.212 | 0.755 |
| 419.1 | 0.019 | 0.15 | 0.328 | 0.354 |
| 369.3 | 0.131 | 0.415 | 0.226 | 0.736 |
| 377.7 | 0.093 | 0.376 | 0.265 | 0.684 |
| 384.7 | 0.072 | 0.332 | 0.289 | 0.643 |
| 398.1 | 0.045 | 0.263 | 0.335 | 0.545 |
| 342.1 | 0.665 | 0.22 | 0.079 | 0.914 |
| 401.9 | 0.038 | 0.244 | 0.345 | 0.515 |
| 402.8 | 0.036 | 0.241 | 0.347 | 0.507 |
| 406.1 | 0.033 | 0.223 | 0.352 | 0.478 |
| 411.6 | 0.025 | 0.194 | 0.35 | 0.429 |
| 412.7 | 0.023 | 0.187 | 0.348 | 0.419 |
| 420.8 | 0.018 | 0.136 | 0.32 | 0.335 |
| 359.3 | 0.208 | 0.423 | 0.171 | 0.804 |
| 426.7 | 0.012 | 0.097 | 0.249 | 0.288 |
| 429.3 | 0.010 | 0.086 | 0.23 | 0.251 |
| 430.4 | 0.007 | 0.08 | 0.221 | 0.234 |
| 344.5 | 0.536 | 0.289 | 0.091 | 0.9 |
| 347.2 | 0.438 | 0.332 | 0.106 | 0.88 |
8591; methanol + epichlorohydrin + 2,3-dimethoxy-1-propanol; 00016:00756:01962