NIST Standard Reference Database 106

Solubility System:

**Ethene with 1-Propene,1,1,2,3,3-pentafluoro-3-trifluoroethenyloxy- or per-fluoro (propylene vinyl) ether**

**Components:**

(1) 1-Propene,1,1,2,3,3-pentafluoro-3-trifluoroethenyloxy- or per-fluoro (propylene vinyl) ether; C5F8O; [64080-43-9] NIST Chemistry WebBook for detail

(2) Ethene; C2H4; [74-85-1] NIST Chemistry WebBook for detail

**Original Measurements:**

Sokolov, Yu. P.; Konshin, A.I., Zh. Prikl. Khim. 1989, 62, 1395-1398.

**Variables:**

Temperature = 298.15 K to 353.15 K

Pressure = 298.15 K to 353.15 K

**Prepared By:**

W. Hayduk

**Experimental Data:**(Subscripts 1,2,3, ..., in column headings refer to components 1,2,3, ...)

t/°C | T/K | Pressure [MPa] | Henry's law constant, K [MPa/mol fraction] | Henry Constant Note | Solubility [mol/L] | Solubility Note | Method/Comments | Method Note |
---|---|---|---|---|---|---|---|---|

25 | 298.15 | 0.20 | 5.79 | 3 | 0.08 | c1 | 3.40 | 2 Distribution Constant, K(d) |

25 | 298.15 | 0.31 | − | 3 | 0.23 | c1 | − | 2 Distribution Constant, K(d) |

25 | 298.15 | 0.51 | − | 3 | 0.52 | c1 | − | 2 Distribution Constant, K(d) |

25 | 298.15 | 0.71 | − | 3 | 0.80 | c1 | − | 2 Distribution Constant, K(d) |

25 | 298.15 | 0.91 | − | 3 | 0.97 | c1 | − | 2 Distribution Constant, K(d) |

25 | 298.15 | 1.11 | − | 3 | 1.34 | c1 | − | 2 Distribution Constant, K(d) |

25 | 298.15 | 1.32 | − | 3 | 1.62 | c1 | − | 2 Distribution Constant, K(d) |

50 | 323.15 | 0.51 | 7.11 | 3 | 0.31 | c1 | 2.76 | 2 Distribution Constant, K(d) |

50 | 323.15 | 0.71 | − | 3 | 0.47 | c1 | − | 2 Distribution Constant, K(d) |

50 | 323.15 | 0.91 | − | 3 | 0.71 | c1 | − | 2 Distribution Constant, K(d) |

50 | 323.15 | 1.11 | − | 3 | 0.87 | c1 | − | 2 Distribution Constant, K(d) |

50 | 323.15 | 1.32 | − | 3 | 1.12 | c1 | − | 2 Distribution Constant, K(d) |

70 | 343.15 | 0.71 | 8.58 | 3 | 0.37 | c1 | 2.64 | 2 Distribution Constant, K(d) |

70 | 343.15 | 0.91 | − | 3 | 0.51 | c1 | − | 2 Distribution Constant, K(d) |

70 | 343.15 | 1.11 | − | 3 | 0.76 | c1 | − | 2 Distribution Constant, K(d) |

70 | 343.15 | 1.32 | − | 3 | 0.95 | c1 | − | 2 Distribution Constant, K(d) |

80 | 353.15 | 0.71 | 11.30 | 3 | 0.23 | c1 | 1.66 | 2 Distribution Constant, K(d) |

80 | 353.15 | 0.91 | − | 3 | 0.32 | c1 | − | 2 Distribution Constant, K(d) |

80 | 353.15 | 1.11 | − | 3 | 0.46 | c1 | − | 2 Distribution Constant, K(d) |

**Notes:**

^{1}Calculated by Compiler.

^{2}Distribution constant K

_{d}= C

_{1}/C

_{g}where C

_{1}= mol/litre in liquid, C

_{g}= mol /litre in gas.

^{3}Stated by authors to be lim (

*p*

_{1}/

*x*

_{1}) for

*p*

_{1}= partial pressure of gas.

**Method/Apparatus/Procedure:**

The solubilities were measured using a stirred reactor with a magnetic drive having a volume of 250 cm

^{3}and equipped with a pressure gauge and a surrounding jacket for temperature control. Gas and sample handling systems were attached. A volume of 100-200 cm

^{3}of deaerated solvent was charged to the reactor and equilibrated. A small liquid sample chamber was used to confine a known volume of saturated solution. The sample was then completely evaporated into a much larger vessel. Helium carrier gas was used to increase the pressure of the vapor gas mixture to about 0.12 MPs. The sample was then analyzed by gas chromatography. Details are in Ref. 1.

**Source and Purity of Materials:**

No information about gas or solvent source or purity was supplied.

**Estimated Errors:**

Solubility: δ

*x*

_{1}/

*x*

_{1}= ± 0.02 (compiler)

**References:**

1. Sokolov, Yu. A.; Konshin, A.I., Zh. Prikl. Khim. 1987, 60, 2720.