Mixture of Carbon dioxide + Propene, hexafluoro-

Datasets

1. Mole fraction (4)
2. P_vap - Vapor or sublimation pressure, kPa (4)

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0180	273.16	0.1350
0.0940	273.20	0.4390
0.1450	273.16	0.5750
0.2520	273.20	0.7070
0.3580	273.16	0.7910
0.4350	273.19	0.8310
0.5910	273.19	0.8890
0.6900	273.17	0.9170
0.7030	273.16	0.9210
0.7110	273.16	0.9230
0.7450	273.16	0.9320
0.1080	263.23	0.5360
0.2280	263.22	0.7240
0.2660	263.21	0.7570
0.2850	263.22	0.7710
0.3010	263.23	0.7820
0.3220	263.21	0.7950
0.4560	263.22	0.8620
0.5380	263.22	0.8890
0.5900	263.22	0.9050
0.6230	263.22	0.9150
0.6800	263.21	0.9270
0.7120	263.22	0.9320
0.7390	263.22	0.9410
0.8020	263.23	0.9520
0.8760	263.23	0.9710
0.9360	263.23	0.9840
0.9530	263.23	0.9880
0.1190	253.17	0.6120
0.2750	253.17	0.7880
0.3500	253.16	0.8420
0.4010	253.17	0.8650
0.4980	253.18	0.8960
0.5160	253.15	0.8990
0.5640	253.16	0.9140
0.6150	253.16	0.9250
0.6660	253.15	0.9360
0.7710	253.16	0.9560
0.8210	253.16	0.9650
0.9080	253.15	0.9810
0.9270	253.15	0.9840
0.9800	253.16	0.9960
0.1500	243.24	0.7100
0.2700	243.22	0.8250
0.4350	243.22	0.8960
0.4530	243.24	0.9020
0.5160	243.22	0.9180
0.6120	243.22	0.9370
0.6560	243.21	0.9450
0.7180	243.23	0.9550
0.7920	243.24	0.9650
0.8800	243.21	0.9780
0.9480	243.23	0.9890
0.9770	243.23	0.9960
0.2520	233.18	0.8450
0.4100	233.19	0.9070
0.5170	233.20	0.9350
0.6660	233.19	0.9570
0.7370	233.19	0.9660
0.7940	233.18	0.9710
0.8630	233.20	0.9800
0.9110	233.19	0.9860
0.9540	233.18	0.9920
0.9780	233.18	0.9960

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0320	273.15	0.1990
0.0760	273.15	0.3800
0.0820	313.15	0.2480
0.1880	313.15	0.3790
0.2590	273.15	0.7150
0.2870	313.15	0.5180
0.3470	313.15	0.5990
0.4030	273.15	0.8090
0.4390	313.15	0.6710
0.5720	313.15	0.7580
0.5750	273.15	0.8750
0.6840	273.15	0.9080
0.7030	313.15	0.8140
0.7600	273.15	0.9340

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0180	273.16	0.1350
0.0940	273.20	0.4390
0.1450	273.16	0.5750
0.2520	273.20	0.7070
0.3580	273.16	0.7910
0.4350	273.19	0.8310
0.5910	273.19	0.8890
0.6900	273.17	0.9170
0.7030	273.16	0.9210
0.7110	273.16	0.9230
0.7450	273.16	0.9320
0.1080	263.23	0.5360
0.2280	263.22	0.7240
0.2660	263.21	0.7570
0.2850	263.22	0.7710
0.3010	263.23	0.7820
0.3220	263.21	0.7950
0.4560	263.22	0.8620
0.5380	263.22	0.8890
0.5900	263.22	0.9050
0.6230	263.22	0.9150
0.6800	263.21	0.9270
0.7120	263.22	0.9320
0.7390	263.22	0.9410
0.8020	263.23	0.9520
0.8760	263.23	0.9710
0.9360	263.23	0.9840
0.9530	263.23	0.9880
0.1190	253.17	0.6120
0.2750	253.17	0.7880
0.3500	253.16	0.8420
0.4010	253.17	0.8650
0.4980	253.18	0.8960
0.5160	253.15	0.8990
0.5640	253.16	0.9140
0.6150	253.16	0.9250
0.6660	253.15	0.9360
0.7710	253.16	0.9560
0.8210	253.16	0.9650
0.9080	253.15	0.9810
0.9270	253.15	0.9840
0.9800	253.16	0.9960
0.1500	243.24	0.7100
0.2700	243.22	0.8250
0.4350	243.22	0.8960
0.4530	243.24	0.9020
0.5160	243.22	0.9180
0.6120	243.22	0.9370
0.6560	243.21	0.9450
0.7180	243.23	0.9550
0.7920	243.24	0.9650
0.8800	243.21	0.9780
0.9480	243.23	0.9890
0.9770	243.23	0.9960
0.2520	233.18	0.8450
0.4100	233.19	0.9070
0.5170	233.20	0.9350
0.6660	233.19	0.9570
0.7370	233.19	0.9660
0.7940	233.18	0.9710
0.8630	233.20	0.9800
0.9110	233.19	0.9860
0.9540	233.18	0.9920
0.9780	233.18	0.9960

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0320	273.15	0.1990
0.0760	273.15	0.3800
0.0820	313.15	0.2480
0.1880	313.15	0.3790
0.2590	273.15	0.7150
0.2870	313.15	0.5180
0.3470	313.15	0.5990
0.4030	273.15	0.8090
0.4390	313.15	0.6710
0.5720	313.15	0.7580
0.5750	273.15	0.8750
0.6840	273.15	0.9080
0.7030	313.15	0.8140
0.7600	273.15	0.9340

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0180	273.16	386.00
0.0940	273.20	615.00
0.1450	273.16	757.00
0.2520	273.20	1072.00
0.3580	273.16	1393.00
0.4350	273.19	1632.00
0.5910	273.19	2110.00
0.6900	273.17	2412.00
0.7030	273.16	2454.00
0.7110	273.16	2485.00
0.7450	273.16	2595.00
0.1080	263.23	492.00
0.2280	263.22	783.00
0.2660	263.21	873.00
0.2850	263.22	919.00
0.3010	263.23	959.00
0.3220	263.21	1014.00
0.4560	263.22	1332.00
0.5380	263.22	1522.00
0.5900	263.22	1644.00
0.6230	263.22	1722.00
0.6800	263.21	1852.00
0.7120	263.22	1935.00
0.7390	263.22	1994.00
0.8020	263.23	2152.00
0.8760	263.23	2327.00
0.9360	263.23	2480.00
0.9530	263.23	2529.00
0.1190	253.17	385.00
0.2750	253.17	681.00
0.3500	253.16	818.00
0.4010	253.17	914.00
0.4980	253.18	1083.00
0.5160	253.15	1115.00
0.5640	253.16	1202.00
0.6150	253.16	1290.00
0.6660	253.15	1380.00
0.7710	253.16	1560.00
0.8210	253.16	1646.00
0.9080	253.15	1800.00
0.9270	253.15	1833.00
0.9800	253.16	1935.00
0.1500	243.24	331.00
0.2700	243.22	504.00
0.4350	243.22	730.00
0.4530	243.24	753.00
0.5160	243.22	840.00
0.6120	243.22	962.00
0.6560	243.21	1017.00
0.7180	243.23	1083.00
0.7920	243.24	1175.00
0.8800	243.21	1287.00
0.9480	243.23	1378.00
0.9770	243.23	1407.00
0.2520	233.18	348.00
0.4100	233.19	505.00
0.5170	233.20	620.00
0.6660	233.19	750.00
0.7370	233.19	808.00
0.7940	233.18	840.00
0.8630	233.20	899.00
0.9110	233.19	938.00
0.9540	233.18	974.00
0.9780	233.18	995.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0320	273.15	406.00
0.0760	273.15	524.00
0.0820	313.15	1530.00
0.1880	313.15	2111.00
0.2590	273.15	1072.00
0.2870	313.15	2707.00
0.3470	313.15	3063.00
0.4030	273.15	1482.00
0.4390	313.15	3630.00
0.5720	313.15	4557.00
0.5750	273.15	1992.00
0.6840	273.15	2357.00
0.7030	313.15	5620.00
0.7600	273.15	2604.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0180	273.16	386.00
0.0940	273.20	615.00
0.1450	273.16	757.00
0.2520	273.20	1072.00
0.3580	273.16	1393.00
0.4350	273.19	1632.00
0.5910	273.19	2110.00
0.6900	273.17	2412.00
0.7030	273.16	2454.00
0.7110	273.16	2485.00
0.7450	273.16	2595.00
0.1080	263.23	492.00
0.2280	263.22	783.00
0.2660	263.21	873.00
0.2850	263.22	919.00
0.3010	263.23	959.00
0.3220	263.21	1014.00
0.4560	263.22	1332.00
0.5380	263.22	1522.00
0.5900	263.22	1644.00
0.6230	263.22	1722.00
0.6800	263.21	1852.00
0.7120	263.22	1935.00
0.7390	263.22	1994.00
0.8020	263.23	2152.00
0.8760	263.23	2327.00
0.9360	263.23	2480.00
0.9530	263.23	2529.00
0.1190	253.17	385.00
0.2750	253.17	681.00
0.3500	253.16	818.00
0.4010	253.17	914.00
0.4980	253.18	1083.00
0.5160	253.15	1115.00
0.5640	253.16	1202.00
0.6150	253.16	1290.00
0.6660	253.15	1380.00
0.7710	253.16	1560.00
0.8210	253.16	1646.00
0.9080	253.15	1800.00
0.9270	253.15	1833.00
0.9800	253.16	1935.00
0.1500	243.24	331.00
0.2700	243.22	504.00
0.4350	243.22	730.00
0.4530	243.24	753.00
0.5160	243.22	840.00
0.6120	243.22	962.00
0.6560	243.21	1017.00
0.7180	243.23	1083.00
0.7920	243.24	1175.00
0.8800	243.21	1287.00
0.9480	243.23	1378.00
0.9770	243.23	1407.00
0.2520	233.18	348.00
0.4100	233.19	505.00
0.5170	233.20	620.00
0.6660	233.19	750.00
0.7370	233.19	808.00
0.7940	233.18	840.00
0.8630	233.20	899.00
0.9110	233.19	938.00
0.9540	233.18	974.00
0.9780	233.18	995.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0320	273.15	406.00
0.0760	273.15	524.00
0.0820	313.15	1530.00
0.1880	313.15	2111.00
0.2590	273.15	1072.00
0.2870	313.15	2707.00
0.3470	313.15	3063.00
0.4030	273.15	1482.00
0.4390	313.15	3630.00
0.5720	313.15	4557.00
0.5750	273.15	1992.00
0.6840	273.15	2357.00
0.7030	313.15	5620.00
0.7600	273.15	2604.00

Sources

• Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
• Vapor-Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)