Mixture of Ethene, tetrafluoro- + Cyclobutane, octafluoro-

Datasets

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

Mole fraction of Ethene, tetrafluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethene, tetrafluoro- (1) - Gas
0.0000	248.30	0.0000
0.0000	263.00	0.0000
0.0000	282.90	0.0000
0.0520	282.90	0.3290
0.1370	282.90	0.5850
0.1550	263.00	0.7200
0.2510	282.90	0.7410
0.2680	263.00	0.8150
0.3180	248.30	0.8800
0.3200	282.90	0.7940
0.3440	263.00	0.8510
0.3950	248.30	0.9070
0.4170	263.00	0.8830
0.4230	282.90	0.8490
0.4490	248.30	0.9230
0.4720	263.00	0.9080
0.4810	248.30	0.9320
0.5130	282.90	0.8820
0.5340	263.00	0.9230
0.5380	248.30	0.9440
0.5980	248.30	0.9550
0.6030	282.90	0.9120
0.6170	263.00	0.9400
0.6540	248.30	0.9630
0.6810	282.90	0.9310
0.6880	263.00	0.9570
0.6980	248.30	0.9690
0.7420	248.30	0.9740
0.7630	263.00	0.9680
0.7630	282.90	0.9510
1.0000	248.30	1.0000
1.0000	263.00	1.0000
1.0000	282.90	1.0000

Mole fraction of Ethene, tetrafluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethene, tetrafluoro- (1) - Gas
0.0000	248.30	0.0000
0.0000	263.00	0.0000
0.0000	282.90	0.0000
0.0520	282.90	0.3290
0.1370	282.90	0.5850
0.1550	263.00	0.7200
0.2510	282.90	0.7410
0.2680	263.00	0.8150
0.3180	248.30	0.8800
0.3200	282.90	0.7940
0.3440	263.00	0.8510
0.3950	248.30	0.9070
0.4170	263.00	0.8830
0.4230	282.90	0.8490
0.4490	248.30	0.9230
0.4720	263.00	0.9080
0.4810	248.30	0.9320
0.5130	282.90	0.8820
0.5340	263.00	0.9230
0.5380	248.30	0.9440
0.5980	248.30	0.9550
0.6030	282.90	0.9120
0.6170	263.00	0.9400
0.6540	248.30	0.9630
0.6810	282.90	0.9310
0.6880	263.00	0.9570
0.6980	248.30	0.9690
0.7420	248.30	0.9740
0.7630	263.00	0.9680
0.7630	282.90	0.9510
1.0000	248.30	1.0000
1.0000	263.00	1.0000
1.0000	282.90	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	248.30	40.00
0.0000	263.00	81.00
0.0000	282.90	180.00
0.0520	282.90	252.00
0.1370	282.90	398.00
0.1550	263.00	254.00
0.2510	282.90	594.00
0.2680	263.00	366.00
0.3180	248.30	256.00
0.3200	282.90	720.00
0.3440	263.00	450.00
0.3950	248.30	307.00
0.4170	263.00	535.00
0.4230	282.90	897.00
0.4490	248.30	349.00
0.4720	263.00	607.00
0.4810	248.30	380.00
0.5130	282.90	1065.00
0.5340	263.00	699.00
0.5380	248.30	427.00
0.5980	248.30	477.00
0.6030	282.90	1257.00
0.6170	263.00	798.00
0.6540	248.30	525.00
0.6810	282.90	1427.00
0.6880	263.00	897.00
0.6980	248.30	569.00
0.7420	248.30	615.00
0.7630	263.00	994.00
0.7630	282.90	1645.00
1.0000	248.30	866.00
1.0000	263.00	1357.00
1.0000	282.90	2330.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	248.30	40.00
0.0000	263.00	81.00
0.0000	282.90	180.00
0.0520	282.90	252.00
0.1370	282.90	398.00
0.1550	263.00	254.00
0.2510	282.90	594.00
0.2680	263.00	366.00
0.3180	248.30	256.00
0.3200	282.90	720.00
0.3440	263.00	450.00
0.3950	248.30	307.00
0.4170	263.00	535.00
0.4230	282.90	897.00
0.4490	248.30	349.00
0.4720	263.00	607.00
0.4810	248.30	380.00
0.5130	282.90	1065.00
0.5340	263.00	699.00
0.5380	248.30	427.00
0.5980	248.30	477.00
0.6030	282.90	1257.00
0.6170	263.00	798.00
0.6540	248.30	525.00
0.6810	282.90	1427.00
0.6880	263.00	897.00
0.6980	248.30	569.00
0.7420	248.30	615.00
0.7630	263.00	994.00
0.7630	282.90	1645.00
1.0000	248.30	866.00
1.0000	263.00	1357.00
1.0000	282.90	2330.00

Sources

• Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (248 to 283) K