Mixture of Propene + Ethane, pentafluoro-

Datasets

1. Azeotropic composition: mole fraction (4)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. Azeotropic pressure, kPa (2)

Azeotropic composition: mole fraction of Ethane, pentafluoro- (2) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Ethane, pentafluoro- (2) - Liquid
263.15	0.5350
278.15	0.5568
293.15	0.5782
308.15	0.6025
323.15	0.6221

Mole fraction of Ethane, pentafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, pentafluoro- (2) - Gas
0.0595	323.15	0.1036
0.0675	308.15	0.1249
0.0817	263.15	0.1902
0.0844	293.15	0.1522
0.1268	308.15	0.2058
0.1551	323.15	0.2262
0.1779	278.15	0.2784
0.2112	293.15	0.2991
0.2393	263.15	0.3557
0.2505	308.15	0.3361
0.2624	278.15	0.3556
0.2631	323.15	0.3332
0.3517	308.15	0.4058
0.3600	293.15	0.4186
0.3684	278.15	0.4346
0.3873	263.15	0.4545
0.4229	323.15	0.4631
0.4648	293.15	0.4965
0.4890	278.15	0.5104
0.5060	263.15	0.5216
0.5162	308.15	0.5385
0.5237	293.15	0.5398
0.5270	263.15	0.5355
0.5445	323.15	0.5600
0.5577	278.15	0.5633
0.6096	278.15	0.6009
0.6142	293.15	0.6098
0.6337	263.15	0.5990
0.6387	323.15	0.6381
0.6450	308.15	0.6390
0.6897	293.15	0.6711
0.6934	278.15	0.6569
0.7169	323.15	0.7056
0.7266	293.15	0.6994
0.7297	263.15	0.6629
0.7751	308.15	0.7513
0.7803	263.15	0.7102
0.7853	278.15	0.7258
0.7908	323.15	0.7754
0.7968	293.15	0.7663
0.8126	263.15	0.7393
0.8408	308.15	0.8159
0.8424	278.15	0.7890
0.8631	323.15	0.8460
0.8954	293.15	0.8645
0.9115	263.15	0.8418
0.9198	308.15	0.8994

Azeotropic composition: mole fraction of Ethane, pentafluoro- (2) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Ethane, pentafluoro- (2) - Liquid
263.15	0.5350
278.15	0.5568
293.15	0.5782
308.15	0.6025
323.15	0.6221

Mole fraction of Ethane, pentafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, pentafluoro- (2) - Gas
0.0595	323.15	0.1036
0.0675	308.15	0.1249
0.0817	263.15	0.1902
0.0844	293.15	0.1522
0.1268	308.15	0.2058
0.1551	323.15	0.2262
0.1779	278.15	0.2784
0.2112	293.15	0.2991
0.2393	263.15	0.3557
0.2505	308.15	0.3361
0.2624	278.15	0.3556
0.2631	323.15	0.3332
0.3517	308.15	0.4058
0.3600	293.15	0.4186
0.3684	278.15	0.4346
0.3873	263.15	0.4545
0.4229	323.15	0.4631
0.4648	293.15	0.4965
0.4890	278.15	0.5104
0.5060	263.15	0.5216
0.5162	308.15	0.5385
0.5237	293.15	0.5398
0.5270	263.15	0.5355
0.5445	323.15	0.5600
0.5577	278.15	0.5633
0.6096	278.15	0.6009
0.6142	293.15	0.6098
0.6337	263.15	0.5990
0.6387	323.15	0.6381
0.6450	308.15	0.6390
0.6897	293.15	0.6711
0.6934	278.15	0.6569
0.7169	323.15	0.7056
0.7266	293.15	0.6994
0.7297	263.15	0.6629
0.7751	308.15	0.7513
0.7803	263.15	0.7102
0.7853	278.15	0.7258
0.7908	323.15	0.7754
0.7968	293.15	0.7663
0.8126	263.15	0.7393
0.8408	308.15	0.8159
0.8424	278.15	0.7890
0.8631	323.15	0.8460
0.8954	293.15	0.8645
0.9115	263.15	0.8418
0.9198	308.15	0.8994

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	263.15	428.70
0.0000	278.15	673.60
0.0000	293.15	1012.90
0.0000	308.15	1465.30
0.0000	323.15	2047.90
0.0595	323.15	2205.50
0.0675	308.15	1602.40
0.0817	263.15	498.00
0.0844	293.15	1145.50
0.1268	308.15	1703.80
0.1551	323.15	2415.90
0.1779	278.15	833.40
0.2112	293.15	1263.60
0.2393	263.15	556.00
0.2505	308.15	1847.00
0.2624	278.15	877.20
0.2631	323.15	2589.50
0.3517	308.15	1929.00
0.3600	293.15	1346.80
0.3684	278.15	905.60
0.3873	263.15	585.80
0.4229	323.15	2747.10
0.4648	293.15	1376.40
0.4890	278.15	921.50
0.5060	263.15	589.30
0.5162	308.15	1995.10
0.5237	293.15	1386.40
0.5270	263.15	591.10
0.5445	323.15	2813.70
0.5577	278.15	923.10
0.6096	278.15	925.00
0.6142	293.15	1390.80
0.6337	263.15	591.00
0.6387	323.15	2827.10
0.6450	308.15	2005.80
0.6897	293.15	1383.90
0.6934	278.15	918.20
0.7169	323.15	2813.60
0.7266	293.15	1376.00
0.7297	263.15	580.50
0.7751	308.15	1969.30
0.7803	263.15	567.50
0.7853	278.15	902.50
0.7908	323.15	2774.20
0.7968	293.15	1352.80
0.8126	263.15	566.80
0.8408	308.15	1930.60
0.8424	278.15	882.30
0.8631	323.15	2713.50
0.8954	293.15	1299.70
0.9115	263.15	531.10
0.9198	308.15	1863.40
1.0000	263.15	482.40
1.0000	278.15	782.10
1.0000	293.15	1205.60
1.0000	308.15	1773.20
1.0000	323.15	2531.10

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	263.15	428.70
0.0000	278.15	673.60
0.0000	293.15	1012.90
0.0000	308.15	1465.30
0.0000	323.15	2047.90
0.0595	323.15	2205.50
0.0675	308.15	1602.40
0.0817	263.15	498.00
0.0844	293.15	1145.50
0.1268	308.15	1703.80
0.1551	323.15	2415.90
0.1779	278.15	833.40
0.2112	293.15	1263.60
0.2393	263.15	556.00
0.2505	308.15	1847.00
0.2624	278.15	877.20
0.2631	323.15	2589.50
0.3517	308.15	1929.00
0.3600	293.15	1346.80
0.3684	278.15	905.60
0.3873	263.15	585.80
0.4229	323.15	2747.10
0.4648	293.15	1376.40
0.4890	278.15	921.50
0.5060	263.15	589.30
0.5162	308.15	1995.10
0.5237	293.15	1386.40
0.5270	263.15	591.10
0.5445	323.15	2813.70
0.5577	278.15	923.10
0.6096	278.15	925.00
0.6142	293.15	1390.80
0.6337	263.15	591.00
0.6387	323.15	2827.10
0.6450	308.15	2005.80
0.6897	293.15	1383.90
0.6934	278.15	918.20
0.7169	323.15	2813.60
0.7266	293.15	1376.00
0.7297	263.15	580.50
0.7751	308.15	1969.30
0.7803	263.15	567.50
0.7853	278.15	902.50
0.7908	323.15	2774.20
0.7968	293.15	1352.80
0.8126	263.15	566.80
0.8408	308.15	1930.60
0.8424	278.15	882.30
0.8631	323.15	2713.50
0.8954	293.15	1299.70
0.9115	263.15	531.10
0.9198	308.15	1863.40
1.0000	263.15	482.40
1.0000	278.15	782.10
1.0000	293.15	1205.60
1.0000	308.15	1773.20
1.0000	323.15	2531.10

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
263.15	593.50
278.15	927.00
293.15	1390.30
308.15	2001.90
323.15	2818.10

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
263.15	593.50
278.15	927.00
293.15	1390.30
308.15	2001.90
323.15	2818.10

Sources

• Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K