Mixture of 1-Propanol + Ethane

Datasets

1. Mole fraction (2)
2. Lower consolute temperature, K (4)
3. P_c - Critical pressure, kPa (2)
4. P_vap - Vapor or sublimation pressure, kPa (4)
5. T_c - Critical temperature, K (2)

Mole fraction of Ethane (2) [ref]

Fixed		Measured
Mole fraction of Ethane (2) - Liquid	Temperature, K - Gas	Mole fraction of Ethane (2) - Gas
0.0410	348.68	0.9460
0.0920	348.68	0.9680
0.1420	348.68	0.9770
0.1880	348.68	0.9790
0.2210	317.59	0.9930
0.2290	348.68	0.9800
0.2320	324.51	0.9910
0.2680	348.68	0.9790
0.2980	324.51	0.9920
0.3070	348.68	0.9780
0.3160	317.59	0.9940
0.3450	348.68	0.9760
0.3630	324.51	0.9920
0.3780	317.59	0.9940
0.3970	348.68	0.9710
0.4200	324.51	0.9910
0.4350	317.59	0.9930
0.4550	348.68	0.9650
0.5070	324.51	0.9880
0.5250	317.59	0.9920
0.5480	348.68	0.9480
0.5510	324.51	0.9850
0.5870	317.59	0.9770
0.5900	324.51	0.9650
0.6000	348.68	0.9190
0.6440	324.51	0.9440
0.6500	317.59	0.9680
0.6570	317.59	0.9600
0.6570	348.68	0.8870
0.6750	324.51	0.9250
0.6880	317.59	0.9230
0.7040	324.51	0.8800
0.7060	348.68	0.8660
0.7080	317.59	0.8720
0.7340	324.51	0.8450
0.7720	348.68	0.7720
0.7740	324.51	0.7740
0.7890	317.59	0.7890

Mole fraction of Ethane (2) [ref]

Fixed		Measured
Mole fraction of Ethane (2) - Liquid	Temperature, K - Gas	Mole fraction of Ethane (2) - Gas
0.0410	348.68	0.9460
0.0920	348.68	0.9680
0.1420	348.68	0.9770
0.1880	348.68	0.9790
0.2210	317.59	0.9930
0.2290	348.68	0.9800
0.2320	324.51	0.9910
0.2680	348.68	0.9790
0.2980	324.51	0.9920
0.3070	348.68	0.9780
0.3160	317.59	0.9940
0.3450	348.68	0.9760
0.3630	324.51	0.9920
0.3780	317.59	0.9940
0.3970	348.68	0.9710
0.4200	324.51	0.9910
0.4350	317.59	0.9930
0.4550	348.68	0.9650
0.5070	324.51	0.9880
0.5250	317.59	0.9920
0.5480	348.68	0.9480
0.5510	324.51	0.9850
0.5870	317.59	0.9770
0.5900	324.51	0.9650
0.6000	348.68	0.9190
0.6440	324.51	0.9440
0.6500	317.59	0.9680
0.6570	317.59	0.9600
0.6570	348.68	0.8870
0.6750	324.51	0.9250
0.6880	317.59	0.9230
0.7040	324.51	0.8800
0.7060	348.68	0.8660
0.7080	317.59	0.8720
0.7340	324.51	0.8450
0.7720	348.68	0.7720
0.7740	324.51	0.7740
0.7890	317.59	0.7890

Lower consolute temperature, K [ref]

Lower consolute temperature, K - Liquid mixture 1
313.03

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
315.26

Lower consolute temperature, K [ref]

Lower consolute temperature, K - Liquid mixture 1
313.03

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
315.26

Critical pressure, kPa [ref]

Mole fraction of Ethane (2) - Liquid	Critical pressure, kPa - Liquid
0.7720	9488.00
0.7740	6932.00
0.7890	5978.00

Critical pressure, kPa [ref]

Mole fraction of Ethane (2) - Liquid	Critical pressure, kPa - Liquid
0.7720	9488.00
0.7740	6932.00
0.7890	5978.00

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
313.03	5348.00
313.32	5379.00
313.43	5391.00
313.52	5399.00
313.60	5408.00
313.66	5415.00
313.71	5421.00
313.77	5427.00
313.84	5434.00
313.88	5441.00
313.93	5445.00
313.99	5450.00
314.06	5459.00
314.10	5464.00
314.15	5469.00
314.23	5478.00
314.30	5486.00
314.39	5496.00
314.46	5504.00
314.49	5508.00
314.51	5510.00
314.66	5527.00
314.89	5556.00
315.26	5597.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0410	348.68	841.00
0.0920	348.68	1817.00
0.1420	348.68	2809.00
0.1880	348.68	3603.00
0.2210	317.59	2817.00
0.2290	348.68	4344.00
0.2320	324.51	3243.00
0.2680	348.68	5057.00
0.2980	324.51	3899.00
0.3070	348.68	5711.00
0.3160	317.59	3844.00
0.3450	348.68	6324.00
0.3630	324.51	4624.00
0.3780	317.59	4349.00
0.3970	348.68	7076.00
0.4200	324.51	5241.00
0.4350	317.59	4836.00
0.4550	348.68	7682.00
0.5070	324.51	5880.00
0.5250	317.59	5336.00
0.5480	348.68	8529.00
0.5510	324.51	6111.00
0.5870	317.59	5595.00
0.5900	324.51	6362.00
0.6000	348.68	8929.00
0.6440	324.51	6546.00
0.6500	317.59	5727.00
0.6570	317.59	5773.00
0.6570	348.68	9170.00
0.6750	324.51	6676.00
0.6880	317.59	5868.00
0.7040	324.51	6782.00
0.7060	348.68	9396.00
0.7080	317.59	5957.00
0.7340	324.51	6824.00
0.7720	348.68	9488.00
0.7740	324.51	6932.00
0.7890	317.59	5978.00

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
313.03	5348.00
313.32	5379.00
313.43	5391.00
313.52	5399.00
313.60	5408.00
313.66	5415.00
313.71	5421.00
313.77	5427.00
313.84	5434.00
313.88	5441.00
313.93	5445.00
313.99	5450.00
314.06	5459.00
314.10	5464.00
314.15	5469.00
314.23	5478.00
314.30	5486.00
314.39	5496.00
314.46	5504.00
314.49	5508.00
314.51	5510.00
314.66	5527.00
314.89	5556.00
315.26	5597.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0410	348.68	841.00
0.0920	348.68	1817.00
0.1420	348.68	2809.00
0.1880	348.68	3603.00
0.2210	317.59	2817.00
0.2290	348.68	4344.00
0.2320	324.51	3243.00
0.2680	348.68	5057.00
0.2980	324.51	3899.00
0.3070	348.68	5711.00
0.3160	317.59	3844.00
0.3450	348.68	6324.00
0.3630	324.51	4624.00
0.3780	317.59	4349.00
0.3970	348.68	7076.00
0.4200	324.51	5241.00
0.4350	317.59	4836.00
0.4550	348.68	7682.00
0.5070	324.51	5880.00
0.5250	317.59	5336.00
0.5480	348.68	8529.00
0.5510	324.51	6111.00
0.5870	317.59	5595.00
0.5900	324.51	6362.00
0.6000	348.68	8929.00
0.6440	324.51	6546.00
0.6500	317.59	5727.00
0.6570	317.59	5773.00
0.6570	348.68	9170.00
0.6750	324.51	6676.00
0.6880	317.59	5868.00
0.7040	324.51	6782.00
0.7060	348.68	9396.00
0.7080	317.59	5957.00
0.7340	324.51	6824.00
0.7720	348.68	9488.00
0.7740	324.51	6932.00
0.7890	317.59	5978.00

Critical temperature, K [ref]

Mole fraction of Ethane (2) - Liquid	Critical temperature, K - Liquid
0.7720	348.68
0.7740	324.51
0.7890	317.59

Critical temperature, K [ref]

Mole fraction of Ethane (2) - Liquid	Critical temperature, K - Liquid
0.7720	348.68
0.7740	324.51
0.7890	317.59

Sources

• Experimental Determination and Correlation of Phase Equilibria for the Ethane + 1-Propanol and Propane + 1-Propanol Systems