Mixture of Octane + Phenol + Water

Datasets

1. Mole fraction (16)

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
313.15	0.2065
333.15	0.0467

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Phenol (2) - Liquid mixture 2
313.15	0.3106
333.15	0.2365

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 3)

Temperature, K - Liquid mixture 3	Mole fraction of Phenol (2) - Liquid mixture 3
313.15	0.0236
333.15	0.0322

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Octane (1) - Liquid mixture 1
313.15	0.9697
333.15	0.9459

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Octane (1) - Liquid mixture 2
313.15	0.0074
333.15	0.0097

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 3)

Temperature, K - Liquid mixture 3	Mole fraction of Octane (1) - Liquid mixture 3
313.15	0.0010
333.15	0.0010

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Octane (1) - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
298.15	0.0000	0.2755
298.15	0.0262	0.5286
298.15	0.0321	0.5738
298.15	0.0386	0.6118
298.15	0.0471	0.6532
298.15	0.0596	0.6983
298.15	0.0783	0.7481
298.15	0.0905	0.7626
298.15	0.1029	0.7833
298.15	0.1106	0.7928
298.15	0.1207	0.8028
298.15	0.1347	0.8195
298.15	0.1417	0.8231
298.15	0.1527	0.8300
298.15	0.1648	0.8352
323.15	0.0000	0.1932
323.15	0.0097	0.2365
323.15	0.0119	0.2960
323.15	0.0190	0.4162
323.15	0.0256	0.4695
323.15	0.0331	0.4965
323.15	0.0447	0.5859
323.15	0.0485	0.6059
323.15	0.0682	0.6410
323.15	0.0828	0.6692
323.15	0.0920	0.6852
323.15	0.1119	0.7153
323.15	0.1225	0.7200
323.15	0.1245	0.7223
323.15	0.1585	0.7326
323.15	0.1678	0.7343
323.15	0.1840	0.7359
323.15	0.2018	0.7314
323.15	0.2234	0.7227
323.15	0.2566	0.7047
323.15	0.3011	0.6704
323.15	0.3223	0.6540
323.15	0.3671	0.6127
323.15	0.3950	0.5874
323.15	0.4532	0.5318
323.15	0.8397	0.1454

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Octane (1) - Gas	Mole fraction of Phenol (2) - Gas	Mole fraction of Octane (1) - Liquid	Mole fraction of Phenol (2) - Liquid
333.15	17.40	0.0936	0.0241	0.0058	0.6149
333.15	18.05	0.0485	0.0256	0.0064	0.5228
333.15	18.88	0.0561	0.0206	0.0135	0.4523
333.15	19.11	0.0657	0.0175	0.0022	0.5037
333.15	19.23	0.0206	0.0165	0.0027	0.4401
333.15	19.59	0.1994	0.0217	0.0084	0.5744
333.15	20.20	0.1314	0.0208	0.0038	0.4896
333.15	20.81	0.0910	0.0165	0.0054	0.4590
333.15	21.38	0.1119	0.0168	0.0067	0.4652
333.15	21.84	0.2340	0.0203	0.0072	0.5331
333.15	24.69	0.2375	0.0161	0.0084	0.4631
333.15	24.89	0.2676	0.0140	0.0095	0.4702
333.15	26.05	0.3412	0.0226	0.0050	0.4946
363.15	40.73	0.1814	0.1027	0.0133	0.7041
363.15	42.06	0.2832	0.1340	0.0141	0.6952
363.15	46.28	0.3454	0.1145	0.0139	0.6976
363.15	49.80	0.0626	0.0480	0.0076	0.6470
363.15	50.46	0.2313	0.0837	0.0094	0.6388
363.15	50.89	0.3607	0.0831	0.0120	0.6780
363.15	52.98	0.0559	0.0385	0.0081	0.6184
363.15	55.08	0.2100	0.0581	0.0076	0.5658
363.15	56.14	0.0789	0.0372	0.0068	0.6121
363.15	57.88	0.0837	0.0345	0.0074	0.6120
363.15	57.98	0.1060	0.0375	0.0073	0.6259
363.15	58.13	0.0963	0.0228	0.0081	0.5981
363.15	69.30	0.2281	0.0224	0.0133	0.5926
363.15	82.82	0.2465	0.0002	0.0080	0.3868
363.15	84.46	0.2499	0.0002	0.0068	0.4438

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
313.15	0.2065
333.15	0.0467

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Phenol (2) - Liquid mixture 2
313.15	0.3106
333.15	0.2365

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 3)

Temperature, K - Liquid mixture 3	Mole fraction of Phenol (2) - Liquid mixture 3
313.15	0.0236
333.15	0.0322

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Octane (1) - Liquid mixture 1
313.15	0.9697
333.15	0.9459

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Octane (1) - Liquid mixture 2
313.15	0.0074
333.15	0.0097

Mole fraction of Octane (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 3)

Temperature, K - Liquid mixture 3	Mole fraction of Octane (1) - Liquid mixture 3
313.15	0.0010
333.15	0.0010

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Octane (1) - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
298.15	0.0000	0.2755
298.15	0.0262	0.5286
298.15	0.0321	0.5738
298.15	0.0386	0.6118
298.15	0.0471	0.6532
298.15	0.0596	0.6983
298.15	0.0783	0.7481
298.15	0.0905	0.7626
298.15	0.1029	0.7833
298.15	0.1106	0.7928
298.15	0.1207	0.8028
298.15	0.1347	0.8195
298.15	0.1417	0.8231
298.15	0.1527	0.8300
298.15	0.1648	0.8352
323.15	0.0000	0.1932
323.15	0.0097	0.2365
323.15	0.0119	0.2960
323.15	0.0190	0.4162
323.15	0.0256	0.4695
323.15	0.0331	0.4965
323.15	0.0447	0.5859
323.15	0.0485	0.6059
323.15	0.0682	0.6410
323.15	0.0828	0.6692
323.15	0.0920	0.6852
323.15	0.1119	0.7153
323.15	0.1225	0.7200
323.15	0.1245	0.7223
323.15	0.1585	0.7326
323.15	0.1678	0.7343
323.15	0.1840	0.7359
323.15	0.2018	0.7314
323.15	0.2234	0.7227
323.15	0.2566	0.7047
323.15	0.3011	0.6704
323.15	0.3223	0.6540
323.15	0.3671	0.6127
323.15	0.3950	0.5874
323.15	0.4532	0.5318
323.15	0.8397	0.1454

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Octane (1) - Gas	Mole fraction of Phenol (2) - Gas	Mole fraction of Octane (1) - Liquid	Mole fraction of Phenol (2) - Liquid
333.15	17.40	0.0936	0.0241	0.0058	0.6149
333.15	18.05	0.0485	0.0256	0.0064	0.5228
333.15	18.88	0.0561	0.0206	0.0135	0.4523
333.15	19.11	0.0657	0.0175	0.0022	0.5037
333.15	19.23	0.0206	0.0165	0.0027	0.4401
333.15	19.59	0.1994	0.0217	0.0084	0.5744
333.15	20.20	0.1314	0.0208	0.0038	0.4896
333.15	20.81	0.0910	0.0165	0.0054	0.4590
333.15	21.38	0.1119	0.0168	0.0067	0.4652
333.15	21.84	0.2340	0.0203	0.0072	0.5331
333.15	24.69	0.2375	0.0161	0.0084	0.4631
333.15	24.89	0.2676	0.0140	0.0095	0.4702
333.15	26.05	0.3412	0.0226	0.0050	0.4946
363.15	40.73	0.1814	0.1027	0.0133	0.7041
363.15	42.06	0.2832	0.1340	0.0141	0.6952
363.15	46.28	0.3454	0.1145	0.0139	0.6976
363.15	49.80	0.0626	0.0480	0.0076	0.6470
363.15	50.46	0.2313	0.0837	0.0094	0.6388
363.15	50.89	0.3607	0.0831	0.0120	0.6780
363.15	52.98	0.0559	0.0385	0.0081	0.6184
363.15	55.08	0.2100	0.0581	0.0076	0.5658
363.15	56.14	0.0789	0.0372	0.0068	0.6121
363.15	57.88	0.0837	0.0345	0.0074	0.6120
363.15	57.98	0.1060	0.0375	0.0073	0.6259
363.15	58.13	0.0963	0.0228	0.0081	0.5981
363.15	69.30	0.2281	0.0224	0.0133	0.5926
363.15	82.82	0.2465	0.0002	0.0080	0.3868
363.15	84.46	0.2499	0.0002	0.0068	0.4438

Sources

• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water