Mixture of Aniline + Octane + Cyclohexylamine

Datasets

1. Temperature, K x Pressure, kPa x Mole fraction (3)

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

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Octane (2) - Liquid	Mole fraction of Aniline (1) - Liquid	Mole fraction of Aniline (1) - Gas	Mole fraction of Octane (2) - Gas
333.15	6.92	0.0813	0.8726	0.0885	0.8813
333.15	7.43	0.1273	0.3603	0.0891	0.5836
333.15	8.94	0.1486	0.0169	0.0025	0.2650
333.15	8.95	0.2678	0.2124	0.0223	0.5788
333.15	9.32	0.2480	0.0097	0.0015	0.4576
333.15	9.39	0.3754	0.0358	0.0014	0.6055
333.15	9.79	0.2807	0.0269	0.0038	0.4210
333.15	10.02	0.5528	0.0222	0.0053	0.7645
333.15	10.07	0.6099	0.1407	0.0512	0.7258
333.15	10.42	0.6881	0.1107	0.0290	0.8018
363.15	23.32	0.1563	0.5506	0.0537	0.6566
363.15	23.88	0.1096	0.1814	0.0372	0.3247
363.15	26.18	0.1786	0.5154	0.0572	0.6540
363.15	27.92	0.3180	0.2561	0.0568	0.6827
363.15	28.32	0.1391	0.0083	0.0024	0.2504
363.15	28.88	0.1593	0.0081	0.0008	0.3131
363.15	29.22	0.2009	0.0072	0.0009	0.3601
363.15	30.64	0.2767	0.0105	0.0039	0.4566
363.15	31.39	0.4743	0.0459	0.0045	0.6580
363.15	32.04	0.6918	0.1590	0.1111	0.7606
363.15	32.71	0.7566	0.1137	0.0396	0.8363

Mole fraction of Cyclohexylamine (3) [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Aniline (1) - Liquid mixture 1	Mole fraction of Cyclohexylamine (3) - Liquid mixture 1
298.15	0.0860	0.0000
298.15	0.0960	0.0080
298.15	0.1060	0.0180
298.15	0.1210	0.0330
298.15	0.1380	0.0470
298.15	0.1580	0.0650
298.15	0.2000	0.0900
298.15	0.2410	0.1080
298.15	0.2980	0.1260
298.15	0.3840	0.1430
298.15	0.4520	0.1530
298.15	0.5640	0.1600
298.15	0.6610	0.1520
298.15	0.7420	0.1280
298.15	0.8370	0.0820
298.15	0.9220	0.0260
298.15	0.9550	0.0000
333.15	0.2750	0.0000
333.15	0.3030	0.0100
333.15	0.3300	0.0190
333.15	0.3670	0.0260
333.15	0.4190	0.0350
333.15	0.4770	0.0400
333.15	0.5000	0.0420
333.15	0.5370	0.0420
333.15	0.5850	0.0450
333.15	0.6020	0.0440
333.15	0.6130	0.0450
333.15	0.6230	0.0430
333.15	0.6470	0.0430
333.15	0.6760	0.0420
333.15	0.7380	0.0350
333.15	0.8090	0.0210
333.15	0.8650	0.0000

Temperature, K x Mole fraction [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Aniline (1) - Liquid mixture 2	Mole fraction of Cyclohexylamine (3) - Liquid mixture 2	Mole fraction of Cyclohexylamine (3) - Liquid mixture 1	Mole fraction of Aniline (1) - Liquid mixture 1
298.15	0.8150	0.0800	0.0510	0.1670
298.15	0.8940	0.0300	0.0140	0.1060
298.15	0.6610	0.1520	0.0880	0.2290
333.15	0.7460	0.0310	0.0190	0.3300
333.15	0.8670	0.0070	0.0070	0.3020

Sources

• Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
• Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane

Note: These property values are available through the Cheméo API. A free account gives you an access key.