Mixture of Aniline + Cyclohexylamine + Water

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 Water (3) - Liquid	Mole fraction of Aniline (1) - Liquid	Mole fraction of Aniline (1) - Gas	Mole fraction of Water (3) - Gas
333.15	10.36	0.1598	0.0903	0.0390	0.6123
333.15	11.10	0.1527	0.3474	0.0325	0.5975
333.15	11.67	0.1646	0.3748	0.0303	0.6406
333.15	12.14	0.1802	0.2167	0.0153	0.5945
333.15	13.08	0.1838	0.5124	0.0306	0.8212
333.15	13.62	0.2667	0.0853	0.0444	0.7394
333.15	16.59	0.3595	0.1815	0.0414	0.8634
333.15	17.15	0.2898	0.4321	0.0132	0.8883
333.15	17.40	0.4035	0.2852	0.0211	0.8125
333.15	20.12	0.4988	0.1878	0.0515	0.8982
363.15	36.06	0.1086	0.4129	0.0067	0.5880
363.15	36.95	0.1421	0.0886	0.0287	0.6002
363.15	40.76	0.1470	0.3005	0.0298	0.5999
363.15	46.21	0.1893	0.5123	0.0497	0.8121
363.15	48.02	0.2268	0.1057	0.0465	0.7539
363.15	49.40	0.2043	0.4259	0.0143	0.7587
363.15	51.14	0.2625	0.2854	0.0155	0.7986
363.15	53.79	0.2706	0.4043	0.0226	0.8436
363.15	58.84	0.3568	0.1223	0.0475	0.8366
363.15	71.82	0.5336	0.1717	0.0183	0.9437

Mole fraction of Cyclohexylamine (2) [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 (2) - Liquid mixture 1
298.15	0.0040	0.0230
298.15	0.0070	0.0000
298.15	0.0110	0.0530
298.15	0.0220	0.0800
298.15	0.0350	0.1000
298.15	0.0420	0.1110
298.15	0.0620	0.1250
298.15	0.0770	0.1330
298.15	0.0880	0.1380
298.15	0.1020	0.1430
298.15	0.1210	0.1470
298.15	0.1370	0.1500
298.15	0.1900	0.1580
298.15	0.2280	0.1590
298.15	0.2530	0.1520
298.15	0.2990	0.1480
298.15	0.3410	0.1410
298.15	0.3760	0.1310
298.15	0.4050	0.1300
298.15	0.4490	0.1210
298.15	0.4900	0.1100
298.15	0.5340	0.0980
298.15	0.5770	0.0840
298.15	0.6090	0.0730
298.15	0.6610	0.0530
298.15	0.6970	0.0380
298.15	0.7350	0.0190
298.15	0.7750	0.0000
333.15	0.0030	0.0220
333.15	0.0040	0.0380
333.15	0.0050	0.0470
333.15	0.0060	0.0580
333.15	0.0080	0.0680
333.15	0.0100	0.0770
333.15	0.0120	0.0860
333.15	0.0150	0.0940
333.15	0.0180	0.1010
333.15	0.0240	0.1120
333.15	0.0290	0.1180
333.15	0.0330	0.1240
333.15	0.0400	0.1310
333.15	0.0540	0.1410
333.15	0.0710	0.1490
333.15	0.0960	0.1670
333.15	0.1150	0.1750
333.15	0.1400	0.1830
333.15	0.1760	0.1910
333.15	0.2000	0.1910
333.15	0.2340	0.1900
333.15	0.2760	0.1870
333.15	0.3070	0.1820
333.15	0.3400	0.1720
333.15	0.3770	0.1670
333.15	0.4170	0.1580
333.15	0.4580	0.1420
333.15	0.4890	0.1290
333.15	0.5220	0.1140
333.15	0.5360	0.1110
333.15	0.5600	0.1010
333.15	0.5970	0.0880
333.15	0.6320	0.0730
333.15	0.6710	0.0530
333.15	0.7150	0.0000
333.15	0.0030	0.0290
333.15	0.0080	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 (2) - Liquid mixture 2	Mole fraction of Cyclohexylamine (2) - Liquid mixture 1	Mole fraction of Aniline (1) - Liquid mixture 1
298.15	0.0060	0.0030	0.1320	0.3200
298.15	0.0060	0.0030	0.1500	0.2330
298.15	0.0060	0.0060	0.1490	0.1220
333.15	0.0000	0.0040	0.1700	0.0920
333.15	0.0000	0.0050	0.1700	0.1180
333.15	0.0050	0.0040	0.1840	0.2180
333.15	0.0030	0.0050	0.1930	0.1650

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.