Mixture of Cyclohexane, methyl- + Tetrahydrofuran + Water

Datasets

1. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mole fraction of Tetrahydrofuran (2) - Liquid mixture 1	Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1	Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2	Mole fraction of Tetrahydrofuran (2) - Liquid mixture 2
278.15	0.0000	0.9995	0.0000	0.0000
278.15	0.7258	0.0793	0.0002	0.1905
278.15	0.1065	0.8928	0.0001	0.0180
278.15	0.2548	0.7443	0.0001	0.0374
278.15	0.4031	0.5882	0.0001	0.0576
278.15	0.4369	0.5496	0.0001	0.0630
278.15	0.5990	0.3614	0.0001	0.0943
278.15	0.7029	0.2174	0.0001	0.1280
278.15	0.7396	0.1174	0.0001	0.1821
278.15	0.7385	0.1044	0.0001	0.1860
288.15	0.5186	0.4649	0.0001	0.0529
288.15	0.0000	0.9980	0.0001	0.0000
288.15	0.5375	0.4453	0.0002	0.0585
288.15	0.5949	0.3792	0.0002	0.0675
288.15	0.6812	0.2516	0.0002	0.0830
288.15	0.7231	0.1715	0.0002	0.0978
288.15	0.7281	0.1148	0.0002	0.1168
288.15	0.7296	0.1271	0.0002	0.1179
288.15	0.7018	0.0759	0.0002	0.1539
288.15	0.0827	0.9153	0.0001	0.0101
288.15	0.1633	0.8344	0.0001	0.0166
288.15	0.1670	0.8297	0.0001	0.0172
288.15	0.2192	0.7755	0.0001	0.0225
288.15	0.2823	0.7114	0.0001	0.0282
288.15	0.3798	0.6120	0.0001	0.0455
288.15	0.4685	0.5170	0.0001	0.0524
298.15	0.6476	0.2915	0.0003	0.0685
298.15	0.7024	0.1900	0.0003	0.0853
298.15	0.7109	0.1613	0.0004	0.0966
298.15	0.7098	0.1173	0.0004	0.1083
298.15	0.6844	0.0710	0.0005	0.1252
298.15	0.6615	0.0604	0.0007	0.1365
298.15	0.6191	0.0435	0.0007	0.1614
298.15	0.0797	0.9163	0.0001	0.0068
298.15	0.2120	0.7839	0.0002	0.0186
298.15	0.0000	0.9967	0.0001	0.0000
298.15	0.3144	0.6745	0.0002	0.0273
298.15	0.4554	0.5246	0.0002	0.0429
298.15	0.5542	0.4130	0.0002	0.0522
323.15	0.3698	0.6095	0.0003	0.0186
323.15	0.4098	0.5652	0.0003	0.0234
323.15	0.4460	0.5250	0.0004	0.0266
323.15	0.5496	0.4068	0.0004	0.0322
323.15	0.5986	0.3442	0.0006	0.0421
323.15	0.0000	0.9941	0.0002	0.0000
323.15	0.6336	0.3003	0.0007	0.0451
323.15	0.6708	0.2309	0.0007	0.0483
323.15	0.6911	0.1822	0.0008	0.0651
323.15	0.6975	0.1611	0.0009	0.0655
323.15	0.6928	0.1353	0.0009	0.0599
323.15	0.6803	0.1022	0.0009	0.0794
323.15	0.6588	0.0821	0.0009	0.0882
323.15	0.6309	0.0599	0.0009	0.0811
323.15	0.6134	0.0553	0.0009	0.0983
323.15	0.0875	0.9069	0.0002	0.0042
323.15	0.1448	0.8494	0.0002	0.0090
323.15	0.2645	0.7253	0.0002	0.0168
323.15	0.2933	0.6940	0.0003	0.0169
343.15	0.2265	0.7510	0.0012	0.0084
343.15	0.0000	0.9919	0.0005	0.0000
343.15	0.0378	0.9525	0.0008	0.0012
343.15	0.1276	0.8578	0.0011	0.0049

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mole fraction of Tetrahydrofuran (2) - Liquid mixture 1	Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1	Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2	Mole fraction of Tetrahydrofuran (2) - Liquid mixture 2
278.15	0.0000	0.9995	0.0000	0.0000
278.15	0.7258	0.0793	0.0002	0.1905
278.15	0.1065	0.8928	0.0001	0.0180
278.15	0.2548	0.7443	0.0001	0.0374
278.15	0.4031	0.5882	0.0001	0.0576
278.15	0.4369	0.5496	0.0001	0.0630
278.15	0.5990	0.3614	0.0001	0.0943
278.15	0.7029	0.2174	0.0001	0.1280
278.15	0.7396	0.1174	0.0001	0.1821
278.15	0.7385	0.1044	0.0001	0.1860
288.15	0.5186	0.4649	0.0001	0.0529
288.15	0.0000	0.9980	0.0001	0.0000
288.15	0.5375	0.4453	0.0002	0.0585
288.15	0.5949	0.3792	0.0002	0.0675
288.15	0.6812	0.2516	0.0002	0.0830
288.15	0.7231	0.1715	0.0002	0.0978
288.15	0.7281	0.1148	0.0002	0.1168
288.15	0.7296	0.1271	0.0002	0.1179
288.15	0.7018	0.0759	0.0002	0.1539
288.15	0.0827	0.9153	0.0001	0.0101
288.15	0.1633	0.8344	0.0001	0.0166
288.15	0.1670	0.8297	0.0001	0.0172
288.15	0.2192	0.7755	0.0001	0.0225
288.15	0.2823	0.7114	0.0001	0.0282
288.15	0.3798	0.6120	0.0001	0.0455
288.15	0.4685	0.5170	0.0001	0.0524
298.15	0.6476	0.2915	0.0003	0.0685
298.15	0.7024	0.1900	0.0003	0.0853
298.15	0.7109	0.1613	0.0004	0.0966
298.15	0.7098	0.1173	0.0004	0.1083
298.15	0.6844	0.0710	0.0005	0.1252
298.15	0.6615	0.0604	0.0007	0.1365
298.15	0.6191	0.0435	0.0007	0.1614
298.15	0.0797	0.9163	0.0001	0.0068
298.15	0.2120	0.7839	0.0002	0.0186
298.15	0.0000	0.9967	0.0001	0.0000
298.15	0.3144	0.6745	0.0002	0.0273
298.15	0.4554	0.5246	0.0002	0.0429
298.15	0.5542	0.4130	0.0002	0.0522
323.15	0.3698	0.6095	0.0003	0.0186
323.15	0.4098	0.5652	0.0003	0.0234
323.15	0.4460	0.5250	0.0004	0.0266
323.15	0.5496	0.4068	0.0004	0.0322
323.15	0.5986	0.3442	0.0006	0.0421
323.15	0.0000	0.9941	0.0002	0.0000
323.15	0.6336	0.3003	0.0007	0.0451
323.15	0.6708	0.2309	0.0007	0.0483
323.15	0.6911	0.1822	0.0008	0.0651
323.15	0.6975	0.1611	0.0009	0.0655
323.15	0.6928	0.1353	0.0009	0.0599
323.15	0.6803	0.1022	0.0009	0.0794
323.15	0.6588	0.0821	0.0009	0.0882
323.15	0.6309	0.0599	0.0009	0.0811
323.15	0.6134	0.0553	0.0009	0.0983
323.15	0.0875	0.9069	0.0002	0.0042
323.15	0.1448	0.8494	0.0002	0.0090
323.15	0.2645	0.7253	0.0002	0.0168
323.15	0.2933	0.6940	0.0003	0.0169
343.15	0.2265	0.7510	0.0012	0.0084
343.15	0.0000	0.9919	0.0005	0.0000
343.15	0.0378	0.9525	0.0008	0.0012
343.15	0.1276	0.8578	0.0011	0.0049

Sources

• (Liquid + liquid) equilibria in the (water + tetrahydrofuran + methylcyclohexane) ternary system at temperatures between (278 and 343) K and atmospheric pressure: Experimental data and correlation