Mixture of 1-Dodecanol + Phenol + Water

Datasets

1. Temperature, K x Mass fraction (2)

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mass fraction of Phenol (2) - Liquid mixture 1	Mass fraction of 1-Dodecanol (1) - Liquid mixture 1	Mass fraction of 1-Dodecanol (1) - Liquid mixture 2	Mass fraction of Phenol (2) - Liquid mixture 2
298.15	0.0000	0.9863	0.0006	0.0000
313.15	0.0000	0.9857	0.0008	0.0000
313.15	0.0560	0.9259	0.0007	0.0026
313.15	0.1214	0.8564	0.0007	0.0071
313.15	0.1824	0.7909	0.0006	0.0131
313.15	0.2391	0.7226	0.0006	0.0203
313.15	0.2918	0.6735	0.0005	0.0282
313.15	0.3393	0.6224	0.0004	0.0372
313.15	0.3822	0.5757	0.0004	0.0452
313.15	0.4199	0.5339	0.0003	0.0522
323.15	0.0000	0.9820	0.0011	0.0000
298.15	0.0367	0.9477	0.0006	0.0015
323.15	0.0319	0.9475	0.0010	0.0015
323.15	0.0981	0.8773	0.0010	0.0058
323.15	0.1563	0.8156	0.0009	0.0120
323.15	0.2245	0.7428	0.0008	0.0211
323.15	0.2761	0.6772	0.0006	0.0288
323.15	0.3122	0.6278	0.0005	0.0353
323.15	0.3556	0.5796	0.0005	0.0416
323.15	0.3922	0.5388	0.0004	0.0480
333.15	0.0000	0.9806	0.0012	0.0000
333.15	0.0553	0.9231	0.0010	0.0030
298.15	0.1081	0.8724	0.0005	0.0053
333.15	0.1320	0.8421	0.0009	0.0099
333.15	0.2013	0.7688	0.0009	0.0196
333.15	0.2822	0.6834	0.0008	0.0307
333.15	0.3403	0.6215	0.0006	0.0393
333.15	0.3995	0.5583	0.0005	0.0485
333.15	0.4405	0.5132	0.0005	0.0552
333.15	0.4659	0.4840	0.0004	0.0614
343.15	0.0000	0.9766	0.0013	0.0000
343.15	0.0560	0.9173	0.0011	0.0032
343.15	0.1277	0.8414	0.0010	0.0106
298.15	0.1655	0.8111	0.0004	0.0101
343.15	0.1924	0.7729	0.0009	0.0200
343.15	0.2516	0.7094	0.0009	0.0292
343.15	0.3112	0.6468	0.0008	0.0387
343.15	0.3749	0.5781	0.0006	0.0496
343.15	0.4491	0.5008	0.0006	0.0614
343.15	0.4797	0.4660	0.0005	0.0682
298.15	0.2299	0.7431	0.0003	0.0175
298.15	0.2869	0.6822	0.0003	0.0244
298.15	0.3518	0.6150	0.0003	0.0324
298.15	0.4053	0.5587	0.0002	0.0421
298.15	0.4431	0.5173	0.0001	0.0510

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed		Measured
Temperature, K - Liquid mixture 2	Mass fraction of Phenol (2) - Liquid mixture 1	Mass fraction of 1-Dodecanol (1) - Liquid mixture 1	Mass fraction of 1-Dodecanol (1) - Liquid mixture 2	Mass fraction of Phenol (2) - Liquid mixture 2
298.15	0.0000	0.9863	0.0006	0.0000
313.15	0.0000	0.9857	0.0008	0.0000
313.15	0.0560	0.9259	0.0007	0.0026
313.15	0.1214	0.8564	0.0007	0.0071
313.15	0.1824	0.7909	0.0006	0.0131
313.15	0.2391	0.7226	0.0006	0.0203
313.15	0.2918	0.6735	0.0005	0.0282
313.15	0.3393	0.6224	0.0004	0.0372
313.15	0.3822	0.5757	0.0004	0.0452
313.15	0.4199	0.5339	0.0003	0.0522
323.15	0.0000	0.9820	0.0011	0.0000
298.15	0.0367	0.9477	0.0006	0.0015
323.15	0.0319	0.9475	0.0010	0.0015
323.15	0.0981	0.8773	0.0010	0.0058
323.15	0.1563	0.8156	0.0009	0.0120
323.15	0.2245	0.7428	0.0008	0.0211
323.15	0.2761	0.6772	0.0006	0.0288
323.15	0.3122	0.6278	0.0005	0.0353
323.15	0.3556	0.5796	0.0005	0.0416
323.15	0.3922	0.5388	0.0004	0.0480
333.15	0.0000	0.9806	0.0012	0.0000
333.15	0.0553	0.9231	0.0010	0.0030
298.15	0.1081	0.8724	0.0005	0.0053
333.15	0.1320	0.8421	0.0009	0.0099
333.15	0.2013	0.7688	0.0009	0.0196
333.15	0.2822	0.6834	0.0008	0.0307
333.15	0.3403	0.6215	0.0006	0.0393
333.15	0.3995	0.5583	0.0005	0.0485
333.15	0.4405	0.5132	0.0005	0.0552
333.15	0.4659	0.4840	0.0004	0.0614
343.15	0.0000	0.9766	0.0013	0.0000
343.15	0.0560	0.9173	0.0011	0.0032
343.15	0.1277	0.8414	0.0010	0.0106
298.15	0.1655	0.8111	0.0004	0.0101
343.15	0.1924	0.7729	0.0009	0.0200
343.15	0.2516	0.7094	0.0009	0.0292
343.15	0.3112	0.6468	0.0008	0.0387
343.15	0.3749	0.5781	0.0006	0.0496
343.15	0.4491	0.5008	0.0006	0.0614
343.15	0.4797	0.4660	0.0005	0.0682
298.15	0.2299	0.7431	0.0003	0.0175
298.15	0.2869	0.6822	0.0003	0.0244
298.15	0.3518	0.6150	0.0003	0.0324
298.15	0.4053	0.5587	0.0002	0.0421
298.15	0.4431	0.5173	0.0001	0.0510

Sources

• Experimental Measurement and Thermodynamic Model of Liquid-Liquid Equilibrium for the Ternary System of 1-Dodecanol-Phenol-Water