Mixture of Acetonitrile + Morpholine + Decane

Datasets

1. Temperature, K x Mole fraction (4)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 2	Mole fraction of Acetonitrile (1) - Liquid mixture 2	Mole fraction of Acetonitrile (1) - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 1
298.15	0.0456	0.9387	0.0572	0.0155
298.15	0.1227	0.8570	0.0590	0.0414
298.15	0.1746	0.8020	0.0627	0.0592
298.15	0.2319	0.7399	0.0683	0.0799
298.15	0.2915	0.6744	0.0716	0.1034
298.15	0.3653	0.5919	0.0727	0.1347
298.15	0.4224	0.5263	0.0771	0.1625
298.15	0.4900	0.4459	0.0777	0.2013
313.15	0.0438	0.9342	0.0543	0.0178
313.15	0.1210	0.8516	0.0706	0.0515
313.15	0.1731	0.7939	0.0755	0.0742
313.15	0.2276	0.7331	0.0885	0.0993
313.15	0.2837	0.6687	0.0963	0.1277
313.15	0.3487	0.5928	0.1083	0.1617
313.15	0.4073	0.5184	0.1201	0.2069
313.15	0.4566	0.4494	0.1333	0.2496

Mole fraction of Morpholine (2) [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Acetonitrile (1) - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 1
298.15	0.0644	0.0648
298.15	0.0796	0.2911
298.15	0.0817	0.1581
298.15	0.0958	0.5000
298.15	0.1423	0.6373
298.15	0.2792	0.6076
298.15	0.3459	0.5604
298.15	0.4121	0.5122
313.15	0.0734	0.0422
313.15	0.1020	0.1441
313.15	0.1300	0.2252
313.15	0.2051	0.4526
313.15	0.3185	0.5046
313.15	0.4567	0.4468

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 2	Mole fraction of Acetonitrile (1) - Liquid mixture 2	Mole fraction of Acetonitrile (1) - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 1
298.15	0.0456	0.9387	0.0572	0.0155
298.15	0.1227	0.8570	0.0590	0.0414
298.15	0.1746	0.8020	0.0627	0.0592
298.15	0.2319	0.7399	0.0683	0.0799
298.15	0.2915	0.6744	0.0716	0.1034
298.15	0.3653	0.5919	0.0727	0.1347
298.15	0.4224	0.5263	0.0771	0.1625
298.15	0.4900	0.4459	0.0777	0.2013
313.15	0.0438	0.9342	0.0543	0.0178
313.15	0.1210	0.8516	0.0706	0.0515
313.15	0.1731	0.7939	0.0755	0.0742
313.15	0.2276	0.7331	0.0885	0.0993
313.15	0.2837	0.6687	0.0963	0.1277
313.15	0.3487	0.5928	0.1083	0.1617
313.15	0.4073	0.5184	0.1201	0.2069
313.15	0.4566	0.4494	0.1333	0.2496

Mole fraction of Morpholine (2) [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Acetonitrile (1) - Liquid mixture 1	Mole fraction of Morpholine (2) - Liquid mixture 1
298.15	0.0644	0.0648
298.15	0.0796	0.2911
298.15	0.0817	0.1581
298.15	0.0958	0.5000
298.15	0.1423	0.6373
298.15	0.2792	0.6076
298.15	0.3459	0.5604
298.15	0.4121	0.5122
313.15	0.0734	0.0422
313.15	0.1020	0.1441
313.15	0.1300	0.2252
313.15	0.2051	0.4526
313.15	0.3185	0.5046
313.15	0.4567	0.4468

Sources

• Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K