Mixture of Acetonitrile + Morpholine + Dodecane

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	0.0866	0.9048	0.0443	0.0299
298.15	0.1295	0.8603	0.0461	0.0438
298.15	0.1766	0.8115	0.0468	0.0601
298.15	0.2430	0.7419	0.0487	0.0825
298.15	0.2959	0.6862	0.0501	0.1044
298.15	0.3843	0.5916	0.0557	0.1412
298.15	0.4390	0.5323	0.0572	0.1668
298.15	0.5215	0.4414	0.0584	0.2116
313.15	0.0411	0.9467	0.0539	0.0182
313.15	0.0925	0.8943	0.0562	0.0400
313.15	0.1425	0.8423	0.0617	0.0630
313.15	0.2699	0.7059	0.0733	0.1241
313.15	0.3365	0.6334	0.0817	0.1583
313.15	0.4054	0.5552	0.0846	0.1952
313.15	0.4721	0.4776	0.0900	0.2395
313.15	0.5555	0.3758	0.0941	0.3059

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	0.0454	0.0387
298.15	0.0547	0.0931
298.15	0.0621	0.1631
298.15	0.0913	0.4478
298.15	0.0945	0.5772
298.15	0.1106	0.6868
298.15	0.1694	0.7158
298.15	0.2756	0.6563
298.15	0.3642	0.5832
313.15	0.0761	0.1150
313.15	0.0909	0.1984
313.15	0.0996	0.3575
313.15	0.1140	0.4883
313.15	0.1398	0.6019
313.15	0.2729	0.6062
313.15	0.3217	0.5826

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	0.0866	0.9048	0.0443	0.0299
298.15	0.1295	0.8603	0.0461	0.0438
298.15	0.1766	0.8115	0.0468	0.0601
298.15	0.2430	0.7419	0.0487	0.0825
298.15	0.2959	0.6862	0.0501	0.1044
298.15	0.3843	0.5916	0.0557	0.1412
298.15	0.4390	0.5323	0.0572	0.1668
298.15	0.5215	0.4414	0.0584	0.2116
313.15	0.0411	0.9467	0.0539	0.0182
313.15	0.0925	0.8943	0.0562	0.0400
313.15	0.1425	0.8423	0.0617	0.0630
313.15	0.2699	0.7059	0.0733	0.1241
313.15	0.3365	0.6334	0.0817	0.1583
313.15	0.4054	0.5552	0.0846	0.1952
313.15	0.4721	0.4776	0.0900	0.2395
313.15	0.5555	0.3758	0.0941	0.3059

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	0.0454	0.0387
298.15	0.0547	0.0931
298.15	0.0621	0.1631
298.15	0.0913	0.4478
298.15	0.0945	0.5772
298.15	0.1106	0.6868
298.15	0.1694	0.7158
298.15	0.2756	0.6563
298.15	0.3642	0.5832
313.15	0.0761	0.1150
313.15	0.0909	0.1984
313.15	0.0996	0.3575
313.15	0.1140	0.4883
313.15	0.1398	0.6019
313.15	0.2729	0.6062
313.15	0.3217	0.5826

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