Mixture of Carbon dioxide + 9,12,15-Octadecatrienoic acid, (Z,Z,Z)- + Ethanol

Datasets

1. Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Mole fraction of Carbon dioxide (1) - Liquid	Mole fraction of Ethanol (3) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.6536	0.1634	303.00	6780.00
0.6536	0.1634	313.00	8430.00
0.6536	0.1634	323.00	10290.00
0.6536	0.1634	333.00	12120.00
0.6536	0.1634	343.00	14070.00
0.6640	0.1660	303.00	7230.00
0.6640	0.1660	313.00	8870.00
0.6640	0.1660	323.00	10300.00
0.6640	0.1660	333.00	12320.00
0.6640	0.1660	343.00	14170.00
0.6832	0.1708	303.00	7430.00
0.6832	0.1708	313.00	9240.00
0.6832	0.1708	323.00	11230.00
0.6832	0.1708	333.00	13130.00
0.6832	0.1708	343.00	15220.00
0.7027	0.1757	303.00	7440.00
0.7027	0.1757	313.00	9520.00
0.7027	0.1757	323.00	11910.00
0.7027	0.1757	333.00	13990.00
0.7027	0.1757	343.00	16130.00
0.7224	0.1806	303.00	7400.00
0.7224	0.1806	313.00	9830.00
0.7224	0.1806	323.00	12670.00
0.7224	0.1806	333.00	14875.00
0.7224	0.1806	343.00	17070.00
0.7394	0.1849	303.00	8480.00
0.7394	0.1849	313.00	10790.00
0.7394	0.1849	323.00	13340.00
0.7394	0.1849	333.00	15480.00
0.7394	0.1849	343.00	17600.00
0.7552	0.1888	303.00	9220.00
0.7552	0.1888	313.00	11510.00
0.7552	0.1888	323.00	13850.00
0.7552	0.1888	333.00	16230.00
0.7552	0.1888	343.00	18220.00
0.7606	0.1902	303.00	9400.00
0.7606	0.1902	313.00	11600.00
0.7606	0.1902	323.00	13780.00
0.7606	0.1902	333.00	16040.00
0.7606	0.1902	343.00	18150.00
0.7718	0.1929	303.00	8410.00
0.7718	0.1929	313.00	10660.00
0.7718	0.1929	323.00	12910.00
0.7718	0.1929	333.00	15200.00
0.7718	0.1929	343.00	17180.00
0.7856	0.1964	303.00	6710.00
0.7856	0.1964	313.00	8460.00
0.7856	0.1964	323.00	10910.00
0.7856	0.1964	333.00	13070.00
0.7856	0.1964	343.00	15060.00
0.7996	0.1999	303.00	6235.00
0.7996	0.1999	313.00	7675.00
0.7996	0.1999	323.00	9510.00
0.7996	0.1999	333.00	11575.00
0.7996	0.1999	343.00	13470.00

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Mole fraction of Carbon dioxide (1) - Liquid	Mole fraction of Ethanol (3) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.6536	0.1634	303.00	6780.00
0.6536	0.1634	313.00	8430.00
0.6536	0.1634	323.00	10290.00
0.6536	0.1634	333.00	12120.00
0.6536	0.1634	343.00	14070.00
0.6640	0.1660	303.00	7230.00
0.6640	0.1660	313.00	8870.00
0.6640	0.1660	323.00	10300.00
0.6640	0.1660	333.00	12320.00
0.6640	0.1660	343.00	14170.00
0.6832	0.1708	303.00	7430.00
0.6832	0.1708	313.00	9240.00
0.6832	0.1708	323.00	11230.00
0.6832	0.1708	333.00	13130.00
0.6832	0.1708	343.00	15220.00
0.7027	0.1757	303.00	7440.00
0.7027	0.1757	313.00	9520.00
0.7027	0.1757	323.00	11910.00
0.7027	0.1757	333.00	13990.00
0.7027	0.1757	343.00	16130.00
0.7224	0.1806	303.00	7400.00
0.7224	0.1806	313.00	9830.00
0.7224	0.1806	323.00	12670.00
0.7224	0.1806	333.00	14875.00
0.7224	0.1806	343.00	17070.00
0.7394	0.1849	303.00	8480.00
0.7394	0.1849	313.00	10790.00
0.7394	0.1849	323.00	13340.00
0.7394	0.1849	333.00	15480.00
0.7394	0.1849	343.00	17600.00
0.7552	0.1888	303.00	9220.00
0.7552	0.1888	313.00	11510.00
0.7552	0.1888	323.00	13850.00
0.7552	0.1888	333.00	16230.00
0.7552	0.1888	343.00	18220.00
0.7606	0.1902	303.00	9400.00
0.7606	0.1902	313.00	11600.00
0.7606	0.1902	323.00	13780.00
0.7606	0.1902	333.00	16040.00
0.7606	0.1902	343.00	18150.00
0.7718	0.1929	303.00	8410.00
0.7718	0.1929	313.00	10660.00
0.7718	0.1929	323.00	12910.00
0.7718	0.1929	333.00	15200.00
0.7718	0.1929	343.00	17180.00
0.7856	0.1964	303.00	6710.00
0.7856	0.1964	313.00	8460.00
0.7856	0.1964	323.00	10910.00
0.7856	0.1964	333.00	13070.00
0.7856	0.1964	343.00	15060.00
0.7996	0.1999	303.00	6235.00
0.7996	0.1999	313.00	7675.00
0.7996	0.1999	323.00	9510.00
0.7996	0.1999	333.00	11575.00
0.7996	0.1999	343.00	13470.00

Sources

• Phase equilibrium measurements of ternary systems formed by linoleic and linolenic acids in carbon dioxide/ethanol mixtures