Mixture of Carbon dioxide + Hexadecanoic acid, ethyl ester

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (12)
2. Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.5033	3100.00
303.15	0.5845	4140.00
303.15	0.7398	5590.00
303.15	0.8163	5950.00
303.15	0.8666	6430.00
313.15	0.5033	3520.00
313.15	0.5845	4820.00
313.15	0.7398	6510.00
313.15	0.8163	7750.00
313.15	0.8666	8510.00
313.15	0.8984	9570.00
313.15	0.9368	10750.00
323.15	0.5033	4110.00
323.15	0.5845	5280.00
323.15	0.7398	7600.00
323.15	0.8163	9540.00
323.15	0.8666	10500.00
323.15	0.8984	12060.00
323.15	0.9368	13450.00
333.15	0.5033	4590.00
333.15	0.5845	5930.00
333.15	0.7398	8980.00
333.15	0.8163	11380.00
333.15	0.8666	12950.00
333.15	0.8984	14700.00
333.15	0.9368	15800.00
343.15	0.5033	5250.00
343.15	0.5845	6900.00
343.15	0.7398	9980.00
343.15	0.8163	13230.00
343.15	0.8666	14860.00
343.15	0.8984	17050.00
343.15	0.9368	18310.00
353.15	0.5033	6020.00
353.15	0.5845	7570.00
353.15	0.7398	11100.00
353.15	0.8163	14940.00
353.15	0.8666	17100.00
353.15	0.8984	19050.00
353.15	0.9368	20360.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.9913	6740.00
313.15	0.9628	11070.00
313.15	0.9808	10430.00
313.15	0.9913	9640.00
323.15	0.9628	13670.00
323.15	0.9808	13300.00
323.15	0.9913	12150.00
333.15	0.9628	16420.00
333.15	0.9808	15730.00
333.15	0.9913	14480.00
343.15	0.9628	18760.00
343.15	0.9808	18280.00
343.15	0.9913	16740.00
353.15	0.9628	20860.00
353.15	0.9808	20300.00
353.15	0.9913	18750.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 303.15 (Liquid mixture 1)

Mole fraction of Carbon dioxide (1) - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8984	7000.00
0.9368	7940.00
0.9628	8070.00
0.9808	7570.00

Vapor or sublimation pressure, kPa [ref]

Mole fraction of Carbon dioxide (1) - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8984	6780.00

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
303.15	6780.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Hexadecanoic acid, ethyl ester (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2190	308.50	6700.00
0.2190	318.50	7930.00
0.2190	328.50	9400.00
0.2190	338.70	10930.00
0.2190	348.20	12380.00
0.2190	358.30	13820.00
0.1620	308.60	7360.00
0.1620	318.70	8990.00
0.1620	328.80	11000.00
0.1620	338.80	13010.00
0.1620	348.50	14880.00
0.1620	358.40	16670.00
0.1170	308.60	7910.00
0.1170	318.60	10370.00
0.1170	328.70	13000.00
0.1170	338.90	15340.00
0.1170	348.40	17460.00
0.1170	358.50	19470.00
0.0932	309.10	9040.00
0.0932	318.30	11620.00
0.0932	328.20	14170.00
0.0932	338.50	16650.00
0.0932	348.80	18750.00
0.0932	358.60	20610.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.5033	3100.00
303.15	0.5845	4140.00
303.15	0.7398	5590.00
303.15	0.8163	5950.00
303.15	0.8666	6430.00
313.15	0.5033	3520.00
313.15	0.5845	4820.00
313.15	0.7398	6510.00
313.15	0.8163	7750.00
313.15	0.8666	8510.00
313.15	0.8984	9570.00
313.15	0.9368	10750.00
323.15	0.5033	4110.00
323.15	0.5845	5280.00
323.15	0.7398	7600.00
323.15	0.8163	9540.00
323.15	0.8666	10500.00
323.15	0.8984	12060.00
323.15	0.9368	13450.00
333.15	0.5033	4590.00
333.15	0.5845	5930.00
333.15	0.7398	8980.00
333.15	0.8163	11380.00
333.15	0.8666	12950.00
333.15	0.8984	14700.00
333.15	0.9368	15800.00
343.15	0.5033	5250.00
343.15	0.5845	6900.00
343.15	0.7398	9980.00
343.15	0.8163	13230.00
343.15	0.8666	14860.00
343.15	0.8984	17050.00
343.15	0.9368	18310.00
353.15	0.5033	6020.00
353.15	0.5845	7570.00
353.15	0.7398	11100.00
353.15	0.8163	14940.00
353.15	0.8666	17100.00
353.15	0.8984	19050.00
353.15	0.9368	20360.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.9913	6740.00
313.15	0.9628	11070.00
313.15	0.9808	10430.00
313.15	0.9913	9640.00
323.15	0.9628	13670.00
323.15	0.9808	13300.00
323.15	0.9913	12150.00
333.15	0.9628	16420.00
333.15	0.9808	15730.00
333.15	0.9913	14480.00
343.15	0.9628	18760.00
343.15	0.9808	18280.00
343.15	0.9913	16740.00
353.15	0.9628	20860.00
353.15	0.9808	20300.00
353.15	0.9913	18750.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 303.15 (Liquid mixture 1)

Mole fraction of Carbon dioxide (1) - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8984	7000.00
0.9368	7940.00
0.9628	8070.00
0.9808	7570.00

Vapor or sublimation pressure, kPa [ref]

Mole fraction of Carbon dioxide (1) - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8984	6780.00

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 1
303.15	6780.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Hexadecanoic acid, ethyl ester (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2190	308.50	6700.00
0.2190	318.50	7930.00
0.2190	328.50	9400.00
0.2190	338.70	10930.00
0.2190	348.20	12380.00
0.2190	358.30	13820.00
0.1620	308.60	7360.00
0.1620	318.70	8990.00
0.1620	328.80	11000.00
0.1620	338.80	13010.00
0.1620	348.50	14880.00
0.1620	358.40	16670.00
0.1170	308.60	7910.00
0.1170	318.60	10370.00
0.1170	328.70	13000.00
0.1170	338.90	15340.00
0.1170	348.40	17460.00
0.1170	358.50	19470.00
0.0932	309.10	9040.00
0.0932	318.30	11620.00
0.0932	328.20	14170.00
0.0932	338.50	16650.00
0.0932	348.80	18750.00
0.0932	358.60	20610.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Hexadecanoic acid, ethyl ester (2) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0637	308.60	10090.00
0.0637	318.10	12850.00
0.0637	328.20	15650.00
0.0637	338.70	18180.00
0.0637	349.00	20550.00
0.0637	359.60	22720.00
0.0477	308.60	10710.00
0.0477	319.20	13780.00
0.0477	328.80	16310.00
0.0477	338.30	18630.00
0.0477	348.70	20950.00
0.0477	358.40	23010.00
0.0324	308.30	10380.00
0.0324	318.40	13360.00
0.0324	328.30	15950.00
0.0324	338.50	18440.00
0.0324	348.80	20690.00
0.0324	358.60	22600.00
0.0202	308.60	10290.00
0.0202	318.30	13200.00
0.0202	328.30	15860.00
0.0202	338.30	18290.00
0.0202	348.30	20390.00
0.0202	358.40	22370.00
0.0135	308.50	9540.00
0.0135	318.70	12650.00
0.0135	328.50	15360.00
0.0135	338.20	17710.00
0.0135	348.60	20020.00
0.0135	358.30	21880.00
0.0077	308.40	8760.00
0.0077	318.80	11740.00
0.0077	328.60	14280.00
0.0077	338.30	16320.00
0.0077	348.50	18430.00
0.0077	358.40	20570.00
0.0051	308.70	8480.00
0.0051	318.70	11170.00
0.0051	328.80	13450.00
0.0051	338.40	15420.00
0.0051	348.40	17230.00
0.0051	358.50	19170.00
0.0027	308.30	8060.00
0.0027	318.60	10530.00
0.0027	328.50	12640.00
0.0027	338.30	14470.00
0.0027	348.60	15910.00
0.0027	358.50	17490.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Hexadecanoic acid, ethyl ester (2) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0637	308.60	10090.00
0.0637	318.10	12850.00
0.0637	328.20	15650.00
0.0637	338.70	18180.00
0.0637	349.00	20550.00
0.0637	359.60	22720.00
0.0477	308.60	10710.00
0.0477	319.20	13780.00
0.0477	328.80	16310.00
0.0477	338.30	18630.00
0.0477	348.70	20950.00
0.0477	358.40	23010.00
0.0324	308.30	10380.00
0.0324	318.40	13360.00
0.0324	328.30	15950.00
0.0324	338.50	18440.00
0.0324	348.80	20690.00
0.0324	358.60	22600.00
0.0202	308.60	10290.00
0.0202	318.30	13200.00
0.0202	328.30	15860.00
0.0202	338.30	18290.00
0.0202	348.30	20390.00
0.0202	358.40	22370.00
0.0135	308.50	9540.00
0.0135	318.70	12650.00
0.0135	328.50	15360.00
0.0135	338.20	17710.00
0.0135	348.60	20020.00
0.0135	358.30	21880.00
0.0077	308.40	8760.00
0.0077	318.80	11740.00
0.0077	328.60	14280.00
0.0077	338.30	16320.00
0.0077	348.50	18430.00
0.0077	358.40	20570.00
0.0051	308.70	8480.00
0.0051	318.70	11170.00
0.0051	328.80	13450.00
0.0051	338.40	15420.00
0.0051	348.40	17230.00
0.0051	358.50	19170.00
0.0027	308.30	8060.00
0.0027	318.60	10530.00
0.0027	328.50	12640.00
0.0027	338.30	14470.00
0.0027	348.60	15910.00
0.0027	358.50	17490.00

Sources

• Phase equilibrium measurements and thermodynamic modelling for the system (CO2 + ethyl palmitate + ethanol) at high pressures
• High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series