Mixture of Decanoic acid, ethyl ester + Carbon dioxide

Datasets

1. P_c - Critical pressure, kPa (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. T_c - Critical temperature, K (2)
4. Vapor or sublimation pressure, kPa (2)

Critical pressure, kPa [ref]

Mole fraction of Carbon dioxide (2) - Liquid	Critical pressure, kPa - Liquid
0.4957	9417.40
0.6026	11241.70
0.7088	13282.90
0.8033	15380.50
0.8591	17949.90
1.0000	7379.80

Critical pressure, kPa [ref]

Mole fraction of Carbon dioxide (2) - Liquid	Critical pressure, kPa - Liquid
0.4957	9417.40
0.6026	11241.70
0.7088	13282.90
0.8033	15380.50
0.8591	17949.90
1.0000	7379.80

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Decanoic acid, ethyl ester (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2750	308.50	5860.00
0.2750	318.60	6910.00
0.2750	328.70	8000.00
0.2750	338.70	9120.00
0.2750	348.70	10200.00
0.2750	358.50	11290.00
0.2120	308.40	6490.00
0.2120	318.40	7760.00
0.2120	328.60	9120.00
0.2120	338.70	10460.00
0.2120	348.70	11840.00
0.2120	358.70	13250.00
0.1620	308.50	6930.00
0.1620	318.50	8290.00
0.1620	328.50	9780.00
0.1620	338.60	11400.00
0.1620	348.60	13010.00
0.1620	358.60	14520.00
0.1250	308.40	7140.00
0.1250	318.30	8640.00
0.1250	328.30	10340.00
0.1250	338.20	12130.00
0.1250	348.20	13800.00
0.1250	358.50	15460.00
0.0875	308.40	7390.00
0.0875	318.30	9020.00
0.0875	328.40	10880.00
0.0875	338.40	12800.00
0.0875	348.50	14690.00
0.0622	308.50	7590.00
0.0622	318.60	9300.00
0.0469	308.50	7580.00
0.0469	318.40	9260.00
0.0287	308.50	7720.00
0.0187	308.50	7840.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Decanoic acid, ethyl ester (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2750	308.50	5860.00
0.2750	318.60	6910.00
0.2750	328.70	8000.00
0.2750	338.70	9120.00
0.2750	348.70	10200.00
0.2750	358.50	11290.00
0.2120	308.40	6490.00
0.2120	318.40	7760.00
0.2120	328.60	9120.00
0.2120	338.70	10460.00
0.2120	348.70	11840.00
0.2120	358.70	13250.00
0.1620	308.50	6930.00
0.1620	318.50	8290.00
0.1620	328.50	9780.00
0.1620	338.60	11400.00
0.1620	348.60	13010.00
0.1620	358.60	14520.00
0.1250	308.40	7140.00
0.1250	318.30	8640.00
0.1250	328.30	10340.00
0.1250	338.20	12130.00
0.1250	348.20	13800.00
0.1250	358.50	15460.00
0.0875	308.40	7390.00
0.0875	318.30	9020.00
0.0875	328.40	10880.00
0.0875	338.40	12800.00
0.0875	348.50	14690.00
0.0622	308.50	7590.00
0.0622	318.60	9300.00
0.0469	308.50	7580.00
0.0469	318.40	9260.00
0.0287	308.50	7720.00
0.0187	308.50	7840.00

Critical temperature, K [ref]

Mole fraction of Carbon dioxide (2) - Liquid	Critical temperature, K - Liquid
0.4957	651.03
0.6026	638.61
0.7088	622.49
0.8033	605.65
0.8591	578.03
1.0000	304.30

Critical temperature, K [ref]

Mole fraction of Carbon dioxide (2) - Liquid	Critical temperature, K - Liquid
0.4957	651.03
0.6026	638.61
0.7088	622.49
0.8033	605.65
0.8591	578.03
1.0000	304.30

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Decanoic acid, ethyl ester (1) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0875	358.40	16430.00
0.0622	328.50	11260.00
0.0622	338.60	13300.00
0.0622	348.60	15120.00
0.0622	358.70	16770.00
0.0469	328.50	11330.00
0.0469	338.60	13310.00
0.0469	348.80	15110.00
0.0469	358.80	16720.00
0.0287	318.50	9510.00
0.0287	328.50	11420.00
0.0287	338.60	13320.00
0.0287	348.80	15040.00
0.0287	358.80	16560.00
0.0187	318.50	9610.00
0.0187	328.50	11440.00
0.0187	338.60	13260.00
0.0187	348.70	14850.00
0.0187	358.80	16210.00
0.0129	308.10	7670.00
0.0129	318.60	9370.00
0.0129	328.60	11180.00
0.0129	338.70	12930.00
0.0129	348.50	14380.00
0.0129	358.50	15520.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Decanoic acid, ethyl ester (1) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0875	358.40	16430.00
0.0622	328.50	11260.00
0.0622	338.60	13300.00
0.0622	348.60	15120.00
0.0622	358.70	16770.00
0.0469	328.50	11330.00
0.0469	338.60	13310.00
0.0469	348.80	15110.00
0.0469	358.80	16720.00
0.0287	318.50	9510.00
0.0287	328.50	11420.00
0.0287	338.60	13320.00
0.0287	348.80	15040.00
0.0287	358.80	16560.00
0.0187	318.50	9610.00
0.0187	328.50	11440.00
0.0187	338.60	13260.00
0.0187	348.70	14850.00
0.0187	358.80	16210.00
0.0129	308.10	7670.00
0.0129	318.60	9370.00
0.0129	328.60	11180.00
0.0129	338.70	12930.00
0.0129	348.50	14380.00
0.0129	358.50	15520.00

Sources

• High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements