Mixture of Carbon dioxide + Tetradecanoic acid, ethyl ester

Datasets

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

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2470	308.50	6360.00
0.2470	318.40	7560.00
0.2470	328.60	8830.00
0.2470	338.20	10020.00
0.2470	348.70	11390.00
0.2470	358.50	12490.00
0.1880	308.50	7010.00
0.1880	318.50	8500.00
0.1880	328.70	10070.00
0.1880	338.30	11630.00
0.1880	348.80	13320.00
0.1880	358.60	14790.00
0.1350	308.40	7500.00
0.1350	318.50	9350.00
0.1350	328.60	11490.00
0.1350	338.60	13610.00
0.1350	348.70	15670.00
0.1350	358.30	17480.00
0.0947	308.50	7810.00
0.0947	318.50	10200.00
0.0947	328.60	12770.00
0.0947	338.70	15110.00
0.0947	348.90	17310.00
0.0947	358.50	19200.00
0.0699	308.50	7950.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2470	308.50	6360.00
0.2470	318.40	7560.00
0.2470	328.60	8830.00
0.2470	338.20	10020.00
0.2470	348.70	11390.00
0.2470	358.50	12490.00
0.1880	308.50	7010.00
0.1880	318.50	8500.00
0.1880	328.70	10070.00
0.1880	338.30	11630.00
0.1880	348.80	13320.00
0.1880	358.60	14790.00
0.1350	308.40	7500.00
0.1350	318.50	9350.00
0.1350	328.60	11490.00
0.1350	338.60	13610.00
0.1350	348.70	15670.00
0.1350	358.30	17480.00
0.0947	308.50	7810.00
0.0947	318.50	10200.00
0.0947	328.60	12770.00
0.0947	338.70	15110.00
0.0947	348.90	17310.00
0.0947	358.50	19200.00
0.0699	308.50	7950.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0699	318.60	10780.00
0.0699	328.70	13440.00
0.0699	338.90	15870.00
0.0699	348.40	17920.00
0.0699	358.60	19910.00
0.0499	308.50	8160.00
0.0499	318.50	11040.00
0.0499	328.50	13670.00
0.0499	338.40	15990.00
0.0499	348.70	18240.00
0.0499	358.60	20170.00
0.0397	308.50	8200.00
0.0397	318.50	11080.00
0.0397	328.50	13700.00
0.0397	338.30	15950.00
0.0397	348.90	18180.00
0.0397	358.60	20060.00
0.0381	308.30	8160.00
0.0381	318.40	11030.00
0.0381	328.40	13670.00
0.0381	338.20	15930.00
0.0381	348.60	18130.00
0.0381	358.50	20040.00
0.0237	308.40	8070.00
0.0237	318.40	10870.00
0.0237	328.60	13500.00
0.0237	339.00	15900.00
0.0237	348.60	17850.00
0.0237	358.20	19590.00
0.0152	308.30	7960.00
0.0152	318.20	10540.00
0.0152	328.40	13140.00
0.0152	338.30	15340.00
0.0152	348.60	17390.00
0.0152	358.10	19000.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Gas	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0699	318.60	10780.00
0.0699	328.70	13440.00
0.0699	338.90	15870.00
0.0699	348.40	17920.00
0.0699	358.60	19910.00
0.0499	308.50	8160.00
0.0499	318.50	11040.00
0.0499	328.50	13670.00
0.0499	338.40	15990.00
0.0499	348.70	18240.00
0.0499	358.60	20170.00
0.0397	308.50	8200.00
0.0397	318.50	11080.00
0.0397	328.50	13700.00
0.0397	338.30	15950.00
0.0397	348.90	18180.00
0.0397	358.60	20060.00
0.0381	308.30	8160.00
0.0381	318.40	11030.00
0.0381	328.40	13670.00
0.0381	338.20	15930.00
0.0381	348.60	18130.00
0.0381	358.50	20040.00
0.0237	308.40	8070.00
0.0237	318.40	10870.00
0.0237	328.60	13500.00
0.0237	339.00	15900.00
0.0237	348.60	17850.00
0.0237	358.20	19590.00
0.0152	308.30	7960.00
0.0152	318.20	10540.00
0.0152	328.40	13140.00
0.0152	338.30	15340.00
0.0152	348.60	17390.00
0.0152	358.10	19000.00

Sources

• High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series