Mixture of Carbon dioxide + Butanoic acid, 2-methyl-, ethyl ester

Datasets

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

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.4050	313.20	0.9890
0.6050	313.20	0.9950
0.7800	313.20	0.9930
0.8940	313.20	0.9940
0.9620	313.20	0.9950
0.2050	323.20	0.9930
0.4280	323.20	0.9940
0.5360	323.20	0.9960
0.6620	323.20	0.9940
0.8120	323.20	0.9950
0.8570	323.20	0.9940
0.9040	323.20	0.9920
0.2230	333.20	0.9900
0.3950	333.20	0.9940
0.5100	333.20	0.9930
0.6120	333.20	0.9940
0.6690	333.20	0.9890
0.8020	333.20	0.9920
0.8520	333.20	0.9890

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.4050	313.20	0.9890
0.6050	313.20	0.9950
0.7800	313.20	0.9930
0.8940	313.20	0.9940
0.9620	313.20	0.9950
0.2050	323.20	0.9930
0.4280	323.20	0.9940
0.5360	323.20	0.9960
0.6620	323.20	0.9940
0.8120	323.20	0.9950
0.8570	323.20	0.9940
0.9040	323.20	0.9920
0.2230	333.20	0.9900
0.3950	333.20	0.9940
0.5100	333.20	0.9930
0.6120	333.20	0.9940
0.6690	333.20	0.9890
0.8020	333.20	0.9920
0.8520	333.20	0.9890

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.4050	313.20	2960.00
0.6050	313.20	4410.00
0.7800	313.20	5980.00
0.8940	313.20	7030.00
0.9620	313.20	7900.00
0.2050	323.20	2100.00
0.4280	323.20	3460.00
0.5360	323.20	4560.00
0.6620	323.20	5790.00
0.8120	323.20	7390.00
0.8570	323.20	8010.00
0.9040	323.20	8450.00
0.2230	333.20	2650.00
0.3950	333.20	4050.00
0.5100	333.20	5040.00
0.6120	333.20	6180.00
0.6690	333.20	6950.00
0.8020	333.20	8110.00
0.8520	333.20	9280.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.4050	313.20	2960.00
0.6050	313.20	4410.00
0.7800	313.20	5980.00
0.8940	313.20	7030.00
0.9620	313.20	7900.00
0.2050	323.20	2100.00
0.4280	323.20	3460.00
0.5360	323.20	4560.00
0.6620	323.20	5790.00
0.8120	323.20	7390.00
0.8570	323.20	8010.00
0.9040	323.20	8450.00
0.2230	333.20	2650.00
0.3950	333.20	4050.00
0.5100	333.20	5040.00
0.6120	333.20	6180.00
0.6690	333.20	6950.00
0.8020	333.20	8110.00
0.8520	333.20	9280.00

Sources

• High-pressure (vapor + liquid) equilibria for binary systems containing carbon dioxide and key apple odorants, hexanal and ethyl-2-methylbutyrate