Mixture of Carbon dioxide + Methylene chloride

Datasets

1. Henry's Law constant (mole fraction scale), kPa (2)
2. P_vap - Vapor or sublimation pressure, kPa (6)
3. Vapor or sublimation pressure, kPa (4)
4. V_m - Molar volume, m3/mol (2)

Henry's Law constant (mole fraction scale), kPa of Carbon dioxide (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of Carbon dioxide (1) - Liquid
283.15	9727.0
288.15	10550.0
293.15	11400.0
298.15	12300.0
303.15	13230.0
308.15	14200.0
313.15	15210.0
318.15	16250.0
323.15	17330.0

Henry's Law constant (mole fraction scale), kPa of Carbon dioxide (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (mole fraction scale), kPa of Carbon dioxide (1) - Liquid
283.15	9727.0
288.15	10550.0
293.15	11400.0
298.15	12300.0
303.15	13230.0
308.15	14200.0
313.15	15210.0
318.15	16250.0
323.15	17330.0

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1580	308.20	1730.00
0.1580	318.20	2030.00
0.1580	328.20	2410.00
0.2970	308.20	2880.00
0.2970	318.20	3390.00
0.2970	328.20	3990.00
0.4110	308.20	3680.00
0.4110	318.20	4310.00
0.4110	328.20	5040.00
0.5360	308.20	4420.00
0.5360	318.20	5250.00
0.5360	328.20	6180.00
0.6540	308.20	5150.00
0.6540	318.20	6140.00
0.6540	328.20	7120.00
0.7060	308.20	5390.00
0.7060	318.20	6520.00
0.7060	328.20	7610.00
0.7850	308.20	5910.00
0.7850	318.20	6930.00
0.7850	328.20	8200.00
0.8510	308.20	6330.00
0.8510	318.20	7580.00
0.8510	328.20	8920.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.00	0.5686	4650.00
313.00	0.6580	5390.00
313.00	0.7437	5940.00
313.00	0.8527	6810.00
313.00	0.9301	7430.00
313.00	0.9378	7620.00
313.00	0.9470	7720.00
323.00	0.5686	5630.00
323.00	0.6580	6370.00
323.00	0.7437	7040.00
323.00	0.8522	8260.00
323.00	0.8977	8690.00
323.00	0.9301	8750.00
323.00	0.9378	8730.00
333.00	0.5686	6470.00
333.00	0.6580	7300.00
333.00	0.7437	8140.00
333.00	0.8522	9290.00
333.00	0.8977	9630.00
343.00	0.5686	7330.00
343.00	0.6580	8380.00
343.00	0.7437	9170.00
343.00	0.8522	10190.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0440	550.00
0.1140	1240.00
0.1880	1920.00
0.2690	2630.00
0.4440	4010.00
0.5330	4660.00
0.6440	5340.00
0.7380	6020.00
0.8300	6680.00
0.8590	6950.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1580	308.20	1730.00
0.1580	318.20	2030.00
0.1580	328.20	2410.00
0.2970	308.20	2880.00
0.2970	318.20	3390.00
0.2970	328.20	3990.00
0.4110	308.20	3680.00
0.4110	318.20	4310.00
0.4110	328.20	5040.00
0.5360	308.20	4420.00
0.5360	318.20	5250.00
0.5360	328.20	6180.00
0.6540	308.20	5150.00
0.6540	318.20	6140.00
0.6540	328.20	7120.00
0.7060	308.20	5390.00
0.7060	318.20	6520.00
0.7060	328.20	7610.00
0.7850	308.20	5910.00
0.7850	318.20	6930.00
0.7850	328.20	8200.00
0.8510	308.20	6330.00
0.8510	318.20	7580.00
0.8510	328.20	8920.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.00	0.5686	4650.00
313.00	0.6580	5390.00
313.00	0.7437	5940.00
313.00	0.8527	6810.00
313.00	0.9301	7430.00
313.00	0.9378	7620.00
313.00	0.9470	7720.00
323.00	0.5686	5630.00
323.00	0.6580	6370.00
323.00	0.7437	7040.00
323.00	0.8522	8260.00
323.00	0.8977	8690.00
323.00	0.9301	8750.00
323.00	0.9378	8730.00
333.00	0.5686	6470.00
333.00	0.6580	7300.00
333.00	0.7437	8140.00
333.00	0.8522	9290.00
333.00	0.8977	9630.00
343.00	0.5686	7330.00
343.00	0.6580	8380.00
343.00	0.7437	9170.00
343.00	0.8522	10190.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0440	550.00
0.1140	1240.00
0.1880	1920.00
0.2690	2630.00
0.4440	4010.00
0.5330	4660.00
0.6440	5340.00
0.7380	6020.00
0.8300	6680.00
0.8590	6950.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
302.40	0.0116	224.00
297.40	0.0118	202.00
292.40	0.0120	183.00
287.40	0.0121	165.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (1) - Gas	Vapor or sublimation pressure, kPa - Gas
313.00	0.9727	7360.00
323.00	0.9727	8300.00
333.00	0.9301	9260.00
343.00	0.8977	10090.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
302.40	0.0116	224.00
297.40	0.0118	202.00
292.40	0.0120	183.00
287.40	0.0121	165.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (1) - Gas	Vapor or sublimation pressure, kPa - Gas
313.00	0.9727	7360.00
323.00	0.9727	8300.00
333.00	0.9301	9260.00
343.00	0.8977	10090.00

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (1) - Liquid	Molar volume, m3/mol - Liquid
0.0440	0.0001
0.1140	0.0001
0.1880	0.0001
0.2690	0.0001
0.4440	0.0001
0.5330	0.0001
0.6440	0.0001
0.7380	0.0001
0.8300	0.0001
0.8590	0.0001

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 313 (Liquid)

Mole fraction of Carbon dioxide (1) - Liquid	Molar volume, m3/mol - Liquid
0.0440	0.0001
0.1140	0.0001
0.1880	0.0001
0.2690	0.0001
0.4440	0.0001
0.5330	0.0001
0.6440	0.0001
0.7380	0.0001
0.8300	0.0001
0.8590	0.0001

Sources

• Phase behavior of the poly(vinyl pyrrolidone) + dichloromethane + supercritical carbon dioxide system
• Effect of Dissolved Poly(lactic acid) on the Solubility of CO2, N2, and He Gases in Dichloromethane
• High Pressure Phase Equilibria of the Related Substances in the Limonene Oxidation in Supercritical CO2
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Gas Solubilities (CO2, O2, Ar, N2, H2, and He) in Liquid Chlorinated Methanes