Mixture of 2-Propanol, 2-methyl- + Carbon dioxide

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (4)
3. ρ_l - Mass density, kg/m3 (2)
4. Vapor or sublimation pressure, kPa (2)

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.2918	351.27	0.9588
0.3232	341.59	0.9771
0.3633	351.27	0.9573
0.3638	331.93	0.9959
0.3981	341.59	0.9751
0.4241	351.27	0.9541
0.4441	331.93	0.9839
0.4696	341.59	0.9722
0.5003	351.27	0.9524
0.5202	331.93	0.9834
0.5479	341.59	0.9671
0.5701	351.27	0.9482
0.6157	331.93	0.9814
0.6291	341.59	0.9633
0.6448	351.27	0.9439
0.7377	341.59	0.9526
0.7402	351.27	0.9356
0.7774	331.93	0.9691
0.7851	351.27	0.9182
0.7963	341.59	0.9454
0.8303	331.93	0.9654
0.8554	351.27	0.8554
0.9027	341.59	0.9027

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.2918	351.27	0.9588
0.3232	341.59	0.9771
0.3633	351.27	0.9573
0.3638	331.93	0.9959
0.3981	341.59	0.9751
0.4241	351.27	0.9541
0.4441	331.93	0.9839
0.4696	341.59	0.9722
0.5003	351.27	0.9524
0.5202	331.93	0.9834
0.5479	341.59	0.9671
0.5701	351.27	0.9482
0.6157	331.93	0.9814
0.6291	341.59	0.9633
0.6448	351.27	0.9439
0.7377	341.59	0.9526
0.7402	351.27	0.9356
0.7774	331.93	0.9691
0.7851	351.27	0.9182
0.7963	341.59	0.9454
0.8303	331.93	0.9654
0.8554	351.27	0.8554
0.9027	341.59	0.9027

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2918	351.27	5010.00
0.3232	341.59	5010.00
0.3633	351.27	6080.00
0.3638	331.93	5010.00
0.3981	341.59	6080.00
0.4241	351.27	6960.00
0.4441	331.93	6080.00
0.4696	341.59	6960.00
0.5003	351.27	8020.00
0.5202	331.93	6960.00
0.5479	341.59	8020.00
0.5701	351.27	8990.00
0.6157	331.93	7930.00
0.6291	341.59	8990.00
0.6448	351.27	9970.00
0.7377	341.59	9970.00
0.7402	351.27	11040.00
0.7774	331.93	9480.00
0.7851	351.27	11520.00
0.7963	341.59	10550.00
0.8303	331.93	9970.00
0.8554	351.27	12010.00
0.9027	341.59	11040.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.00	0.4970	7000.00
333.00	0.6070	8020.00
333.00	0.7000	9000.00
333.00	0.7950	9710.00
333.00	0.9050	10470.00
343.00	0.4970	7800.00
343.00	0.6070	8920.00
343.00	0.7000	9700.00
353.00	0.4970	8560.00
353.00	0.6070	9750.00
353.00	0.7000	10830.00
368.00	0.4970	9600.00
368.00	0.6070	10580.00
368.00	0.7000	11520.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2918	351.27	5010.00
0.3232	341.59	5010.00
0.3633	351.27	6080.00
0.3638	331.93	5010.00
0.3981	341.59	6080.00
0.4241	351.27	6960.00
0.4441	331.93	6080.00
0.4696	341.59	6960.00
0.5003	351.27	8020.00
0.5202	331.93	6960.00
0.5479	341.59	8020.00
0.5701	351.27	8990.00
0.6157	331.93	7930.00
0.6291	341.59	8990.00
0.6448	351.27	9970.00
0.7377	341.59	9970.00
0.7402	351.27	11040.00
0.7774	331.93	9480.00
0.7851	351.27	11520.00
0.7963	341.59	10550.00
0.8303	331.93	9970.00
0.8554	351.27	12010.00
0.9027	341.59	11040.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.00	0.4970	7000.00
333.00	0.6070	8020.00
333.00	0.7000	9000.00
333.00	0.7950	9710.00
333.00	0.9050	10470.00
343.00	0.4970	7800.00
343.00	0.6070	8920.00
343.00	0.7000	9700.00
353.00	0.4970	8560.00
353.00	0.6070	9750.00
353.00	0.7000	10830.00
368.00	0.4970	9600.00
368.00	0.6070	10580.00
368.00	0.7000	11520.00

Mass density, kg/m3 [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
1000.00	0.0000	765.3
1000.00	1.0000	17.9
2000.00	0.0000	766.2
2000.00	0.1000	771.1
2000.00	1.0000	37.1
3000.00	0.0000	767.2
3000.00	0.1000	772.3
3000.00	0.2000	776.5
3000.00	1.0000	58.7
4000.00	0.0000	768.0
4000.00	0.1000	773.3
4000.00	0.2000	777.8
4000.00	0.3000	781.0
4000.00	1.0000	83.5
5000.00	0.0000	768.9
5000.00	0.1000	774.4
5000.00	0.2000	779.0
5000.00	0.3000	782.5
5000.00	0.4000	786.3
5000.00	1.0000	112.7
6000.00	0.0000	769.8
6000.00	0.1000	775.5
6000.00	0.2000	780.3
6000.00	0.3000	784.0
6000.00	0.4000	788.1
6000.00	0.5000	790.9
6000.00	1.0000	148.8
7000.00	0.0000	770.6
7000.00	0.1000	776.5
7000.00	0.2000	781.5
7000.00	0.3000	785.4
7000.00	0.4000	790.0
7000.00	0.5000	793.3
7000.00	0.6000	794.3
7000.00	1.0000	197.3
8000.00	0.0000	771.4
8000.00	0.1000	777.5
8000.00	0.2000	782.4
8000.00	0.3000	786.8
8000.00	0.4000	791.7
8000.00	0.5000	795.6
8000.00	0.6000	797.5
8000.00	0.7000	796.8
8000.00	0.8000	783.7
8000.00	1.0000	276.7
9000.00	0.0000	772.3
9000.00	0.1000	778.5
9000.00	0.2000	783.9
9000.00	0.3000	788.2
9000.00	0.4000	793.4
9000.00	0.5000	797.8
9000.00	0.6000	800.6
9000.00	0.7000	801.4
9000.00	0.8000	791.5
9000.00	0.9000	753.3
9000.00	0.9500	703.6
9000.00	1.0000	483.4
10000.00	0.0000	773.1
10000.00	0.1000	779.5
10000.00	0.2000	785.0
10000.00	0.3000	789.6
10000.00	0.4000	795.2
10000.00	0.5000	800.0
10000.00	0.6000	803.5
10000.00	0.7000	805.7
10000.00	0.8000	798.6
10000.00	0.9000	768.1
10000.00	0.9500	731.7
10000.00	1.0000	627.4

Mass density, kg/m3 [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
1000.00	0.0000	765.3
1000.00	1.0000	17.9
2000.00	0.0000	766.2
2000.00	0.1000	771.1
2000.00	1.0000	37.1
3000.00	0.0000	767.2
3000.00	0.1000	772.3
3000.00	0.2000	776.5
3000.00	1.0000	58.7
4000.00	0.0000	768.0
4000.00	0.1000	773.3
4000.00	0.2000	777.8
4000.00	0.3000	781.0
4000.00	1.0000	83.5
5000.00	0.0000	768.9
5000.00	0.1000	774.4
5000.00	0.2000	779.0
5000.00	0.3000	782.5
5000.00	0.4000	786.3
5000.00	1.0000	112.7
6000.00	0.0000	769.8
6000.00	0.1000	775.5
6000.00	0.2000	780.3
6000.00	0.3000	784.0
6000.00	0.4000	788.1
6000.00	0.5000	790.9
6000.00	1.0000	148.8
7000.00	0.0000	770.6
7000.00	0.1000	776.5
7000.00	0.2000	781.5
7000.00	0.3000	785.4
7000.00	0.4000	790.0
7000.00	0.5000	793.3
7000.00	0.6000	794.3
7000.00	1.0000	197.3
8000.00	0.0000	771.4
8000.00	0.1000	777.5
8000.00	0.2000	782.4
8000.00	0.3000	786.8
8000.00	0.4000	791.7
8000.00	0.5000	795.6
8000.00	0.6000	797.5
8000.00	0.7000	796.8
8000.00	0.8000	783.7
8000.00	1.0000	276.7
9000.00	0.0000	772.3
9000.00	0.1000	778.5
9000.00	0.2000	783.9
9000.00	0.3000	788.2
9000.00	0.4000	793.4
9000.00	0.5000	797.8
9000.00	0.6000	800.6
9000.00	0.7000	801.4
9000.00	0.8000	791.5
9000.00	0.9000	753.3
9000.00	0.9500	703.6
9000.00	1.0000	483.4
10000.00	0.0000	773.1
10000.00	0.1000	779.5
10000.00	0.2000	785.0
10000.00	0.3000	789.6
10000.00	0.4000	795.2
10000.00	0.5000	800.0
10000.00	0.6000	803.5
10000.00	0.7000	805.7
10000.00	0.8000	798.6
10000.00	0.9000	768.1
10000.00	0.9500	731.7
10000.00	1.0000	627.4

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (2) - Gas	Vapor or sublimation pressure, kPa - Gas
343.00	0.7950	10350.00
343.00	0.9050	11070.00
353.00	0.7950	11560.00
353.00	0.9050	11630.00
368.00	0.7950	12030.00
368.00	0.9050	11780.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Carbon dioxide (2) - Gas	Vapor or sublimation pressure, kPa - Gas
343.00	0.7950	10350.00
343.00	0.9050	11070.00
353.00	0.7950	11560.00
353.00	0.9050	11630.00
368.00	0.7950	12030.00
368.00	0.9050	11780.00

Sources

• Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
• High-Pressure Vapor-Liquid Equilibria for CO2 + 2-Butanol, CO2 + iso-Butanol and CO2 + tert-Butanol Systems
• Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}