Mixture of Ethane, nitro- + 2-Propanol, 1-methoxy-

Datasets

1. P_vap - Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.15	0.0000	6.10
313.15	0.0254	6.19
313.15	0.0498	6.24
313.15	0.1005	6.31
313.15	0.1510	6.33
313.15	0.2020	6.34
313.15	0.3031	6.27
313.15	0.3995	6.15
313.15	0.4478	6.07
313.15	0.4984	5.96
313.15	0.5038	5.94
313.15	0.5660	5.79
313.15	0.6011	5.71
313.15	0.7016	5.36
313.15	0.8002	4.92
313.15	0.9013	4.34
313.15	0.9503	4.00
313.15	1.0000	3.61
353.15	0.0000	33.11
353.15	0.0503	33.86
353.15	0.1012	34.31
353.15	0.1526	34.61
353.15	0.2040	34.75
353.15	0.2583	34.79
353.15	0.3113	34.59
353.15	0.4047	34.22
353.15	0.4386	33.97
353.15	0.4910	33.60
353.15	0.5255	33.30
353.15	0.5815	32.72
353.15	0.5956	32.61
353.15	0.7041	31.08
353.15	0.8009	29.35
353.15	0.9019	27.07
353.15	0.9502	25.75
353.15	1.0000	24.18

Sources

• Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid

Note: These property values are available through the Cheméo API. A free account gives you an access key.