Mixture of n-Hexane + Ethanol, 2-propoxy-

Datasets

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

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-propoxy- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.0990	24.94
303.15	0.1410	24.90
303.15	0.1990	24.32
303.15	0.3240	23.51
303.15	0.3980	22.87
303.15	0.5110	22.01
303.15	0.5690	21.27
303.15	0.6840	19.60
303.15	0.8240	14.89
303.15	0.8870	11.00
313.15	0.0990	36.04
313.15	0.1410	35.95
313.15	0.1990	35.53
313.15	0.3240	34.30
313.15	0.3980	33.65
313.15	0.5110	31.80
313.15	0.5690	30.55
313.15	0.6840	28.30
313.15	0.8240	21.90
313.15	0.8870	16.28
323.15	0.0990	51.62
323.15	0.1410	50.88
323.15	0.1990	49.96
323.15	0.3240	48.99
323.15	0.3980	47.12
323.15	0.5110	44.54
323.15	0.5690	43.56
323.15	0.6840	39.95
323.15	0.8240	30.52
323.15	0.8870	22.61

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-propoxy- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	0.0990	24.94
303.15	0.1410	24.90
303.15	0.1990	24.32
303.15	0.3240	23.51
303.15	0.3980	22.87
303.15	0.5110	22.01
303.15	0.5690	21.27
303.15	0.6840	19.60
303.15	0.8240	14.89
303.15	0.8870	11.00
313.15	0.0990	36.04
313.15	0.1410	35.95
313.15	0.1990	35.53
313.15	0.3240	34.30
313.15	0.3980	33.65
313.15	0.5110	31.80
313.15	0.5690	30.55
313.15	0.6840	28.30
313.15	0.8240	21.90
313.15	0.8870	16.28
323.15	0.0990	51.62
323.15	0.1410	50.88
323.15	0.1990	49.96
323.15	0.3240	48.99
323.15	0.3980	47.12
323.15	0.5110	44.54
323.15	0.5690	43.56
323.15	0.6840	39.95
323.15	0.8240	30.52
323.15	0.8870	22.61

Sources

• Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems