Mixture of Formic acid, butyl ester + Ethanol, 2-ethoxy-

Datasets

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

Mole fraction of Ethanol, 2-ethoxy- (2) [ref]

Fixed		Measured
Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol, 2-ethoxy- (2) - Gas
0.0000	333.15	0.0000
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0680	333.15	0.0312
0.0684	343.15	0.0328
0.1296	343.15	0.0560
0.1365	333.15	0.0547
0.1407	353.15	0.0726
0.1900	343.15	0.0753
0.2000	333.15	0.0713
0.2033	353.15	0.0842
0.2529	343.15	0.0984
0.2673	353.15	0.1064
0.3137	333.15	0.1070
0.3571	353.15	0.1369
0.3746	333.15	0.1259
0.4096	343.15	0.1440
0.4416	353.15	0.1646
0.4645	343.15	0.1615
0.4684	333.15	0.1536
0.5233	353.15	0.1896
0.5380	343.15	0.1923
0.5776	353.15	0.2165
0.6181	343.15	0.2178
0.6507	353.15	0.2485
0.6652	333.15	0.2332
0.6991	343.15	0.2723
0.7320	333.15	0.2746
0.7520	353.15	0.3259
0.7735	343.15	0.3323
0.7840	333.15	0.3222
0.8042	353.15	0.3740
0.8249	333.15	0.3791
0.8379	343.15	0.4171
0.8649	353.15	0.4752
0.8791	333.15	0.4708
0.8990	343.15	0.5360
0.9047	353.15	0.5741
0.9174	333.15	0.5715
0.9421	343.15	0.6782
0.9468	353.15	0.7023
0.9553	333.15	0.7145
0.9742	353.15	0.8401
0.9752	343.15	0.8324
0.9765	333.15	0.8050
1.0000	333.15	1.0000
1.0000	343.15	1.0000
1.0000	353.15	1.0000

Mole fraction of Ethanol, 2-ethoxy- (2) [ref]

Fixed		Measured
Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol, 2-ethoxy- (2) - Gas
0.0000	333.15	0.0000
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0680	333.15	0.0312
0.0684	343.15	0.0328
0.1296	343.15	0.0560
0.1365	333.15	0.0547
0.1407	353.15	0.0726
0.1900	343.15	0.0753
0.2000	333.15	0.0713
0.2033	353.15	0.0842
0.2529	343.15	0.0984
0.2673	353.15	0.1064
0.3137	333.15	0.1070
0.3571	353.15	0.1369
0.3746	333.15	0.1259
0.4096	343.15	0.1440
0.4416	353.15	0.1646
0.4645	343.15	0.1615
0.4684	333.15	0.1536
0.5233	353.15	0.1896
0.5380	343.15	0.1923
0.5776	353.15	0.2165
0.6181	343.15	0.2178
0.6507	353.15	0.2485
0.6652	333.15	0.2332
0.6991	343.15	0.2723
0.7320	333.15	0.2746
0.7520	353.15	0.3259
0.7735	343.15	0.3323
0.7840	333.15	0.3222
0.8042	353.15	0.3740
0.8249	333.15	0.3791
0.8379	343.15	0.4171
0.8649	353.15	0.4752
0.8791	333.15	0.4708
0.8990	343.15	0.5360
0.9047	353.15	0.5741
0.9174	333.15	0.5715
0.9421	343.15	0.6782
0.9468	353.15	0.7023
0.9553	333.15	0.7145
0.9742	353.15	0.8401
0.9752	343.15	0.8324
0.9765	333.15	0.8050
1.0000	333.15	1.0000
1.0000	343.15	1.0000
1.0000	353.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	19.50
0.0000	343.15	29.10
0.0000	353.15	42.24
0.0680	333.15	18.99
0.0684	343.15	28.39
0.1296	343.15	27.63
0.1365	333.15	18.50
0.1407	353.15	41.12
0.1900	343.15	26.75
0.2000	333.15	17.86
0.2033	353.15	39.99
0.2529	343.15	25.93
0.2673	353.15	38.80
0.3137	333.15	17.05
0.3571	353.15	36.88
0.3746	333.15	16.43
0.4096	343.15	24.24
0.4416	353.15	34.98
0.4645	343.15	23.41
0.4684	333.15	15.47
0.5233	353.15	32.91
0.5380	343.15	22.14
0.5776	353.15	31.40
0.6181	343.15	20.57
0.6507	353.15	29.19
0.6652	333.15	12.96
0.6991	343.15	18.70
0.7320	333.15	11.89
0.7520	353.15	25.81
0.7735	343.15	16.76
0.7840	333.15	10.91
0.8042	353.15	23.75
0.8249	333.15	10.07
0.8379	343.15	14.90
0.8649	353.15	21.09
0.8791	333.15	8.84
0.8990	343.15	12.91
0.9047	353.15	19.11
0.9174	333.15	7.87
0.9421	343.15	11.20
0.9468	353.15	16.95
0.9553	333.15	6.77
0.9742	353.15	15.29
0.9752	343.15	9.79
0.9765	333.15	6.14
1.0000	333.15	5.30
1.0000	343.15	8.65
1.0000	353.15	13.62

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	19.50
0.0000	343.15	29.10
0.0000	353.15	42.24
0.0680	333.15	18.99
0.0684	343.15	28.39
0.1296	343.15	27.63
0.1365	333.15	18.50
0.1407	353.15	41.12
0.1900	343.15	26.75
0.2000	333.15	17.86
0.2033	353.15	39.99
0.2529	343.15	25.93
0.2673	353.15	38.80
0.3137	333.15	17.05
0.3571	353.15	36.88
0.3746	333.15	16.43
0.4096	343.15	24.24
0.4416	353.15	34.98
0.4645	343.15	23.41
0.4684	333.15	15.47
0.5233	353.15	32.91
0.5380	343.15	22.14
0.5776	353.15	31.40
0.6181	343.15	20.57
0.6507	353.15	29.19
0.6652	333.15	12.96
0.6991	343.15	18.70
0.7320	333.15	11.89
0.7520	353.15	25.81
0.7735	343.15	16.76
0.7840	333.15	10.91
0.8042	353.15	23.75
0.8249	333.15	10.07
0.8379	343.15	14.90
0.8649	353.15	21.09
0.8791	333.15	8.84
0.8990	343.15	12.91
0.9047	353.15	19.11
0.9174	333.15	7.87
0.9421	343.15	11.20
0.9468	353.15	16.95
0.9553	333.15	6.77
0.9742	353.15	15.29
0.9752	343.15	9.79
0.9765	333.15	6.14
1.0000	333.15	5.30
1.0000	343.15	8.65
1.0000	353.15	13.62

Sources

• Vapor-Liquid Equilibrium for Phenol + r-Methyl Benzyl Alcohol and 2-Ethoxyethanol + n-Butyl Formate