Mixture of Toluene + Pentane, 2,3-dimethyl-
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Pentane, 2,3-dimethyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Gas |
0.1958 |
323.20 |
0.3459 |
0.3756 |
323.20 |
0.5687 |
0.6022 |
323.20 |
0.7688 |
0.7978 |
323.20 |
0.8911 |
0.1936 |
343.20 |
0.3315 |
0.3876 |
343.20 |
0.5546 |
0.6039 |
343.20 |
0.7533 |
0.8117 |
343.20 |
0.9001 |
0.1899 |
363.20 |
0.3071 |
0.3847 |
363.20 |
0.5403 |
0.5951 |
363.20 |
0.7351 |
0.7834 |
363.20 |
0.8754 |
Mole fraction of Pentane, 2,3-dimethyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Liquid |
Temperature, K - Gas |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Gas |
0.1958 |
323.20 |
0.3459 |
0.3756 |
323.20 |
0.5687 |
0.6022 |
323.20 |
0.7688 |
0.7978 |
323.20 |
0.8911 |
0.1936 |
343.20 |
0.3315 |
0.3876 |
343.20 |
0.5546 |
0.6039 |
343.20 |
0.7533 |
0.8117 |
343.20 |
0.9001 |
0.1899 |
363.20 |
0.3071 |
0.3847 |
363.20 |
0.5403 |
0.5951 |
363.20 |
0.7351 |
0.7834 |
363.20 |
0.8754 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1958 |
323.20 |
14.80 |
0.3756 |
323.20 |
17.70 |
0.6022 |
323.20 |
20.50 |
0.7978 |
323.20 |
23.10 |
0.1936 |
343.20 |
32.00 |
0.3876 |
343.20 |
36.90 |
0.6039 |
343.20 |
42.80 |
0.8117 |
343.20 |
49.10 |
0.1899 |
363.20 |
62.00 |
0.3847 |
363.20 |
71.70 |
0.5951 |
363.20 |
81.20 |
0.7834 |
363.20 |
90.50 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Pentane, 2,3-dimethyl- (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1958 |
323.20 |
14.80 |
0.3756 |
323.20 |
17.70 |
0.6022 |
323.20 |
20.50 |
0.7978 |
323.20 |
23.10 |
0.1936 |
343.20 |
32.00 |
0.3876 |
343.20 |
36.90 |
0.6039 |
343.20 |
42.80 |
0.8117 |
343.20 |
49.10 |
0.1899 |
363.20 |
62.00 |
0.3847 |
363.20 |
71.70 |
0.5951 |
363.20 |
81.20 |
0.7834 |
363.20 |
90.50 |
Sources