NIST TRC ThermoML Dataset

Isobaric vapor-liquid equilibrium for binary systems of toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa Gupta, B.S.; Lee, M.J.; Fluid Phase Equilibria 2013, 352, 86-92

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. 1,2-dimethylbenzene C8H10 (CTQNGGLPUBDAKN-UHFFFAOYSA-N) - Commercial source
2. toluene C7H8 (YXFVVABEGXRONW-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
1	383.4
0.426	399.0
0.367	401.3
0.291	404.4
0.230	407.0
0.132	411.4
0.094	413.2
0.069	414.3
0	417.5
0.937	385.0
0.920	385.4
0.880	386.3
0.796	388.1
0.693	390.5
0.662	391.4
0.579	393.9
0.500	396.3

1827; benzene + toluene; 00006:00023