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. benzene C6H6 (UHOVQNZJYSORNB-UHFFFAOYSA-N) - Commercial source
2. 1,2-dimethylbenzene C8H10 (CTQNGGLPUBDAKN-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
1	353.3
0.428	375.2
0.318	383.6
0.305	384.7
0.273	387.5
0.216	393.2
0.139	401.4
0.093	406.7
0.057	410.8
0.030	413.9
0	417.5
0.980	353.8
0.948	354.6
0.909	355.7
0.887	356.3
0.826	357.9
0.768	359.8
0.657	363.9
0.543	368.7

32708; benzene + 1,2-dimethylbenzene; 00006:00029