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. n-nonane C9H20 (BKIMMITUMNQMOS-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
0	353.3
0.574	374.2
0.586	374.9
0.694	383.6
0.773	391.4
0.783	392.5
0.869	402.9
0.925	411.1
1	423.8
0.048	354.3
0.061	354.8
0.089	355.2
0.130	356.2
0.182	357.2
0.231	358.2
0.359	363.4
0.455	367.3

20102; benzene + nonane; 00029:00176