NIST TRC ThermoML Dataset

Isobaric (vapour + liquid) equilibria for three binary systems (toluene + anisole, n-butylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa Li, H.; Xia, S.; Ma, P.; Yan, F.; Yang, Z.; Li, Y.; Fluid Phase Equilibria 2014, 369, 109-114

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. methyl phenyl ether C7H8O (RDOXTESZEPMUJZ-UHFFFAOYSA-N) - Commercial source
2. butylbenzene C10H14 (OCKPCBLVNKHBMX-UHFFFAOYSA-N) - Commercial source

Data

P = 101.33 kPa
x (mol mol^-1)	T_bp (K)
0.9568	427.16
0.5094	436.94
0.1731	448.84
0.0817	452.1
0.0490	453.34
0.0305	454.23
0.9313	427.65
0.885	428.54
0.8264	429.74
0.7596	431.06
0.7362	431.59
0.7005	432.55
0.6698	433.45
0.6173	434.78

18634; anisole + butylbenzene; 01463:02770