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. toluene C7H8 (YXFVVABEGXRONW-UHFFFAOYSA-N) - Commercial source

Data

P = 101.33 kPa
x (mol mol^-1)	T_bp (K)
0.9532	384.55
0.3363	404.33
0.0858	418.85
0.0500	423.06
0.0051	426.17
0.9007	385.87
0.8431	387.34
0.8040	388.02
0.7431	389.84
0.6764	392.37
0.6591	392.73
0.6357	393.65
0.5781	395.67

18632; anisole + toluene; 00023:01463