NIST TRC ThermoML Dataset

Isobaric vapor-liquid equilibrium at 101.3 kPa and excess properties at 298.15 K for binary mixtures of methyl phenyl carbonate with methanol or dimethyl carbonate Hwang, I.C.; Shin, S.H.; Jeong, I.Y.; Jeon, Y.H.; Park, S.J.; Fluid Phase Equilibria 2013, 360, 260-264

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. dimethyl carbonate C3H6O3 (IEJIGPNLZYLLBP-UHFFFAOYSA-N) - Commercial source
2. methyl phenyl carbonate C8H8O3 (XTBFPVLHGVYOQH-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
0	363.25
0.8515	421.48
0.8825	430.55
0.9079	437.5
0.9212	443.09
0.9325	449.36
0.9451	455.87
0.9591	462.06
0.9688	467.02
0.9775	471.54
0.9858	475.8
0.1596	366.04
0.9905	480.55
0.9963	484.12
1	487.48
0.3091	370.38
0.3756	373.86
0.5229	380.92
0.6097	388.27
0.6821	394.42
0.7539	404.66
0.8054	412.45

32928; dimethyl carbonate + methyl phenyl carbonate; 00349:04470