NIST TRC ThermoML Dataset

Isobaric vapor-liquid equilibria for binary mixtures from methyl methanoate, dimethoxymethane and dimethyl carbonate at 101.33 kPa Lee, S.; Cho, J.; Kim, Y.C.; Fluid Phase Equilibria 2015, 397, 95-102

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. methyl methanoate C2H4O2 (TZIHFWKZFHZASV-UHFFFAOYSA-N) - Commercial source
2. dimethyl carbonate C3H6O3 (IEJIGPNLZYLLBP-UHFFFAOYSA-N) - Commercial source

Data

P = 101.33 kPa
x (mol mol^-1)	T_bp (K)
1	304.68
0.334	330.05
0.249	335.35
0.197	339.35
0.139	344.6
0.090	350.05
0.026	358.98
0	363.15
0.932	306.68
0.885	307.69
0.796	309.95
0.711	312.46
0.671	314.05
0.598	317.05
0.464	322.88
0.404	325.75

34520; methyl methanoate + dimethyl carbonate; 00349:00829