NIST TRC ThermoML Dataset

Vapor-liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa Ku, H.C.; Tu, C.H.; Fluid Phase Equilibria 2006, 248, 197-205

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. ethanol C2H6O (LFQSCWFLJHTTHZ-UHFFFAOYSA-N) - Commercial source
2. diisopropyl ether C6H14O (ZAFNJMIOTHYJRJ-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
0.044	348.29
0.489	337.97
0.537	337.67
0.598	337.47
0.649	337.35
0.705	337.31
0.757	337.37
0.809	337.58
0.859	337.97
0.907	338.73
0.954	339.92
0.089	345.76
0.143	343.73
0.193	342.15
0.240	341.0
0.287	340.08
0.338	339.34
0.389	338.8
0.440	338.34

18425; ethanol + diisopropyl ether; 00071:00250