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. diisopropyl ether C6H14O (ZAFNJMIOTHYJRJ-UHFFFAOYSA-N) - Commercial source
2. 2,2,4-trimethylpentane C8H18 (NHTMVDHEPJAVLT-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
0.084	368.15
0.534	352.21
0.585	350.82
0.637	349.49
0.690	348.18
0.744	346.88
0.790	345.82
0.849	344.59
0.898	343.57
0.950	342.57
0.125	366.3
0.179	363.99
0.228	362.04
0.273	360.37
0.325	358.57
0.384	356.67
0.427	355.32
0.476	353.86

4448; isopropyl ether + 2,2,4-trimethylpentane; 00026:00250