NIST TRC ThermoML Dataset

High-pressure phase equilibrium for ethylene + 1-butanol at 283.65 K and 290.80 K Kodama, D.; Seki, T.; Kato, M.; Fluid Phase Equilibria 2007, 261, 99-103

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Vapor pressure
Methodology: EBULLIO:UFactor:8
Phase(s): Liquid
Substances:
1. 1-butanol C4H10O (LRHPLDYGYMQRHN-UHFFFAOYSA-N) - Commercial source
2. ethene C2H4 (VGGSQFUCUMXWEO-UHFFFAOYSA-N) - Commercial source

Data

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30687; butan-1-ol + ethene; 00081:02611