NIST TRC ThermoML Dataset

Isobaric vapor-liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa Lladosa, E.; Montón, J.; Burguet, M.; Muñoz, R.; Fluid Phase Equilibria 2006, 247, 47-53

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Liquid
Substances:
1. 1-butanol C4H10O (LRHPLDYGYMQRHN-UHFFFAOYSA-N) - Commercial source
2. 5-oxanonane C8H18O (DURPTKYDGMDSBL-UHFFFAOYSA-N) - Commercial source

Data

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24981; butan-1-ol + dibutyl ether; 00081:00126