Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Vapor-liquid equilibrium of mixtures containing formaldehyde, water, and butynediol

Berje, Juergen, Baldamus, Jens, Burger, Jakob, Hasse, Hans
Fluid Phase Equilib. 2019, 490, 101-106
ABSTRACT
Measurements of the vapor-liquid equilibrium in the system formaldehyde + water + butynediol were performed at 393 K and 413 K for overall formaldehyde mass fractions between 0.1gg-1 and 0.2gg-1 and overall butynediol mass fractions between 0.05gg-1 and 0.35gg-1. The studied system is a complex reactive multicomponent mixture as formaldehyde reacts both with formaldehyde and butynediol. A predictive physico-chemical model of the vapor-liquid equilibrium from the literature [1] is validated by the experiments of the present work. Residue curves are calculated to illustrate the distillation behavior of the studied system.
Compounds
# Formula Name
1 CH2O methanal
2 H2O water
3 C4H6O2 2-butyn-1,4-diol
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • 2
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Mass fraction - 3; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 23
  • POMD
  • 1
  • 2
  • 3
  • Mass fraction - 1 ; Liquid
  • Mass fraction - 3 ; Gas
  • Mass fraction - 1 ; Gas
  • Temperature, K; Liquid
  • Mass fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Chromatography
  • Chromatography
  • Chromatography
  • 23