Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Measurement and correlation of the solubility of maleic anhydride in different organic solvents

Liu, X.[Xiang], Hu, Y.[Yonghong], Liang, M.[Mengmeng], Li, Y.[Yonglan], Yin, J.[Jingjing], Yang, W.[Wenge]
Fluid Phase Equilib. 2014, 367, 1-6
ABSTRACT
Data on corresponding solid liquid equilibrium of maleic anhydride in different organic solvents are essential for industrial design and further theoretical studies. In this study, the solubilities of maleic anhydride were measured in DMF, methanol, acetic acid, acetonitrile, acetone, ethyl acetate, 2-propanol and n-butyl alcohol with the temperature range of 278.15 323.15 K by the analytical stirred-flask method under atmospheric pressure. The experiment results indicated that the solubility of maleic anhydride was highest in DMF and followed by methanol, acetic acid, acetonitrile, acetone, ethyl acetate, 2-propanol and n-butyl alcohol. For the temperature range investigated, the solubilities of maleic anhydride in the organic solvents increased with increasing temperature. Results of these measurements were well-correlated with the modified Apelblat equation, the Buchowski Ksiazaczak lambda h equation and the van't Hoff equation.The calculated solubilities showed good agreement with the experimental data. The modified Apelblat equation was found to regress the solubility data is higher accuracy than the Buchowski Ksiazaczak lambda h equation. The experimental data and model parameters would be useful for optimizing the process of purification of maleic anhydride in industry.
Compounds
# Formula Name
1 C3H7NO dimethylformamide
2 CH4O methanol
3 C2H4O2 acetic acid
4 C2H3N acetonitrile
5 C3H6O acetone
6 C4H8O2 ethyl acetate
7 C3H8O propan-2-ol
8 C4H10O butan-1-ol
9 C4H2O3 maleic anhydride
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
  • 9
  • Normal melting temperature, K ; Crystal
  • Crystal
  • Liquid
  • Air at 1 atmosphere
  • DTA
  • 1
  • POMD
  • 1
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 2
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 3
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 4
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 5
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 9
  • 6
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 7
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10
  • POMD
  • 8
  • 9
  • Mole fraction - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 9
  • gravimetric
  • 10