Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K

Hu, Y.[Yonghong], Kai, Y.[Yumei], Cao, Z.[Zheng], Li, J.[Jiaojiao], Yangb, W.[Wenge]
Fluid Phase Equilib. 2013, 354, 259-264
ABSTRACT
The solubilities of dimethyl succinylsuccinate in tetrahydrofuran, acetic ether, acetone, acetonitrile, 1-propanol, ethanol and methanol pure solvents and tetrahydrofuran + methanol mixed solvents weremeasured within the temperature range 278.15 K to 333.15 K at atmospheric pressure. The solubilityof dimethyl succinylsuccinate in those selected solvents increased with increasing temperature, and thedissolution in tetrahydrofuran is best. The semi-empirical Buchowski Ksiazczak h equation, the modi-fied Apelblat equation and CNIBS/R-K equation were used to correlate with the solubility. In pure solventsthe values of the sum of deviation ( SUM(%Dev)) for Apelblat and Buchowski Ksiazczak h equations are1.1115 and 1.0383, respectively. In the tetrahydrofuran and methanol mixture, the sums of deviation( SUM(%Dev)) for Apelblat equation, Buchowski Ksiazczak h equation and CNIBS/R-K equation are 0.7587,0.7059 and 1.4090, respectively. By comparing models, the solubilities predicted by Buchowski Ksiazczak h equation and Apelblat equation is reasonable in mixture solvent and pure solvent, respectively. Thethermodynamic properties of the solution process, including the enthalpy, and entropy were calculatedby the van t Hoff analysis. The value of enthalpy and entropy were positive.
Compounds
# Formula Name
1 C10H12O6 dimethyl 2,5-dioxocyclohexane-1,4-dicarboxylate
2 CH4O methanol
3 C2H6O ethanol
4 C3H8O propan-1-ol
5 C4H8O2 ethyl acetate
6 C2H3N acetonitrile
7 C4H8O tetrahydrofuran
8 C3H6O acetone
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
  • 2
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 3
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 4
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 5
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 6
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 7
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 12
  • POMD
  • 8
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • Gravimetric with drying of solvent
  • 10
  • POMD
  • 2
  • 7
  • 1
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 1
  • gravimetric with drying of solvent
  • 72