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Solubility modeling, mixing properties and solvent effect of 5-norbornene-2,3-dicarboximide in eleven pure solvents at various temperatures

Mole-fraction solubility of 5-norbornene-2,3-dicarboximide (NODI) in eleven solvents including methanol (MtOH), ethanol (EtOH), 2-ethoxyethanol, methyl acetate (MAC), ethyl acetate (EAC), n-propyl acetate (NPAC), isopropyl acetate (IPAC), n-butyl acetate (NBAC), acetone (DMK), N,N-dimethylformamide...

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Published in:Fluid phase equilibria 2020-05, Vol.512, p.112301, Article 112301
Main Authors: Wan, Yameng, He, Haixia, Zhang, Pengshuai, Zhao, Rui, Sha, Jiao, Li, Tao, Ren, Baozeng
Format: Article
Language:English
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Summary:Mole-fraction solubility of 5-norbornene-2,3-dicarboximide (NODI) in eleven solvents including methanol (MtOH), ethanol (EtOH), 2-ethoxyethanol, methyl acetate (MAC), ethyl acetate (EAC), n-propyl acetate (NPAC), isopropyl acetate (IPAC), n-butyl acetate (NBAC), acetone (DMK), N,N-dimethylformamide (DMF) at (278.15–323.15) K and 1,4-dioxane at (288.15–323.15) K was experimentally measured by laser monitoring technique under 0.1 MPa. Solubility of NODI increased with the increasing temperature. Hansen Solubility Parameter was employed to explain the solubility behavior. The Kamlet-Taft parameters were calculated to investigate the solvent effect based on linear solvation energy relationships concept. Thermodynamic modeling including the Two-Suffix Margules model, Wilson model, NRTL model, NRTL-SAC model and UNIQUAC model were employed to correlate the experimental solubility. Wilson model and NRTL-SAC model were more suitable in correlation with solubility data. Furthermore, thermodynamic properties of mixing process (ΔmixG, ΔmixH, ΔmixS, lnγ1∞, H1E,∞, ζTS and ζH) were discussed based on Wilson equation. •Solubility of NODI in eleven solvents was determined.•Hansen Solubility Parameter was employed to explain the solubility behavior.•KAT-LSER model was applied to analyze the solvent effect.•Solubility was correlated by Margules, Wilson, NRTL, NRTL-SAC and UNIQUAC model.•Thermodynamic properties of mixing process were also discussed.
ISSN:0378-3812
1879-0224
DOI:10.1016/j.fluid.2019.112301