Abstract
The solubilities of two Schiff-base ligands H2L1 and H2L2 (L1=N,N′-bis(3,5-di-tert-butylsalicylidene)-1,2-diphenylethane-1,2-diamine;L2=N,N′-bis(3,5-di-tert-butylsalicylidene)propane-1,2-diamine) and their corresponding oxovanadium(IV) complexes (VOL1 and VOL2) were systematically determined in selected organic solvents using the static equilibrium method over the temperature range of 278.15 - 313.15 K. Solid-liquid equilibrium data were correlated using several empirical equations (Apelblat, van't Hoff, Yaws, polynomial, and λh) as well as activity-coefficient models (Wilson, NRTL, and UNIQUAC). All systems exhibited a monotonic increase in solubility with temperature, indicating endothermic dissolution behavior. Among the investigated models, UNIQUAC provided the most accurate correlation for H2L1, NRTL showed superior performance for H2L2, while the polynomial empirical model yielded the best overall fit for both vanadium complexes. Thermodynamic analysis revealed that the dissolution processes are predominantly enthalpy-driven. Furthermore, Hansen solubility parameters were employed to rationalize solvent-solute interactions and explain solvent-dependent solubility trends. The experimental data and thermodynamic modeling presented in this work provide a reliable basis for solvent screening, solubility prediction, and process-relevant applications of Schiff base vanadium complexes in homogeneous systems. The present data thus provide quantitative guidance for solvent selection and operating condition design in homogeneous catalytic processes and other solution-phase applications.
| Original language | English |
|---|---|
| Article number | 100322 |
| Journal | Chemical Thermodynamics and Thermal Analysis |
| Volume | 22 |
| DOIs | |
| Publication status | Published - Jun 2026 |
| Externally published | Yes |
Keywords
- Activity coefficient models
- Hansen solubility parameters
- Schiff base vanadium complexes
- Solid-liquid equilibrium
- Solvent screening
- Thermodynamic modeling
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