Comprehensive compilation on esterification reactions and predicting reaction kinetics and equilibrium using PC-SAFT

Knowledge of the equilibrium and kinetics of reactions is critical for optimizing industrial chemical processes. In this study, the equilibrium and kinetics of esterification reactions were systematically investigated for a series of carboxylic acids (acetic acid, propionic acid, formic acid, and levulinic acid) and alcohols (methanol, ethanol, n-propanol, and n-butanol), giving a total set of 16 esterification reactions at different temperatures. First, formation properties of reactants and products were utilized to calculate the reaction equilibrium constants Keq of these reactions. These were compared with Keq values obtained by one equilibrium experiment coupled to PC-SAFT predictions. The comparison yielded outstanding agreement between PC-SAFT-assisted Keq values and the formation-property-derived Keq values. The Keq values were then used in activity-based kinetic expressions, and the predicted reaction kinetics were validated against experimental data to demonstrate the model’s accuracy. The deviations between PC-SAFT and experimental data were AAD% (Keq) = 1.66% for the reaction equilibrium and AAD% (r) = 13.8% for the kinetic curves. The Arrhenius equation and van ’t Hoff equation were applied to depict the temperature dependence of reaction rate constants and of Keq for each esterification reaction in a range of 303.15–423.15 K. Thus, activity-based thermodynamic standard properties are provided in this work, guiding the optimization of esterification reactions in a broad range of conditions.

Publication Details

Journal
Technische Universität Dortmund Eldorado (Technische Universität Dortmund)
Published
2025-04-02
DOI
https://doi.org/10.17877/de290r-25544
Primary Topic
Process Optimization and Integration
Type
article
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article

Comprehensive compilation on esterification reactions and predicting reaction kinetics and equilibrium using PC-SAFT

Technische Universität Dortmund Eldorado (Technische Universität Dortmund)
Process Optimization and Integration
article

Comprehensive compilation on esterification reactions and predicting reaction kinetics and equilibrium using PC-SAFT

article en

Abstract

Knowledge of the equilibrium and kinetics of reactions is critical for optimizing industrial chemical processes. In this study, the equilibrium and kinetics of esterification reactions were systematically investigated for a series of carboxylic acids (acetic acid, propionic acid, formic acid, and levulinic acid) and alcohols (methanol, ethanol, n-propanol, and n-butanol), giving a total set of 16 esterification reactions at different temperatures. First, formation properties of reactants and products were utilized to calculate the reaction equilibrium constants Keq of these reactions. These were compared with Keq values obtained by one equilibrium experiment coupled to PC-SAFT predictions. The comparison yielded outstanding agreement between PC-SAFT-assisted Keq values and the formation-property-derived Keq values. The Keq values were then used in activity-based kinetic expressions, and the predicted reaction kinetics were validated against experimental data to demonstrate the model’s accuracy. The deviations between PC-SAFT and experimental data were AAD% (Keq) = 1.66% for the reaction equilibrium and AAD% (r) = 13.8% for the kinetic curves. The Arrhenius equation and van ’t Hoff equation were applied to depict the temperature dependence of reaction rate constants and of Keq for each esterification reaction in a range of 303.15–423.15 K. Thus, activity-based thermodynamic standard properties are provided in this work, guiding the optimization of esterification reactions in a broad range of conditions.

Technische Universität Dortmund Eldorado (Technische Universität Dortmund)
Openalex Percentile: Top 46%
Process Optimization and Integration
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