Thermodynamics of enzyme-catalyzed esterifications: I. Succinic acid esterification with ethanol
- 12 May 2017
- journal article
- biotechnological products-and-process-engineering
- Published by Springer Nature in Applied Microbiology and Biotechnology
- Vol. 101 (15) , 5973-5984
Abstract
Succinic acid (SA) was esterified with ethanol using Candida antarctica lipase B immobilized on acrylic resin at 40 and 50 °C. Enzyme activity in the reaction medium was assured prior to reaction experiments. Reaction-equilibrium experiments were performed for varying initial molalities of SA and water in the reaction mixtures. This allowed calculating the molality-based apparent equilibrium constant K m as function of concentration and temperature. K m was shown to depend strongly on the molality of water and SA as well as on temperature. It could be concluded that increasing the molality of SA shifted the reaction equilibrium towards the products. Water had a strong effect on the activity of the enzyme and on K m . The concentration dependence of K m values was explained by the activity coefficients of the reacting agents. These were predicted with the thermodynamic models Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT), NRTL, and Universal Quasichemical Functional Group Activity Coefficients (UNIFAC), yielding the ratio of activity coefficients of products and reactants K γ . All model parameters were taken from literature. The models yielded K γ values between 25 and 115. Thus, activity coefficients have a huge impact on the consistent determination of the thermodynamic equilibrium constants K th. Combining K m and PC-SAFT-predicted K γ allowed determining K th and the standard Gibbs energy of reaction as function of temperature. This value was shown to be in very good agreement with results obtained from group contribution methods for Gibbs energy of formation. In contrast, inconsistencies were observed for K th using K γ values from the classical gE-models UNIFAC and NRTL. The importance of activity coefficients opens the door for an optimized reaction setup for enzymatic esterifications.Keywords
Funding Information
- Deutsche Forschungsgemeinschaft (Leibniz award to G. Sadowski, the Cluster of Excellence RESOLV (EXC 1069))
This publication has 60 references indexed in Scilit:
- Direct downstream catalysis: From succinate to its diethyl ester without intermediate acidificationChemical Engineering Journal, 2012
- Method of contribution of groups to estimate thermodynamic properties of components of biodiesel formation in liquid phaseFluid Phase Equilibria, 2012
- Mixed Succinic Acid/Acetic Acid Esterification with Ethanol by Reactive Distillation.Industrial & Engineering Chemistry Research, 2011
- The irruption of polymers from renewable resources on the scene of macromolecular science and technologyGreen Chemistry, 2011
- Modeling and optimization of lipase-catalyzed production of succinic acid ester using central composite design analysisJournal of Industrial Microbiology and Biotechnology, 2010
- Recovery of succinic acid from fermentation brothBiotechnology Letters, 2009
- Modeling aqueous electrolyte solutions. Part 2. Weak electrolytesFluid Phase Equilibria, 2009
- Esterification of dicarboxylic acids to diesters over Mn+-montmorillonite clay catalystsCatalysis Letters, 2005
- Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain MoleculesIndustrial & Engineering Chemistry Research, 2001
- Local compositions in thermodynamic excess functions for liquid mixturesAIChE Journal, 1968