Experimental and Theoretical Analysis of Phase Equilibria in a Two-phase System Used for Biocatalytic Esterifications

The partitioning behavior of the reactants 1-butanol, propionic acid and butyl propionate in an aqueous-organic two-phase system consisting of alginate beads suspended in hexane was investigated. Partitioning experiments with a single reactant showed that, even in the dilute region, the equilibrium concentrations of 1-butanol and propionic acid cannot be described by constant partition coefficients as is normally done in the field of biocatalysis. Besides the aqueous alginate beads, two other aqueous phases with different compositions (solutions with and without electrolytes) were also used for partitioning experiments. The equilibrium concentrations of the reactants obtained from the systems with the three different aqueous phases (water, water plus electrolytes, alginate beads) demonstrated that the partitioning behavior of the reactants is scarcely influenced by the presence of the electrolytes or by the alginate matrix, at least up to reactant concentrations of 80 mmol/l in the organic phase. The comparison of the experimental equilibrium concentrations with predicted values obtained from simulations with the modified UNIFAC (Dortmund) model showed a generally good agreement. However, in the dilute region, differences of up to 100% occurred between experimental and predicted values. Thus, for the later detailed mathematical modeling of processes occurring inside the alginate beads (such as mass transfer and enzymatic reaction), the modified UNIFAC (Dortmund) model is not adequate. Therefore, empirical correlations were derived for the mathematical description of the reactants' partitioning behavior. Experiments, conducted with two reactants simultaneously present in the two-phase system, showed that at reactant concentrations in the organic phase higher than 10 mmol/l the partitioning behavior of the investigated reactants is influenced by the presence of the second component. Thus, in systems with multiple reactants the derived correlations are strictly only valid up to this concentration.

[1]  G. Skjåk-Bræk,et al.  Alginate as Immobilization Material for Biocatalysts in Organic Solvents a , 1990 .

[2]  J. Jongejan,et al.  Do organic solvents affect the catalytic properties of lipase? Intrinsic kinetic parameters of lipases in ester hydrolysis and formation in various organic solvents , 1995, Biotechnology and bioengineering.

[3]  Sun Bok Lee,et al.  Effect of water activity on enzyme hydration and enzyme reaction rate in organic solvents , 1995 .

[4]  Alexander M. Klibanov,et al.  Predicting the solvent dependence of enzymatic substrate specificity using semiempirical thermodynamic calculations , 1993 .

[5]  J. Prausnitz,et al.  Extractive catalysis: Solvent effects on equilibria of enzymatic reactions in two-phase systems , 1989 .

[6]  P. Halling,et al.  Substrate specificity and kinetics of Candida rugosa lipase in organic media. , 1996, Enzyme and microbial technology.

[7]  Sun Bok Lee Enzyme reaction kinetics in organic solvents: A theoretical kinetic model and comparison with experimental observations , 1995 .

[8]  A. Klibanov,et al.  On the role of Transition-State Substrate Desolvation in Enzymatic Enantioselectivity in Aqueous-Organic Mixtures , 1998 .

[9]  G. Skjåk‐Braek,et al.  Alginate as immobilization matrix and stabilizing agent in a two-phase liquid system: application in lipase-catalysed reactions. , 1992, Enzyme and microbial technology.

[10]  J. Dordick,et al.  Tailoring lipase specificity by solvent and substrate chemistries , 1993 .

[11]  K. Poutanen,et al.  Applications of immobilized lipases to transesterification and esterification reactions in nonaqueous systems. , 1993, Enzyme and microbial technology.

[12]  C. Bellone,et al.  ON A ROLE , 1996 .

[13]  S. Suye,et al.  Efficient Repeated Use of Alcohol Dehydrogenase with NAD + Regeneration in an Aqueous-organic Two-phase System , 2002 .

[14]  J. Cabral,et al.  Production of Ethyl Butyrate by Candida rugosa Lipase Immobilized in Polyurethane , 1991 .

[15]  A. Janssen,et al.  Solvent effects on lipase‐catalyzed esterification of glycerol and fatty acids , 1993, Biotechnology and bioengineering.

[16]  A. Janssen,et al.  The nature of fatty acid modifies the equilibrium position in the esterification catalyzed by lipase. , 2000, Biotechnology and bioengineering.

[17]  Aage Fredenslund,et al.  Group‐contribution estimation of activity coefficients in nonideal liquid mixtures , 1975 .

[18]  S. Ferreira-Dias,et al.  Production of monoglycerides by glycerolysis of olive oil with immobilized lipases: effect of the water activity , 1995 .

[19]  A. Klibanov,et al.  Solvent variation inverts substrate specificity of an enzyme , 1993 .

[20]  K. Takeda,et al.  DIMERIZATION OF SOME CARBOXYLIC ACIDS IN ORGANIC PHASES , 1987 .

[21]  Jinchuan Wu,et al.  Esterification reactions catalyzed by surfactant-coated Candida rugosa lipase in organic solvents , 2002 .

[22]  A. Marty,et al.  Combining solvent engineering and thermodynamic modeling to enhance selectivity during monoglyceride synthesis by lipase-catalyzed esterification. , 2001, Enzyme and microbial technology.

[23]  J. Vandecasteele,et al.  Enzymatic esterification in organic media: role of water and organic solvent in kinetics and yield of butyl butyrate synthesis , 1991, Applied Microbiology and Biotechnology.

[24]  T. Antczak,et al.  Mathematical modelling of ester synthesis by lipase in biphasic system , 2001 .

[25]  P. Halling,et al.  Solvent selection for biocatalysis in mainly organic systems: Predictions of effects on equilibrium position , 1990, Biotechnology and bioengineering.

[26]  F. Kolisis,et al.  Solvent Effects on Equilibrium Position and Initial Rate of Lipase-catalyzed Esterification Reactions in Organic Solvents: Experimental Results and Prediction Capabilities , 2002 .

[27]  Jiding Li,et al.  A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties , 1993 .

[28]  U. Weidlich A modified UNIFAC model. 1. Prediction of VLE, h_E, and g_E , 1987 .

[29]  P. Adlercreutz,et al.  Water activity and substrate concentration effects on lipase activity. , 1997, Biotechnology and bioengineering.

[30]  P. Halling,et al.  Kinetics of lipase-catalyzed esterification in organic media : correct model and solvent effects on parameters , 1999 .

[31]  Zhen Yang,et al.  Partition coefficients of substrates and products and solvent selection for biocatalysis under nearly anhydrous conditions , 1994, Biotechnology and bioengineering.

[32]  Suojiang Zhang,et al.  Prediction of infinite dilution activity coefficients in aqueous solutions by group contribution models. A critical evaluation , 1998 .

[33]  D. Frense,et al.  Immobilization of Candida rugosa lipase in lyotropic liquid crystals and some properties of the immobilized enzyme , 1996, Biotechnology Letters.

[34]  Jürgen Gmehling,et al.  From UNIFAC to Modified UNIFAC (Dortmund) , 2001 .

[35]  A. Janssen,et al.  Solvent effects on the equilibrium position of lipase-catalyzed esterification of decanoic acid and various alcohols. , 1993 .