Modeling, simulation, and kinetic analysis of a heterogeneous reaction system for the enzymatic conversion of poorly soluble substrate.

We developed a kinetic model that describes a heterogeneous reaction system consisting of a solid substrate suspension for the production of D-amino acid using D-hydantoinase. As a biocatalyst, mass-produced free and whole cell enzymes were used. The heterogeneous reaction system involves dissolution of a solid substrate, enzymatic conversion of the dissolved D-form substrate, spontaneous racemization of an L-form substrate to D-form, and deactivation of the enzyme. In the case of using whole cell enzymes, transfer of the dissolved substrate and product through the cell membrane was considered. The kinetic parameters were determined from experiments, literature data, and by using Marquardt's method of nonlinear regression analysis. The model was simulated using the kinetic parameters and compared with experimental data, and a good agreement was observed between the experimental results and the simulation ones. Factors affecting the kinetics of the heterogeneous reaction system were analyzed on the basis of the kinetic model, and the efficiency of the reaction systems using free and whole cell enzymes was also compared.     

Production of D-amino acid using whole cells of recombinant Escherichia coli with separately and coexpressed D-hydantoinase and N-carbamoylase

We developed a fully enzymatic process employing D-hydantoinase and N-carbamoylase for the production of D-amino acid from 5'-monosubstituted hydantoin. For the comparison of the reaction systems using two sequential enzymes, D-hydantoinase of Bacillus stearothermophilus SD1 and N-carbamoyl-D-amino acid amidohydrolase (N-carbamoylase) of Agrobacterium tumefaciens NRRL B11291 were separately expressed in each host cell and coexpressed in the same host cell. A high level and constitutive expression of both enzymes in Escherichia coli in a soluble form was achieved using a promoter derived from B. stearothermophilus SD1. The expression levels of both enzymes ranged from 17% to 23% of the total soluble protein, depending on the expression system. In the case of employing separately expressed enzymes, the product yield of D-hydroxyphenylglycine from D,L-p-hydroxyphenylhydantoin and productivity were 71% and 2.57 mM/g-cell/h in 15 h, respectively. The accumulation of N-carbamoyl-D-hydroxyphenylglycine was significant over the reaction time. On the other hand, use of coexpressed enzymes resulted in 98% product yield of D-hydroxyphenylglycine in 15 h, minimizing the level of intermediates in the reaction mixture. The productivity of coexpressed whole cell reaction was estimated to be 6.47 mM/g-cell/h in 15 h. The coexpressed system was tested for an elevated concentration of D,L-p-hydroxyphenylhydantoin, and efficient production can be achieved.     

Integration of reactive membrane extraction with lipase-hydrolysis dynamic kinetic resolution of naproxen 2,2,2-trifluoroethyl thioester in isooctane

Lipases immobilized on polypropylene powders have been used as the biocatalyst in the enantioselective hydrolysis of (S)-naproxen from racemic naproxen thioesters in isooctane, in which trioctylamine was added to perform in situ racemization of the remaining (R)-thioester substrate. A detailed study of the kinetics for hydrolysis and racemization indicates that increasing the trioctylamine concentration can activate and stabilize the lipase as well as enhance the racemization and non-stereoselective hydrolysis of the thioester. Effects of the aqueous pH value and trioctylamine concentration on (S)-naproxen dissociation and partitioning in the aqueous phase as well as the transportation in a hollow fiber membrane were further investigated. Good agreements between the experimental data and theoretical results were obtained when the dynamic kinetic resolution process was integrated with a hollow fiber membrane to reactively extract the desired (S)-naproxen out of the reaction medium.     

Thermodynamic activity‐based intrinsic enzyme kinetic sheds light on enzyme–solvent interactions

The reaction medium has major impact on biocatalytic reaction systems and on their economic significance. To allow for tailored medium engineering, thermodynamic phenomena, intrinsic enzyme kinetics, and enzyme–solvent interactions have to be discriminated. To this end, enzyme reaction kinetic modeling was coupled with thermodynamic calculations based on investigations of the alcohol dehydrogenase from Lactobacillus brevis (LbADH) in monophasic water/methyl tert‐butyl ether (MTBE) mixtures as a model solvent. Substrate concentrations and substrate thermodynamic activities were varied separately to identify the individual thermodynamic and kinetic effects on the enzyme activity. Microkinetic parameters based on concentration and thermodynamic activity were derived to successfully identify a positive effect of MTBE on the availability of the substrate to the enzyme, but a negative effect on the enzyme performance. In conclusion, thermodynamic activity‐based kinetic modeling might be a suitable tool to initially curtail the type of enzyme–solvent interactions and thus, a powerful first step to potentially understand the phenomena that occur in nonconventional media in more detail. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:96–103, 2017     

Complete conversion of D,L-5-monosubstituted hydantoins with a low velocity of chemical racemization into D-amino acids using whole cells of recombinant Escherichia coli

A reaction system was developed for the production of D-amino acids from D,L-5-monosubstituted hydantoins with a very slow rate of spontaneous racemization. For this purpose the D-hydantoinase and D-carbamoylase from Agrobacterium radiobacter NRRL B11291 were cloned in separate plasmids and expressed in Escherichia coli. The third enzyme, hydantoin racemase, was cloned from Agrobacterium tumefaciens C58. The hydantoin racemase amino acid sequence was significantly similar to those previously described. A reaction system consisting of recombinant Escherichia coli whole cell biocatalysts containing separately expressed D-hydantoinase, D-carbamoylase, and hydantoin recemase showed high substrate specificity and was effective toward both aliphatic and aromatic D,L-5-monosubstituted hydantoins. After optimizing reaction conditions (pH 8 and 50 degrees C), 100% conversion of D,L-5-(2-methylthioethyl)-hydantoin (15 mM) into D-methionine was obtained in 30 min.     

Evaluation of intrinsic immobilized kinetics in hollow fiber reactor systems.

Immobilized cell and enzyme hollow fiber reactors have been developed for a variety of biochemical and biomedical applications. Reported mathematical models for predicting substrate conversion in these reactors have been limited in accuracy because of the use of free-solution kinetic parameters. This paper describes a method for determining the intrinsic kinetics of enzymes immobilized in hollow fiber reactor systems using a mathematical model for diffusion and reaction in porous media and an optimization procedure to fit intrinsic kinetic parameters to experimental data. Two enzymes, a thermophilic beta-galactosidase that exhibits product inhibition and L-lysine alpha-oxidase, were used in the analysis. The intrinsic kinetic parameters show that immobilization enhanced the activity of the beta-galactosidase while decreasing the activity of L-lysine alpha-oxidase. Both immobilized enzymes had higher Km values than did the soluble enzyme, indicating less affinity for the substrate. These results are used to illustrate the significant improvement in the ability to predict substrate conversion in hollow fiber reactors.     

Iteration model of starch hydrolysis by amylolytic enzymes.

An elaborate computer program to simulate the process of starch hydrolysis by amylolytic enzymes was been developed. It is based on the Monte Carlo method and iteration kinetic model, which predict productive and non-productive amylase complexes with substrates. It describes both multienzymatic and multisubstrate reactions simulating the "real" concentrations of all components versus the time of the depolymerization reaction the number of substrates, intermediate products, and final products are limited only by computer memory. In this work, it is assumed that the "proper" substrate for amylases is the glucoside linkages in starch molecules. Dynamic changes of substrate during the simulation adequately influence the increase or decrease of reaction velocity, as well as the kinetics of depolymerization. The presented kinetic model, can be adapted to describe most enzymatic degradations of a polymer. This computer program has been tested on experimental data obtained for alpha- and beta-amylases.     

Asymmetric reduction of alpha, beta-unsaturated ketone to (R) allylic alcohol by Candida chilensis

A pilot scale whole cell process was developed for the enantioselective 1,2-reduction of prochiral alpha,beta-unsaturated ketone to (R) allylic alcohol using Candida chilensis. Initial development showed high enantiomeric excess (EE > 95%) but low product yield (10%). Process development, using a combination of statistically designed screening and optimization experiments, improved the desired alcohol yield to 90%. The fermentation growth stage, particularly medium composition and growth pH, had a significant impact on the bioconversion while process characterization identified diverse challenges including the presence of multiple enzymes, substrate/product toxicity, and biphasic cellular morphology. Manipulating the fermentation media allowed control of the whole cell morphology to a predominantly unicellular broth, away from the viscous pseudohyphae, which were detrimental to the bioconversion. The activity of a competing enzyme, which produced the undesired saturated ketone and (R) saturated alcohol, was minimized to < or =5% by controlling the reaction pH, temperature, substrate concentration, and biomass level. Despite the toxicity effects limiting the volumetric productivity, a reproducible and scaleable process was demonstrated at pilot scale with high enantioselectivity (EE > 95%) and overall yield greater than 80%. This was the preferred route compared to a partially purified process using ultra centrifugation, which led to improved volumetric productivity but reduced yield (g/day). The whole cell approach proved to be a valuable alternative to chemical reduction routes, as an intermediate step for the asymmetric synthesis of an integrin receptor antagonist for the inhibition of bone resorption and treatment of osteoporosis.     

Enantioselective synthesis of L-homophenylalanine by whole cells of recombinant Escherichia coli expressing L-aminoacylase and N-acylamino acid racemase genes from Deinococcus radiodurans BCRC12827

L-Homophenylalanine (l-HPA) is a chiral unnatural amino acid used in the synthesis of angiotensin converting enzyme inhibitors and many pharmaceuticals. To develop a bioconversion process with dynamic resolution of N-acylamino acids for the l-HPA production, N-acylamino acid racemase (NAAAR) and l-aminoacylase (LAA) genes were cloned from Deinococcus radiodurans BCRC12827 and expressed in Escherichia coli XLIBlue. The recombinant enzymes were purified by nickel-chelate chromatography, and their biochemical properties were determined. The NAAAR had high racemization activity toward chiral N-acetyl-homophenylalanine (NAc-HPA). The LAA exhibited strict l-enantioselection to hydrolyze the NAc-l-HPA. A stirred glass vessel containing transformed E. coli cells expressing D. radiodurans NAAAR and LAA was used for the conversion of NAc-d-HPA to l-HPA. Unbalance activities of LAA and NAAAR were found in E. coli cell coexpressing laa and naaar genes, which resulted in the accumulation of an intermediate, NAc-l-HPA, in the early stage of conversion and a low productivity of 0.83 mmol l-HPA/L h. The results indicated that low activity of LAA present in the biomass is the rate-limiting factor in l-HPA production. In the case of two whole cells with separately expressed enzyme, the enzymatic activities of LAA and NAAAR could be balanced by changing the loading of individual cells. When the activities of two enzymes were fixed at 3600 U/L, 99.9% yield of l-HPA could be reached in 1 h, with a productivity of 10 mmol l-HPA/L h. The cells can be reused at least six cycles at a conversion yield of more than 96%. This is the first NAAAR/LAA process using NAc-HPA as substrate and recombinant whole cells containing Deinococcus enzymes as catalysts for the production of l-HPA to be reported.     

Kinetic modeling of omega-transamination for enzymatic kinetic resolution of alpha-methylbenzylamine

A kinetic model for omega-transaminase from Bacillus thuringiensis JS64 was developed by using the King-Altman method to simulate the kinetic resolution of alpha-methylbenzylamine (alpha-MBA). Starting from a ping-pong bi-bi mechanism, a complete kinetic model including substrate inhibition only in the reverse reaction (i.e., transamination between acetophenone and L-alanine) was developed. The asymmetric synthesis of (S)-alpha-MBA proved to be difficult due to a much lower maximum reverse reaction rate than the maximum forward reaction rate, thermodynamically exergonic forward reaction (i.e., transamination between (S)-alpha-MBA and pyruvate), and the severe product and substrate inhibition of the reverse reaction. Experimental values for kinetic parameters show that the product inhibition constant of (S)-alpha-MBA is the most important parameter on determining the resolution reaction rate, suggesting that the resolution reaction rate will be very low unless (S)-alpha-MBA strongly inhibits the reverse reaction. Using the kinetic model, the kinetic resolution of alpha-MBA in aqueous buffer was simulated, and the simulation results showed a high degree of consistency with experimental data over a range of reaction conditions. Various simulation results suggest that the crucial bottleneck in the kinetic resolution of alpha-MBA lies mainly in the accumulation of acetophenone in reaction media as the reaction proceeds, whereas L-alanine exerts a little inhibitory effect on the reaction. The model predicts that removing acetophenone produced during the reaction can enhance the reaction rate dramatically. Indeed, the biphasic reaction system is capable of extracting acetophenone from the aqueous phase, showing a much higher reaction rate compared to a monophasic reaction system. The kinetic model was also useful in predicting the properties of other, better enzymes as well as the optimal concentrations of amino acceptor and enzyme in the resolution reaction.     

Unexpected racemization of proline or hydroxy-proline phenacyl ester during coupling reactions with Boc-amino acids.

When L-proline or O-benzyl-trans-4-hydroxy-L-proline phenacyl ester was coupled with Boc-amino acids in dimethylformamide using water-soluble carbodiimide (WSCI) in the presence of anhydrous 1-hydroxybenzotriazole (HOBt) as coupling reagents, extensive racemization was observed at the C alpha of the proline or hydroxy-proline residue. The extent of racemization was measured by HPLC after the coupling with Boc-L-Leu-OH in the presence or absence of HOBt. The extent of racemization increased when HOBt was added to the reaction mixture, but greatly decreased when it was not, indicating that HOBt was needed for inducing racemization. Almost no racemization was observed when the coupling reaction was carried out by the mixed anhydride procedure in tetrahydrofuran or by the carbodiimide method in dichloromethane without using HOBt. In the case of coupling reactions with ordinary L-amino acid phenacyl esters, no racemization was observed. Examination of some model systems yielded sufficient evidence to prove that HOBt is an efficient catalyst for racemizing proline or hydroxy-proline phenacyl ester not only in the stage of cyclic intermediate formation but also in the opening of the ring structure. Thus, the racemization reaction was found to be closely related to the formation of the cyclic carbinol-amine derivative.     

Tautomerism of 4-hydroxy-2,5-dimethyl-3(2H)-furanone: evidence for its enantioselective biosynthesis

Chiral natural flavor compounds exhibit characteristic enantiomeric excesses due to stereoselective, enzymatically catalyzed reactions during biogenesis. Although the enzymatic formation of the strawberry key flavor compound 4-hydroxy-2,5-dimethyl-3(2H)-furanone (HDMF; Furaneol(R)) is anticipated, the naturally occurring compound is racemic. As racemization due to keto-enol-tautomerism of HDMF could account for this observation, HDMF was investigated by (1)H-NMR spectroscopy tracing the exchange of the proton bound to the furanone-ring at C2 with deuteron from the medium (D(2)O). In addition, the racemization rate of HDMF was directly determined by cyclodextrin-modified capillary electrophoresis of enantiomerically enriched HDMF stored at different pH values. Tautomerism and the racemization rate of HDMF was lowest at pH values between 4 and 5. However, tautomerism and thus racemization was catalyzed under stronger acidic conditions (pH 2) and especially at pH values greater than 7, the value published for plant cell cytosol. Approximately 50% of the protons at C2 were exchanged with deuteron within 1 h at pH 7.2. Therefore, in order to demonstrate the enzymatic formation of HDMF, incubation experiments with Zygosaccharomyces rouxii as well as strawberry protein extract were carried out under slightly acidic conditions (pH 5), the most suitable pH value for studies on the enantiomeric ratio of HDMF. In both experiments the formation of enantiomerically enriched HDMF could be demonstrated for the first time, whereas incubation experiments under neutral conditions resulted in the detection of racemic HDMF.     

Glucoamylase and glucose oxidase preparations and their combined application for conversion of maltose to gluconic acid

The kinetic behavior of a system of multiple enzyme in solution has been studied in a variable volume batch reactor at pH 5, controlled dissolved oxygen concentration, and T = 30°C. The enzymes used were glucoamylase (R. delemar), glucose oxidase (A. niger), and gluconolactonase (A. niger), all of which are important commercial biocatalysts, and a disaccharide was employed as the starting substrate. This study includes the basic kinetic properties of individual enzymes and interactions between components of the reaction mixture. Classical Michaelis–Menten single substrate or two substrate kinetic with parameters based on initial rate data predict correctly the batch time course of the sequential reaction network.     

Racemization of chlorthalidone in the presence of liposomes

The extent of racemization of (+)-chlorthalidone as a function of pH is examined. The minimum of the log K/pH curve is pH 3. The reaction mechanism of inversion is postulated to involve a carbenium cation over the entire pH range and a ring opening reaction in the alkaline range. The influence of liposomes on the inversion rate is also studied, retardation of the racemization rate being observed with increasing liposome concentration. A model of drug distribution between liposome phase and aqueous phase based on the Nernst distribution principle is presented and reaction kinetic aspects are considered. © 1993 Wiley-Liss, Inc.     

Controlling reaction specificity in pyridoxal phosphate enzymes

Pyridoxal 5'-phosphate enzymes are ubiquitous in the nitrogen metabolism of all organisms. They catalyze a wide variety of reactions including racemization, transamination, decarboxylation, elimination, retro-aldol cleavage, Claisen condensation, and others on substrates containing an amino group, most commonly α-amino acids. The wide variety of reactions catalyzed by PLP enzymes is enabled by the ability of the covalent aldimine intermediate formed between substrate and PLP to stabilize carbanionic intermediates at Cα of the substrate. This review attempts to summarize the mechanisms by which reaction specificity can be achieved in PLP enzymes by focusing on three aspects of these reactions: stereoelectronic effects, protonation state of the external aldimine intermediate, and interaction of the carbanionic intermediate with the protein side chains present in the active site. This article is part of a Special Issue entitled: Pyridoxal Phosphate Enzymology.     

A general solution for the steady-state kinetics of immobilized enzyme systems

A power series solution is presented which describes the steady-state concentration profiles for substrate and product molecules in immobilized enzyme systems. Diffusional effects and product inhibition are incorporated into this model. The kinetic consequences of diffusion limitation and product inhibition for immobilized enzymes are discussed and are compared to kinetic behavior characteristic of other types of effects, such as substrate inhibition and substrate activation.     

Transient-time analysis of substrate-channelling in interacting enzyme systems.

The kinetics of dynamically interacting enzyme systems is examined, in the light of increasing evidence attesting to the widespread occurrence of this mode of organization in vivo. The transient time, a key phenomenological parameter for the coupled reaction, is expressed as a function of the lifetime of the intermediate substrate. The relationships between the transient time and the pseudo-first-order rate constants for the coupled reaction by the complexed and uncomplexed enzyme species are indicative of the mechanism of intermediate transfer ('channelling'). In a dynamically interacting enzyme system these kinetic parameters are composite functions of those for the processes catalysed by the complex and by the separated enzymes. The mathematical paradigm can be extended to a linear sequence of N coupled reactions catalysed by dynamically (pair-wise) interacting enzymes.     

Structure-function correlation of fatty acyl-CoA dehydrogenase and fatty acyl-CoA oxidase

We have employed a new pseudosubstrate, beta-(2-furyl)propionyl coenzyme A (FPCoA), to study the functional properties of two enzymes, fatty acyl-CoA dehydrogenase from porcine liver and fatty acyl-CoA oxidase from Candida tropicalis, involved in the oxidation of fatty acids. Previous studies from our laboratory have shown that the dehydrogenase exhibits oxidase activity at the rate of dissociation of the product charge-transfer complex. This raises the question of the difference in functionality between these two flavoproteins. To investigate these differences, we have compared the pH dependence of product formation, the isotope effects using tetradeuterio-FPCoA, and the spectral properties and chemical reactivity of the product charge-transfer complexes formed with the two enzymes. The pH dependencies of the reaction of FPCoA with electron-transfer flavoprotein (ETF) for the dehydrogenase and of the reaction of FPCoA with O2 for the oxidase are quite similar. Both reactions proceed more rapidly at basic pH values while substrate binds more tightly at acidic pH values. These data for both enzymes are consistent with a mechanism in which enzyme is involved in protonation of the carbonyl group of substrate followed by base-catalyzed removal of the C-2 proton from substrate. The C-2 anion of substrate may then serve as the active species in reduction of enzyme-bound flavin. The deuterium isotope effects for both enzyme systems are primary across the entire pH range, assuring that the chemically important step of substrate oxidation is rate limiting in these steady-state kinetic experiments. The two enzymes differ in the chemical reactivity of their product charge-transfer complexes.(ABSTRACT TRUNCATED AT 250 WORDS)     

Kinetic properties of sorbitol dehydrogenase from calf liver cell cytoplasm

The kinetic properties of sorbitol dehydrogenase from calf liver cell cytoplasm during sorbitol oxidation were studied at pH 7.0, 7.5, 8.0, 9.0 and 10.0. It was found that the shape of kinetic curves for NADH accumulation depends on pH and substrate concentration. At pH 7.0, 7.5 and 8.0 the enzymatic reaction obeys the Michaelis-Menten kinetics with Km of 3.3 x 10(-3) M. 2.3 x 10(-3) M and 2.08 x 10(-3) M, respectively. At pH 9.0 and 10.0 the vovs [So] curves have an "intermediate plateau". The Hill plots for this reaction reveal two slopes that are dependent on substrate concentration. The nH values for sorbitol (up to 2 mM) are 1.0 and 1.16 at pH 9.0 and 10.0, respectively. With a further rise in the substrate concentration, the nH value increases up to 2.4 and 2.18 at pH 9.0 and 10.0, respectively. This is suggestive of the existence of a slowly dissociating enzymatic system of the Np in equilibrium P type (where P is the oligomeric and p the monomeric forms of the enzyme); N approximately greater than 2. The vovs NAD plots are S-shaped at all pH values studied. The data obtained are discussed in terms of regulatory effects of sorbitol and acidity on association-dissociation of sorbitol dehydrogenase from liver cell cytoplasm.     

A kinetic study of hypoxanthine oxidation by milk xanthine oxidase.

The course of the reaction sequence hypoxanthine----xanthine----uric acid catalysed by xanthine:oxygen oxidoreductase from milk was investigated on the basis of u.v. spectra taken during the course of hypoxanthine and xanthine oxidations. It was found that xanthine accumulated in the reaction mixture when hypoxanthine was used as a substrate. The time course of the concentrations of hypoxanthine, xanthine intermediate and uric acid product was simulated numerically. The mathematical model takes into account the competition of substrate, intermediate and product and the accumulation of the intermediate at the enzyme. This type of analysis permits the kinetic parameters of the enzyme for hypoxanthine and xanthine to be obtained.