Biotechnological production of enantiopure epoxides by enzymatic kinetic resolution

Enantiopure epoxides are high value-added synthons for the production of pharmaceuticals, agrochemicals, as well as versatile fine chemicals and have broad scope of market demand for their applications. A major challenge in conventional organic synthesis is to generate such compounds in high enantiopurity with reasonable yield. Among possible chemical and biological technologies for enantiopure epoxide preparation, enzymatic kinetic resolution has been paid much attention with respect to its high enantioselectivity. Epoxide hydrolase (EH) has shown promising characteristics for the preparation of enantiopure epoxides and vicinal diols during enantioselective hydrolysis of racemic epoxides. EH is readily available from microbial resources thus it is being employed for biohydrolysis of a variety of epoxides. Recent technical progress in EH-catalyzed enantioselective hydrolysis is summarized in terms of exploration of novel EH, its functional improvement, high throughput assay, and preparative scale resolution process.     

On liquid-liquid mass transfer in two-liquid-phase fermentations

Almost all two-liquid phase bioprocesses are characterized by the presence of surface active materials (biosurfactants), which significantly influence the interaction between the phases. In order to predict mass transfer rates during cultivations of Pseudomonas oleovorans biosurfactant was isolated from the biosuspension and added in defined amounts to n-octane/water model-dispersions. Effects of biosurfactant concentration on interfacial tension, mean Sauter-diameter, drop size distribution, dispersion stability and liquid-liquid mass transfer coefficients were studied. A comparison was made between calculated solvent transfer rates (STR) and measured solvent uptake rates (SUR) of P. oleovorans cultures. With increasing interfacial surfactant concentration interfacial tension and mean Sauter-diameter decreased until a minimum for both, interfacial tension and mean Sauter-diameter, were reached. Interfacial tension measurements indicate that these minima have to be attributed to a maximum monomolecular surfactant concentration and the formation of polymolecular adsorption layers. Drop size distributions showed that, coalescence and droplet break-up disappear because droplets are stabilized by the biosurfactant adsorption layers at the interface. Mass transfer regime shifted from forced convection and surface renewal to diffusion. Comparison of solvent uptake rates (SUR) and solvent transfer rates (STR) showed that n-octane transfer usually will not be limiting P. oleovorans cultures, however, can become dominant in cultures where solvents with very low miscibilities like n-decane are used.     

Extracellular polymeric substances enhanced mass transfer of polycyclic aromatic hydrocarbons in the two-liquid-phase system for biodegradation

The objective was to elucidate the role of extracellular polymeric substances (EPS) in biodegradation of polycyclic aromatic hydrocarbons in two-liquid-phase system (TLPs). Therefore, biodegradation of phenanthrene (PHE) was conducted in a typical TLPs—silicone oil–water—with PHE-degrading bacteria capable of producing EPS, Sphingobium sp. PHE3 and Micrococcus sp. PHE9. The results showed that the presence of both strains enhanced mass transfer of PHE from silicone oil to water, and that biodegradation of PHE mainly occurred at the interfaces. The ratios of tightly bound (TB) proteins to TB polysaccharides kept almost constant, whereas the ratios of loosely bound (LB) proteins to LB polysaccharides increased during the biodegradation. Furthermore, polysaccharides led to increased PHE solubility in the bulk water, which resulted in an increased PHE mass transfer. Both LB-EPS and TB-EPS (proteins and polysaccharides) correlated with PHE mass transfer in silicone oil, indicating that both proteins and polysaccharides favored bacterial uptake of PHE at the interfaces. It could be concluded that EPS could facilitate microbial degradation of PHE in the TLPs.     

Mass-transfer limitations for immobilized enzyme-catalyzed kinetic resolution of racemate in a fixed-bed reactor

A mathematical model has been developed for immobilized enzyme-catalyzed kinetic resolution of racemate in a fixed-bed reactor in which the enzyme-catalyzed reaction (the irreversible uni-uni competitive Michaelis-Menten kinetics is chosen as an example) was coupled with intraparticle diffusion, external mass transfer, and axial dispersion. The effects of mass-transfer limitations, competitive inhibition of substrates, deactivation on the enzyme effective enantioselectivity, and the optical purity and yield of the desired product are examined quantitatively over a wide range of parameters using the orthogonal collocation method. For a first-order reaction, an analytical solution is derived from the mathematical model for slab-, cylindrical-, and spherical-enzyme supports. Based on the analytical solution for the steady-state resolution process, a new concise formulation is presented to predict quantitatively the mass-transfer limitations on enzyme effective enantioselectivity and optical purity and yield of the desired product for a continuous steady-state kinetic resolution process in a fixed-bed reactor.     

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.     

Interfacial inactivation of epoxide hydrolase in a two-liquid-phase system

Enantioselective epoxide hydrolases are useful biocatalysts for the preparation of enantiopure epoxides and diols. The kinetic resolution of racemic epoxides can be carried out in an organic/aqueous biphasic system to allow use of high epoxide concentrations. Enzyme inactivation in such a system, however, may occur by contact with the interface. In this study, we investigated the factors which influence the interfacial inactivation of Agrobacterium radiobacter epoxide hydrolase in an octane/water biphasic system. Rates of interfacial inactivation were measured both in a stirred-cell, which has a planar interface, and in an emulsion reactor. Interfacial inactivation rates measured in the stirred-cell at a fixed interfacial area increased with mixing intensity. Interfacial inactivation rates per unit area were lower in the emulsion reactor than in the stirred-cell and increased with bulk aqueous enzyme concentration. Circular dichroism measurements showed that during biphasic incubation all unadsorbed soluble enzyme existed in the native conformation. Activity assays showed that the dissolved enzyme was also fully active, indicating that inactivated enzyme precipitated from solution. Using an inactive epoxide hydrolase mutant structurally similar to the wild-type enzyme in order to avoid the conversion of the epoxide, it was found that high concentrations of epoxide in the organic phase increased the rate of interfacial inactivation.     

Preparative method for isosilybin isolation based on enzymatic kinetic resolution of silymarin mixture

The flavonolignan isosilybin (1) is one of the silybin congeners contained in the silymarin complex, which is isolated from the seeds of the milk thistle (Silybum marianum). A number of recent studies have demonstrated that isosilybin is probably the most potent anticancer agent found in silymarin. It occurs as a mixture of two diastereoisomers, A and B. Lipase Novozym 435 was found to allow the preparative production of both optically pure isosilybin A and B in a diastereoisomeric purity of over 95%. A preparatory method based on the enzymatic resolution and other purification methods has been developed, enabling multigram amounts of both optically pure isosilybins A (1a) and B (1b) to be obtained.     

Improved catalytic activity of homochiral dimeric cobalt-salen complex in hydrolytic kinetic resolution of terminal racemic epoxides

Enantiomerically pure epoxides (99%, ee) and diols (98%, ee) from racemic epichlorohydrin, 1,2-epoxypropane, 1,2-epoxyhexane, 1,2-epoxyoctane, and 1,2-epoxydodecane were obtained in 2-12 h by hydrolytic kinetic resolution (HKR) using the recyclable dimeric homochiral Co(III)-salen complex 1' (0.2 mol %) derived from 5,5-(2',2'-dimethylpropane)-di-[(R,R)-{N-(3-tert-butylsalicylidine)-N'-(3',5'-di-tert-butylsalicylidine)}-1,2-cyclohexanediamine] with cobalt(II) acetate. Unlike its monomeric version, the catalyst could be recycled several times without loss in performance. The use of BF(4) as counter ion in HKR reactions was also investigated.     

酶促拆分丁酸环氧丙酯反应体系的筛选

利用脂肪酶对外消旋丁酸环氧丙酯进行了立体选择性的酯水解反应,考察了水解反应体系对拆分反应的影响。实验结果表明：在该水解反应中添加适量正己烷有利于拆分反应的进行;反应体系中正己烷与缓冲液的最适体积比为1：1;磷酸盐缓冲液(pH7．6)的最适离子强度为0.03mmol／L。在最适反应条件下,当该酶促拆分反应的转化率为60.6％,(R)-丁酸环氧丙酯的光学纯度可以达到93．3％。     

Effect of mass transfer in a recirculation batch reactor system for immobilized penicillin amidase

The effect of external mass transfer resistance on the overall reaction rate of the immobilized whole cell penicillin amidase of E. coli in a recirculation batch reactor was investigated. The internal diffusional resistance was found negligible as indicated by the value of effectiveness factor, 0.95. The local environmental change in a column due to the pH drop was successfully overcome by employing buffer solution. The reaction rate was measured by pH-stat method and was found to follow the simple Michaelis-Menten law at the initial stage of the reaction. The values of the net reaction rate experimentally determined were used to calculate the substrate concentration at the external surface of the catalyst pellet and then to calculate the mass transfer coefficient, k(L), at various flow rates and substrate concentrations. The correlation proposed by Chilton and Colburn represented adequately the experimental data. The linear change of log j(D) at low log N(Re) with negative slope was ascribed to the fact that the external mass transfer approached the state of pure diffusion in the limit of zero superficial velocity.     

Silicone-stimulated anthraquinone production and release by Morinda citrifolia in a two-liquid-phase system

Summary A 2.5-fold increase in the release of intracellular anthraquinones was obtained by adding 1 ml L^-1 silicone A to suspension cultures of Morinda citrifolia. Cell growth and secondary metabolite production were not affected even at high silicone A concentrations. Performance of the silicone treatment in a two-liquid-phase system (5 ml n-hexadecane/50 ml medium) resulted in a 150% increase of the overall secondary metabolite productivity.     

Enzyme immobilized in a packed-bed reactor: kinetic parameters and mass transfer effects.

To describe axial dispersion, particle film mass transfer, intraparticle diffusion, and the chemical reaction of the substrate for enzymes immobilized in porous particles in packed columns, we have developed mathematical models for first- and zero-order limits of Michaelis-Menten kinetics. Steady-state solutions were derived for both long and short column boundary conditions and for plug flow. Theory was compared to experiments by hydrolysis of sucrose catalyzed by invertase bound to porous glass particles. Steady-state conversions were measured for a range of flow rates. Pulse response experiments with inert packing were used to determine values of bed void fraction and particle porosity.     

A hyperefficient process for enzymatic cellulose hydrolysis in the intensive mass transfer reactor

Summary A new type of bioreactor, the intensive mass transfer reactor (IMTR), has been developed for enzymatic hydrolysis of cellulose. Using T. reesei cellulases (2 FPU/ml), 3.5–6% of sugars were obtained in the IMTR after 0.5–2 h of cellulose hydrolysis with a productivity of 30–73 g/l.h.     

The influence of cosolvent concentration on enzymatic kinetic resolution of trans-2-phenyl-cyclopropane-1-carboxylic acid derivatives

A method to improve the enantioselectivity of lipase-catalyzed kinetic resolution (KR) of trans-2-phenyl-cyclopropane-1-carboxylic acid derivatives in water–acetone solution is presented. Two different approaches were compared: enzyme-catalyzed esterification and enzymatic hydrolysis of the target ester. A substantial influence of enzyme type, ethoxy group donor, and solvent on conversion and enantioselectivity of the enzymatic esterification was noted. While enzymatic esterification proceeds with poor enantioselectivity, the hydrolysis of target ester proceeds efficiently. Studies on the influence of cosolvent used for the enzymatic hydrolysis reaction showed that kinetic resolution can be performed in acetone and water buffer mixture predominantly containing organic solvent. Any change in organic solvent content resulted in a substantial decrease in enantioselectivity from almost E = 150 to less than 5.     

Enzyme‐assisted physicochemical enantioseparation processes—Part III: Overcoming yield limitations by dynamic kinetic resolution of asparagine via preferential crystallization and enzymatic racemization

The application of enantioseparation methods alone can only yield up to 50% of the desired chiral product. Thus enantioseparation becomes more attractive when accompanied by the racemization of the counter‐enantiomer. Here we present first results of dynamic kinetic resolution of L ‐asparagine (L ‐Asn) via preferential crystallization and enzymatic racemization from a racemic, supersaturated solution on a 20 mL scale. An enzyme lyophilisate (WT amino acid racemase from P. putida KT2440 (E.C. 5.1.1.10), overexpressed in E. coli BL21(DE3)) was used for in situ racemization (enzyme concentrations varying from 0 to 1 mg/mL). When preferential crystallization was applied without any enzyme, a total of 31 mg of L ‐Asn monohydrate could be crystallized, before crystal formation of d ‐Asn started. Crystallization experiments accompanied by enzymatic racemization led to a significant increase of crystallized L ‐Asn (198 mg L ‐Asn monohydrate; >92%ee) giving the first experimental proof for this new process concept of dynamic kinetic resolution via preferential crystallization and enzymatic racemization. Measurements of the racemase activity before and after the crystallization process showed no significant differences, which would allow for enzyme recovery and recycling. Biotechnol. Bioeng. 2009; 104: 1235–1239. © 2009 Wiley Periodicals, Inc.     

Effect of additives on mass transfer in turbine aeration

Mass transfer coefficients and interfacial areas were determined for the aeration of aqueous solutions in a turbine agitated vessel. The mass transfer coefficients measured for water without additive and for sodium chloride solutions matched very well to measurements in the literature for air bubbles of the same diameter in free rise. Thus the only effect of agitation was to determine the bubble size which then in turn set the coefficient. Two surface active agents were studied: sodium dodecyl sulfate and Dow Corning Antifoam C. The rate of mass transfer increased with the former additive but decreased with the latter; however, the mass transfer coefficient was the exact same function of bubble diameter in both cases and the different rates are attributed to the quite different effects on interfacial area.     

Asymmetric ring opening of terminal epoxides via kinetic resolution catalyzed by new bimetallic chiral (salen)Co complexes

The highly enantioselective hydrolytic kinetic resolution (HKR) of racemic terminal epoxides by new bimetallic chiral (salen)Co provides a operationally very simple protocol for the synthesis of enantiomerically enriched terminal epoxides (>99% ee) and diols. Optically pure chlorohydrins have been synthesized in one step by ring‐opening reactions of terminal epoxides with HCl using kinetic resolution. © 2005 Wiley‐Liss, Inc. Chirality     

The kinetic and mass transfer behavior of immobilized invertase on ion-exchange resin beads

Immobilized invertase was prepared by binding native invertase to a polyamine type ion-exchange resin. Kinetic behavior of the immobilized invertase on these small pellets was investigated in a packed-bed reactor. For low flow rates, an effect of interparticle diffusion on the Machaelis constant was observed and a correlation was proposed to evaluate the effect. At high flow rates, Michaelis and inhibition constants were determined and compared with those for native invertase. With large pellets, intraparticle diffusion was found to be important and at high substrate concentrations, the effectiveness factor exceeded unity. Good agreement was found between the theoretical analyses and the experimental data.