Optimisation of enzymatic synthesis of cefaclor with in situ product removal and continuous acyl donor feeding

Enzymatic synthesis of cefaclor by penicillin acylase (PA) was carried out under kinetic control with in situ product removal (ISPR). We present a continuous acyl donor feeding strategy for enzymatic reactions. Using this strategy, the conversion of the antibiotic nucleus was improved from 65 to 91%, and the hydrolysis of phenylglycine methyl ester (PGME) was decreased. Side product (phenylglycine) production was less than half of that in the control batch. The ratio of synthesis to hydrolysis (S/H) in the process was kept stable for longer and at a higher level than in the control. This is a practical method for enzymatic synthesis of cefaclor.     

Enhanced enzymatic synthesis of a semi-synthetic cephalosprin,cefaclor, with in situ product removal

In the enzymatic synthesis of cefaclor, 3-chloro-7-d-(2-phenylglycinamide)-3-cephem-4-carboxylic acid, from phenylglycine methyl ester and 7-aminodesacetoxymethyl-3-chlorocephalosporanic acid, the in situ product could influence both the overall conversion and hydrolysis of the ester. Optimization of the parameters, such as pH 6.2, 5 °C and substrate molar ratio of 2:1, made in situ product removal improve the overall conversion from 64% to 85% (mol/mol).     

A Theory for the Displacement of Proteins and Viruses with Polyethylene Glycol

The displacement action of polyethylene glycol of different molecular weights may be linked to the ability of the polymers to form coiled particles in solution. From conclusions drawn from their sedimentating properties in centrifugal fields the polyethylene glycols of low molecular weights, as expected, are les randomly coiled than those of higher molecular weight. It is suggested that protein molecules have the ability to diffuse into the coils of the polyethylene glycol from which they are excluded when the random coiling increases with increasing polymer concentration. From considerations based on the interaction of the polymer filament with the displaced particle the distribution of the substance between the coils and the intermolecular spaces may be predicted semi-quantitatively.     

Effect of acyl donor chain length and sugar/acyl donor molar ratio on enzymatic synthesis of fatty acid fructose esters

Lipase-catalyzed synthesis of fatty acid sugar esters through direct esterification was performed in 2-methyl 2-butanol as solvent. Fructose and saturated fatty acids were used as substrates and the reaction was catalyzed by immobilized Candida antarctica lipase. The effect of the initial fructose/acyl donor molar ratio and the carbon-chain length of the acyl donor as well as their reciprocal interactions on the reaction performance were investigated. For this purpose, an experimental design taking into account variations of the molar ratio (from 1:1 to 1:5) and the carbon-chain length of the fatty acid (from C8 to C18) was employed. Statistical analysis of the data indicated that the two factors as well as their interactions had significant effects on the sugar esters synthesis. The obtained results showed that whatever the molar ratio used, the highest concentration (73 g l⁻¹), fructose and fatty acid conversion yields (100% and 80%, respectively) and initial reaction rate (40 g l⁻¹ h⁻¹) were reached when using the C18 fatty acid as acyl donor. Low molar ratios gave the best fatty acid conversion yields and initial reaction rates, whereas the best total sugar ester concentrations and fructose conversion yields were obtained for high molar ratios.     

Two-step,one-pot enzymatic synthesis of cefprozil from -phenylacetamido-3-propenyl-cephalosporanic acid (GPRA)

One-pot synthesis of cefprozil was successfully conducted via a two-step enzymatic transformation catalysed by immobilized penicillin acylase from E. coli, where 7-phenylacetamido-3-propenyl-cephalosporanic acid (GPRA) was hydrolysed to 7-amino-3-propenyl-cephalosporanic acid (APRA) and the formed APRA was simultaneously acylated with the hydroxyethyl ester of 4-hydroxy-D-phenylglycine (HPGHE) to produce cefprozil. The yield of cefprozil achieved was around 95%.     

Simple and efficient solid support scavenging of excess acyl donors after enzymatic acylations in organic solvents

A simple and efficient method for removing excess acyl donors following enzymatic acylations in organic solvents was developed. This method is based on selective chemical scavenging of acyl donors using an amino-functionalized solid support, and does not affect the desired acylated product. A wide variety of different acyl donors, including vinyl and trifluoroethyl esters and vinyl carbonates, can be quantitatively removed by this method, thus providing a simple and highly efficient tool for purification of reaction products after enzymatic acylation.     

In situ product removal using a crystallization loop in asymmetric reduction of 4-oxoisophorone by Saccharomyces cerevisiae

In situ product crystallization was investigated for solid product crystals that were obtained during fermentation. The model reaction was the asymmetric reduction of 4-oxoisophorone (OIP) using baker's yeast (S. cerevisiae) as a biocatalyst. The target product was 6R-dihydro-oxoisophorone (DOIP), also known as levodione, a key intermediate in carotenoid synthesis. DOIP was degraded by baker's yeast mainly to (4S,6R)-actinol, an unwanted byproduct in the process. Actinol formation reached up to 12.5% of the initial amount of OIP in the reactor during a batch process. However, better results were obtained when the dissolved DOIP concentration was controlled using an integrated fermentation-crystallization process because: (a) actinol formation was reduced to 4%; and (b) DOIP crystal formation in the reactor was avoided. DOIP productivity was improved by 50% and its selectivity was raised from 87% to 96% relative to the batch process. In the integrated process, most of the product was recovered as pure crystals; this may already minimize, if not eliminate, the need for organic solvents in the final purification steps. An almost sixfold reduction in biocatalyst consumption per kilogram product was achieved, which also can contribute to the minimization of waste streams.     

Chemical permeabilization and in situ removal of daidzein from biologically viable soybean (Glycine max) seeds

After 24 h of chemical permeabilization with 20% (v/v) methanol at 25 °C, the amount of daidzein released from soybean seeds is 15 to 20% of the amount (0.0423 ± 0.0045 mg/g seed dry wt) obtained by physical grinding. With this chemical permeabilization condition, 70% of the permeabilized seeds are still able to germinate. The release of daidzein is enhanced to 33% with the addition of XAD-4 to 20% (v/v) methanol without affecting seed viability. © Rapid Science Ltd. 1998     

Advantages of using non-isothermal bioreactors for the enzymatic synthesis of antibiotics: the penicillin G acylase as enzyme model

A new hydrophobic and catalytic membrane was prepared by immobilizing Penicillin G acylase (PGA, EC.3.5.1.11) from E. coli on a nylon membrane, chemically grafted with butylmethacrylate (BMA). Hexamethylenediamine (HMDA) and glutaraldehyde (Glu) were used as a spacer and coupling agent, respectively. PGA was used for the enzymatic synthesis of cephalexin, using D(-)-phenylglycine methyl ester (PGME) and 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) as substrates. Several factors affecting this reaction, such as pH, temperature, and concentrations of substrates were investigated. The results indicated good enzyme-binding efficiency of the pre-treated membrane, and an increased stability of the immobilized PGA towards pH and temperature. Calculation of the activation energies showed that cephalexin production by the immobilized biocatalyst was limited by diffusion, resulting in a decrease of enzyme activity and substrate affinity. Temperature gradients were employed as a way to reduce the effects of diffusion limitation. Cephalexin was found to linearly increase with the applied temperature gradient. A temperature difference of about 3 degrees C across the catalytic membrane resulted into a cephalexin synthesis increase of 100% with a 50% reduction of the production times. The advantage of using non-isothermal bioreactors in biotechnological processes, including pharmaceutical applications, is also discussed.     

Semi‐continuous in situ magnetic separation for enhanced extracellular protease production—modeling and experimental validation

In modern biotechnology proteases play a major role as detergent ingredients. Especially the production of extracellular protease by Bacillus species facilitates downstream processing because the protease can be directly harvested from the biosuspension. In situ magnetic separation (ISMS) constitutes an excellent adsorptive method for efficient extracellular protease removal during cultivation. In this work, the impact of semi‐continuous ISMS on the overall protease yield has been investigated. Results reveal significant removal of the protease from Bacillus licheniformis cultivations. Bacitracin‐functionalized magnetic particles were successfully applied, regenerated and reused up to 30 times. Immediate reproduction of the protease after ISMS proved the biocompatibility of this integrated approach. Six subsequent ISMS steps significantly increased the overall protease yield up to 98% because proteolytic degradation and potential inhibition of the protease in the medium could be minimized. Furthermore, integration of semi‐continuous ISMS increased the overall process efficiency due to reduction of the medium consumption. Process simulation revealed a deeper insight into protease production, and was used to optimize ISMS steps to obtain the maximum overall protease yield. Biotechnol. Bioeng. 2013; 110: 2161–2172. © 2013 Wiley Periodicals, Inc.     

Kinetically controlled acylation of 6-APA catalyzed by penicillin acylase from Streptomyces lavendulae: effect of reaction conditions in the enzymatic synthesis of penicillin V

Abstract

Enzymatic synthesis of penicillin V (penV) by acylation of 6-aminopenicillanic acid (6-APA) was carried out using methyl phenoxyacetate (MPOA) as activated acyl donor and soluble penicillin acylase from Streptomyces lavendulae (SlPVA) as biocatalyst. The effect of different reaction conditions on penV synthesis was investigated, such as enzyme concentration, pH, molar ratio of 6-APA to MPOA, as well as presence of DMSO as water-miscible co-solvent at different concentrations. Time-course profiles of all reactions followed the typical pattern of kinetically controlled synthesis (KCS) of β-lactam antibiotics: penV concentration reached a maximum (highest yield or Y_max) and then decreased gradually. Such maximum was higher at pH 7.0, observing that final penV concentration was abruptly reduced when basic pH values were employed in the reaction. Under the selected conditions (100?mM Tris/HCl buffer pH 7.0, 30?°C, 2.7% (v/v) DMSO, 20?mM MPOA, 0.3 UI/ml of SlPVA), Y_max was enhanced by increasing the substrate molar ratio (6-APA to MPOA) up to 5, reaching a maximum of 94.5% and a S/H value of 16.4 (ratio of synthetic activity to hydrolytic activity). As a consequence, the use of an excess of 6-APA as nucleophile has allowed us to obtain some of the highest Y_max and S/H values among those reported in literature for KCS of β-lactam antibiotics. Although many penicillin G acylases (PGAs) have been described in kinetically controlled acylations, SlPVA should be considered as a different enzyme in the biocatalytic tool-box for novel potential synthetic processes, mainly due to its different substrate specificity compared to PGAs.     

Penicillin acylase-catalyzed synthesis of beta-lactam antibiotics in highly condensed aqueous systems: beneficial impact of kinetic substrate supersaturation

Advantages of performing penicillin acylase-catalyzed synthesis of new penicillins and cephalosporins by enzymatic acyl transfer to the beta-lactam antibiotic nuclei in the supersaturated solutions of substrates have been demonstrated. It has been shown that the effective nucleophile reactivity of 6-aminopenicillanic (6-APA) and 7-aminodesacetoxycephalosporanic (7-ADCA) acids in their supersaturated solutions continue to grow proportionally to the nucleophile concentration. As a result, synthesis/hydrolysis ratio in the enzymatic synthesis can be significantly (up to three times) increased due to the nucleophile supersaturation. In the antibiotic nuclei conversion to the target antibiotic the remarkable improvement (up to 14%) has been gained. Methods of obtaining relatively stable supersaturated solutions of 6-APA, 7-ADCA, and D-p-hydroxyphenylglycine amide (D-HPGA) have been developed and syntheses of ampicillin, amoxicillin, and cephalexin starting from the supersaturated homogeneous solutions of substrates were performed. Higher synthetic efficiency and increased productivity of these reactions compared to the heterogeneous "aqueous solution-precipitate" systems were observed. The suggested approach seems to be an effective solution for the aqueous synthesis of the most widely requested beta-lactam antibiotics (i.e., amoxicillin, cephalexin, cephadroxil, cephaclor, etc.).     

Design and evaluation of a continuous semipartition bioreactor for in situ liquid‐liquid extractive fermentation

Extractive fermentation (or in situ product removal (ISPR)) is an operational method used to combat product inhibition in fermentations. To achieve ISPR, different separation techniques, modes of operation and physical reactor configurations have been proposed. However, the relative paucity of industrial application necessitates continued investigation into reactor systems. This article outlines a bioreactor designed to facilitate in situ product extraction and recovery, through adapting the reaction volume to include a settler and solvent extraction and recycle section. This semipartition bioreactor is proposed as a new mode of operation for continuous liquid‐liquid extractive fermentation. The design is demonstrated as a modified bench‐top fermentation vessel, initially analysed in terms of fluid dynamic studies, in a model two‐liquid phase system. A continuous abiotic simulation of lactic acid (LA) fermentation is then demonstrated. The results show that mixing in the main reaction vessel is unaffected by the inserted settling zone, and that the size of the settling tube effects the maximum volumetric removal rate. In these tests the largest settling tube gave a potential continuous volumetric removal rate of 7.63 ml/min; sufficiently large to allow for continuous product extraction even in a highly productive fermentation. To demonstrate the applicability of the developed reactor, an abiotic simulation of a LA fermentation was performed. LA was added to reactor continuously at a rate of 33ml/h, while continuous in situ extraction removed the LA using 15% trioctylamine in oleyl alcohol. The reactor showed stable LA concentration of 1 g/L, with the balance of the LA successfully extracted and recovered using back extraction. This study demonstrates a potentially useful physical configuration for continuous in situ extraction.     

The effect of feedback regulation and in situ product removal on the conversion of sugar to cycloheximide by Streptomyces griseus

An addition of cycloheximide to cycloheximide-producing Streptomyces griseus cultures resulted in reductions in the production rate and in the conversion of sugar into cycloheximide. In situ cycloheximide adsorption was observed to enhance: total cycloheximide titers; productivities; and the conversion of sugar to cycloheximide. During the secondary metabolite-producing phase, sugar consumption was observed to be linearly dependent on cycloheximide productivity. From this analysis a true product yield and maintenance coefficient were estimated to be 0.08 g cycloheximide/g glucose and 0.028 g glucose/g cell-h, respectively. The sixfold difference between this true product yield and a theoretical value obtained from knowledge of the biosynthetic pathway is discussed. Since the maintenance sugar requirement for cycloheximide production is large, stimulation of biosynthesis through in situ adsorption significantly increases the overall efficiency of sugar conversion to this secondary metabolite.     

醌那霉素生物合成中间产物的一锅酶促体系研究

【目的】 通过一锅酶法在体外无细胞条件下重构醌那霉素的生物合成途径,实现从原料辅酶A、乙酰-辅酶A和丙二酸到醌那霉素重要中间体的高效转化。【方法】 纯化得到AlpAB、RavC等8个醌那霉素合成相关蛋白和MCAT、MatB等2个辅助蛋白;利用一锅酶法进行体外反应,并用高效液相色谱(high performance liquid chromatography, HPLC)检测反应产物;利用该体系探究Ⅱ型硫酯酶AlpS在合成通路中的功能及作用底物;利用单一变量法对体系温度、pH、最小聚酮合酶(minimal polyketide synthase, minimal PKS)浓度和Ⅱ型硫酯酶AlpS浓度等条件进行优化。【结果】 体系所需的聚酮合酶和辅助蛋白均获得可溶性表达;利用一锅酶法成功合成了醌那霉素的早期重要中间体SEK15、UWM6、rabelomycin、prejadomycin和dehydrorabelomycin;加入AlpS蛋白后以上5种产物产量均有不同程度的提高,其中prejadomycin和dehydrorabelomycin提高较为显著;优化后的反应最适条件为:温度30℃、pH 7.0、最小聚酮合酶(AlpA、AlpB和RavC)浓度各2.8 μmol/L、AlpS 7.2 μmol/L;prejadomycin的产量提高到302 mg/L。【结论】 本研究成功利用一锅酶法在无细胞条件下重构了醌那霉素的早期生物合成途径,合成了醌那霉素的重要中间体SEK15、UWM6、rabelomycin、prejadomycin和dehydrorabelomycin。研究进一步验证了硫酯酶AlpS的链释放功能并推测其作用底物。     

Pulsed column reactor as a novel tool for continuous enzymatic synthesis of peptide in an aqueous/organic biphasic medium

We propose a novel effective method for a continuous peptide synthesis in an aqueous/organic biphasic medium using a pulsed column reactor. N-Formyl-l-aspartyl-l-phenylalanine methyl ester was enzymatically synthesized continuously. With this extractive method using a pulsed column reactor, we can synthesize peptides with a stable performance even if a peptide (or a peptide-amino acid complex) is precipitated due to its high hydrophobicity.     

Enzyme catalyzed biotransformations in aqueous two-phase systems with precipitated substrate and/or product

Biotransformations catalyzed by free and immobilized enzymes have been carried out in aqueous suspensions with up to 25% (w/w) precipitated substrate or product. For the kinetically controlled synthesis of N-Acetyl-Tyr-Arg-NH(2) with up to 0.8 M insoluble activated substrate N-Acetyl-TyrOEt catalyzed by alpha-chymotrypsin (EC3.4.21.1) the dipeptide yield was found to be >90%. This and the space-time yields were higher than those observed for one-phase aqueous systems and much higher than in systems where the insoluble substrate had been solubilized by addition of organic solvents. In the equilibrium controlled hydrolysis of 0.4 M D-phenylglycine-amide catalyzed by immobilized penicillin amidase (EC 3.5.1.11) the product precipitates. The enzyme immobilized in the support with the smallest pores could be reused without reduction in the rate due to precipitation in the pores. This decreases the number of immobilized enzyme molecules that can be used as biocatalysts. The latter was observed for supports with larger pores as the solubility decreases with increasing particle size. These results demonstrate that biotransformations with insoluble substrates or products using free or immobilized enzymes can be easily carried out in aqueous two-phase systems, without organic solvents, provided that the pore sizes of the supports are sufficiently small and that the rate of mass transfer from the precipitated substrate is large. The latter increases with decreasing particle size. (c) 1995 John Wiley & Sons, Inc.     

Overcoming co‐product inhibition in the nicotinamide independent asymmetric bioreduction of activated CC‐bonds using flavin‐dependent ene‐reductases

Eleven flavoproteins from the old yellow enzyme family were found to catalyze the disproportionation (“dismutation”) of conjugated enones. Incomplete conversions, which were attributed to enzyme inhibition by the co‐product phenol could be circumvented via in situ co‐product removal by scavenging the phenol using the polymeric adsorbent MP‐carbonate. The optimized system allowed to reduce an alkene activated by ester groups in a “coupled‐substrate” approach via nicotinamide‐free hydrogen transfer with >90% conversion and complete stereoselectivity. Biotechnol. Bioeng. 2013;110: 3085–3092. © 2013 The Authors. Biotechnology and Bioengineering Published by Willey Periodicals, Inc.