Integrated reactor concepts for the enzymatic kinetic synthesis of cephalexin

Integrated process concepts for enzymatic cephalexin synthesis were investigated by our group, and this article focuses on the integration of reactions and product removal during the reactions. The last step in cephalexin production is the enzymatic kinetic coupling of activated phenylglycine (phenylglycine amide or phenylglycine methyl ester) and 7-aminodeacetoxycephalosporanic acid (7-ADCA). The traditional production of 7-ADCA takes place via a chemical ring expansion step and an enzymatic hydrolysis step starting from penicillin G. However, 7-ADCA can also be produced by the enzymatic hydrolysis of adipyl-7-ADCA. In this work, this reaction was combined with the enzymatic synthesis reaction and performed simultaneously (i.e., one-pot synthesis). Furthermore, in situ product removal by adsorption and complexation were investigated as means of preventing enzymatic hydrolysis of cephalexin. We found that adipyl-7-ADCA hydrolysis and cephalexin synthesis could be performed simultaneously. The maximum yield on conversion (reaction) of the combined process was very similar to the yield of the separate processes performed under the same reaction conditions with the enzyme concentrations adjusted correctly. This implied that the number of reaction steps in the cephalexin process could be reduced significantly. The removal of cephalexin by adsorption was not specific enough to be applied in situ. The adsorbents also bound the substrates and therewith caused lower yields. Complexation with beta-naphthol proved to be an effective removal technique; however, it also showed a drawback in that the activity of the cephalexin-synthesizing enzyme was influenced negatively. Complexation with beta-naphthol rendered a 50% higher cephalexin yield and considerably less byproduct formation (reduction of 40%) as compared to cephalexin synthesis only. If adipyl-7-ADCA hydrolysis and cephalexin synthesis were performed simultaneously and in combination with complexation with beta-naphthol, higher cephalexin concentrations also were found. In conclusion, a highly integrated process (two reactions simultaneously combined with in situ product removal) was shown possible, although further optimization is necessary.     

Modelling of the enzymatic kinetically controlled synthesis of cephalexin: influence of diffusion limitation

In this study the influence of diffusion limitation on enzymatic kinetically controlled cephalexin synthesis from phenylglycine amide and 7-aminodeacetoxycephalosporinic acid (7-ADCA) was investigated systematically. It was found that if diffusion limitation occurred, both the synthesis/hydrolysis ratio (S/H ratio) and the yield decreased, resulting in lower product and higher by-product concentrations. The effect of pH, enzyme loading, and temperature was investigated, their influence on the course of the reaction was evaluated, and eventually diffusion limitation was minimised. It was found that at pH >or=7 the effect of diffusion limitation was eminent; the difference in S/H ratio and yield between free and immobilised enzyme was considerable. At lower pH, the influence of diffusion limitation was minimal. At low temperature, high yields and S/H ratios were found for all enzymes tested because the hydrolysis reactions were suppressed and the synthesis reaction was hardly influenced by temperature. The enzyme loading influenced the S/H ratio and yield, as expected for diffusion-limited particles. For Assemblase 3750 (the number refers to the degree of enzyme loading), it was proven that both cephalexin synthesis and hydrolysis were diffusion limited. For Assemblase 7500, which carries double the enzyme load of Assemblase 3750, these reactions were also proven to be diffusion limited, together with the binding-step of the substrate phenylglycine amide to the enzyme. For an actual process, the effects of diffusion limitation should preferably be minimised. This can be achieved at low temperature, low pH, and high substrate concentrations. An optimum in S/H ratio and yield was found at pH 7.5 and low temperature, where a relatively low reaction pH can be combined with a relatively high solubility of 7-ADCA. When comparing the different enzymes at these conditions, the free enzyme gave slightly better results than both immobilised biocatalysts, but the effect of diffusion limitation was minimal.     

Enhancement of Enzymatic Adipyl-7-ADCA Hydrolysis

We studied enzymatic adipyl-7-ADCA hydrolysis as a new process for the production of 7-aminodeacetoxycephalosporanic acid (7-ADCA), one of the building blocks for cephalosporin antibiotics like cephalexin and cefadroxil. Adipyl-7-ADCA hydrolysis carried out with immobilised glutaryl acylase was considerably enhanced by addition of phenylglycine amide, the side-chain donor used for cephalexin synthesis; unlike reactions carried out with free enzyme. The rate enhancing effect was not specifically related to phenylglycine amide; we found a linear relationship between the reaction rate and the buffering capacity of the added substance. These observations can be explained by a pH-gradient in the immobilised enzyme, the pH inside the particle being lower (corresponding to low enzyme activity) than outside. It was concluded that the buffer reduced the pH-gradient inside the biocatalyst, and therewith, caused the reaction rate enhancing effects. Further, chloride ions decreased the reaction rate strongly, while sodium, magnesium, sulphate, and potassium did not influence the reaction rate much. For an actual process, it is important to use a buffer that is appropriate for the reaction-pH. In that way the amount of enzyme required in a process can be reduced considerably, in our case a factor of three was found.     

Enhancement of Enzymatic Adipyl-7-ADCA Hydrolysis

We studied enzymatic adipyl-7-ADCA hydrolysis as a new process for the production of 7-aminodeacetoxycephalosporanic acid (7-ADCA), one of the building blocks for cephalosporin antibiotics like cephalexin and cefadroxil. Adipyl-7-ADCA hydrolysis carried out with immobilised glutaryl acylase was considerably enhanced by addition of phenylglycine amide, the side-chain donor used for cephalexin synthesis; unlike reactions carried out with free enzyme. The rate enhancing effect was not specifically related to phenylglycine amide; we found a linear relationship between the reaction rate and the buffering capacity of the added substance. These observations can be explained by a pH-gradient in the immobilised enzyme, the pH inside the particle being lower (corresponding to low enzyme activity) than outside. It was concluded that the buffer reduced the pH-gradient inside the biocatalyst, and therewith, caused the reaction rate enhancing effects. Further, chloride ions decreased the reaction rate strongly, while sodium, magnesium, sulphate, and potassium did not influence the reaction rate much. For an actual process, it is important to use a buffer that is appropriate for the reaction-pH. In that way the amount of enzyme required in a process can be reduced considerably, in our case a factor of three was found.     

A two-step,one-pot enzymatic synthesis of cephalexin from D-phenylglycine nitrile

A cascade of two enzymatic transformations is employed in a one-pot synthesis of cephalexin. The nitrile hydratase (from R. rhodochrous MAWE)-catalyzed hydration of D-phenylglycine nitrile to the corresponding amide was combined with the penicillin G acylase (penicillin amidohydrolase, E.C. 3.5.1.11)-catalyzed acylation of 7-ADCA with the in situ-formed amide to afford a two-step, one-pot synthesis of cephalexin. D-Phenylglycine nitrile appeared to have a remarkable selective inhibitory effect on the penicillin G acylase, resulting in a threefold increase in the synthesis/hydrolysis (S/H) ratio. 1,5-Dihydroxynaphthalene, when added to the reaction mixture, cocrystallized with cephalexin. The resulting low cephalexin concentration prevented its chemical as well as enzymatic degradation; cephalexin was obtained at 79% yield with an S/H ratio of 7.7.     

Use of aqueous two-phase systems for in situ extraction of water soluble antibiotics during their synthesis by enzymes immobilized on porous supports

Yields of kinetically controlled synthesis of antibiotics catalyzed by penicillin G acylase from Escherichia coli (PGA) have been greatly increased by continuous extraction of water soluble products (cephalexin) away from the surroundings of the enzyme. In this way its very rapid enzymatic hydrolysis has been avoided. Enzymes covalently immobilized inside porous supports acting in aqueous two-phase systems have been used to achieve such improvements of synthetic yields. Before the reaction is started, the porous structure of the biocatalyst can be washed and filled with one selected phase. In this way, when the pre-equilibrated biocatalyst is mixed with the second phase (where the reaction product will be extracted), the immobilized enzyme remains in the first selected phase in spite of its possibly different natural trend. Partition coefficients (K) of cephalexin in very different aqueous two-phase systems were firstly evaluated. High K values were obtained under drastic conditions. The best K value for cephalexin (23) was found in 100% PEG 600-3 M ammonium sulfate where cephalexin was extracted to the PEG phase. Pre-incubation of immobilized PGA derivatives in ammonium sulfate and further suspension with 100% PEG 600 allowed us to obtain a 90% synthetic yield of cephalexin from 150 mM phenylglycine methyl ester and 100 mM 7-amino desacetoxicephalosporanic acid (7-ADCA). In this reaction system, the immobilized enzyme remains in the ammonium sulfate phase and hydrolysis of the antibiotic becomes suppressed because of its continuous extraction to the PEG phase. On the contrary, synthetic yields of a similar process carried out in monophasic systems were much lower (55%) because of a rapid enzymatic hydrolysis of cephalexin.     

Equilibrium position, kinetics, and reactor concepts for the adipyl-7-ADCA-hydrolysis process

One of the building blocks of cephalosporin antibiotics is 7-amino-deacetoxycephalosporanic acid (7-ADCA). It is currently produced from penicillin G using an elaborate chemical ring-expansion step followed by an enzyme-catalyzed hydrolysis. However, 7-ADCA-like components can also be produced by direct fermentation. This is of scientific and economic interest because the elaborate ring-expansion step is performed within the microorganism. In this article, the hydrolysis of the fermentation product adipyl-7-ADCA is studied. Adipyl-7-ADCA can be hydrolyzed in an equilibrium reaction to adipic acid and 7-ADCA using glutaryl-acylase. The equilibrium reaction yield is described as a function of pH, temperature, and initial adipyl-7-ADCA concentration. Reaction rate equations were derived for adipyl-7-ADCA-hydrolysis using three (pH-independent) reaction rate constants and the apparent equilibrium constant. The reaction rate constants were calculated from experimental data. Based on the equilibrium position and reaction rate equations the hydrolysis reaction was optimized and standard reactor configurations were evaluated. It was found that equilibrium yields are high at high pH, high temperature and low-initial adipyl-7-ADCA concentration. The course of the reaction could be described well as a function of pH (7-9), temperature (20-40 degrees C) and concentration using the reaction rate equations. It was shown that a series of CSTR's is the best alternative for the process.     

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.).     

Reaction kinetics of cephalexin synthesizing enzyme from Xanthomonas citri

In enzymatic synthesis of cephalexin from D-alpha-phenylglycine methyl ester (PGM) and 7-amino-3-deacetoxy-cephalosporanic acid (7-ADCA) using alpha-acylamino-beta-lactam acylhydrolase from Xanthomonas citri, it was found that this enzyme catalyzes all three reactions including PGM hydrolysis, cephalexin synthesis, and cephalexin hydrolysis. Based on our experimental results, a mechanistic kinetic model for cephalexin synthesizing enzyme system having acyl-enzyme intermediate was proposed. From this kinetic model, the reaction rate equations for three reactions were derived, and the kinetic parameters were evaluated. A good agreement between the simulation results and the experimental results was found.     

Cephalexin synthesis by partially purified and immobilized enzymes

An enzyme which catalyzes the synthesis of cephalexin fromD -α phenylglycinemethylester (PGM) and 7-amino-3-desacetoxy-cephalosporanic acid (7-ADCA) was prepared from Xanthomonas citri (IFO 3835) and partially purified 30-fold by ammonium sulfate fractionation, DEAE-cellulose, and Sepharose-4B column chromatography. The K_m values for 7-ADCA, PGM, and cephalexin were determined as 11.1, 2.1, and 1.61 mM, respectively. The enzymatic cephalexin synthesis follows the reversible bi-uni reaction kinetics. The equilibrium constant is influenced by the initial mole ratios of 7-ADCA and PGM. The cephalexin hydrolysis is catalyzed by the same cephalexin synthesizing enzyme, but methanol does not participate in the hydrolytic reaction. The amount of enzyme in the reaction mixture affects the initial rate but does not influence the equilibrium product concentration. This cephalexin-synthesizing enzyme was immobilized onto several adsorbents. Among these, Kaolin and bentonite showed a higher retention of enzyme activity and stability for reuse. The immobilized-enzyme reaction kinetics were investigated and compared with those of the soluble enzyme. A rate expression for the enzymatic synthesis of cephalexin was derived. The results of computer simulation showed good agreement with the experimental results.     

Purification and characterization of inducible cephalexin synthesizing enzyme in Gluconobacter oxydans

Cephalexin synthesizing enzyme (CSE) of Gluconobacter oxydans ATCC 9324 was purified up to about 940-fold at a yield of 12%. CSE biosynthesis in G. oxydans was found inducible in the presence of D-phenylglycine but not its substrate phenylglycine methyl ester. The purified enzyme was shown homogeneous on SDS-PAGE and exhibited a specific activity of 440 U per mg protein. The apparent molecular mass of the native enzyme was estimated to be 70 kDa over a Superdex 200 gel filtration column and 68 kDa on SDS-PAGE, indicating that the native enzyme is a monomer. Its isoelectric focusing point is 7.1, indicating a neutral character. The enzyme had maximal activity around pH 6.0 to 6.5, and this activity was thermally stable up to 40 degrees C. Synthesis of cephalexin from D-phenylglycine methyl ester and 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) by the purified CSE was demonstrated. Its L-enantiomer was not accepted by CSE. Apart from cephalexin, ampicillin was also synthesized by the purified CSE from its acyl precursors and 6-aminopenicillanic acid (6-APA). Substrate specificity studies indicated that the enzyme required a free alpha amino group and an activated carboxyl group as a methyl ester of D-form phenylglycine. Interestingly, the purified enzyme did not catalyze hydrolysis of its products, e.g., cephalexin, cephradine, and ampicillin, in contrast to enzymes from other strains of Pseudomonadaceae.     

Enhancement effect of polyethylene glycol on enzymatic synthesis of cephalexin

In an enzymatic synthesis of cephalexin (CEX) using an acylase from Xanthomonas citri, the effect of polyethylene glycol (PEG) on the synthetic reaction of 7-amino-3-deacetoxycephalosporanic acid (7-ADCA) and D-alpha-phenyl-glycine methyl ester (PGM) to CEX was investigated. The addition of PEG (MW 300-20,000) increased the yield significantly. This yield enhancement effect tended to increase with the increasing molecular weight of PEG. Addition of PEG to the reaction system did not affect both the CEX and PGM hydrolytic reactions. The PEG added to the reaction medium used in these experiments did not depress the water activity significantly, and the product yield improvement could not be explained by the activity alone. The PEG stabilized the enzyme activity to some extent, but this stabilizing effect was only partially attributable to the yield enhancement of CEX. The enhancing effect of PEG on the synthetic yield increased with the increasing PEG molecular weight or the length of the poly(oxy-1,2-ethanediyl) chain, which increases the hydrophobicity of PEG. This finding consequently has led to the conclusion that the PEG structure renders the affinity between enzyme and 7-ADCA, which is a hydrophobic substrate. The microenvironmental hydrophobicity of PEG and its interaction with the hydrophobic substrate was found to be the main reason for the improvement of the CEX yield. In fact, the Michaelis-Menten kinetic constant for 7-ADCA, K(7-ADCA) in the presence of PEG was smaller than that in the control system (without PEG addition). (c) 1993 John Wiley & Sons, Inc.     

Comparative study of the enzymatic synthesis of cephalexin at high substrate concentration in aqueous and organic media using statistical model

Synthesis of cephalexin with immobilized penicillin acylase at high substrates concentration at an acyl donor to nucleophile molar ratio of 3 was comparatively evaluated in aqueous and ethylene glycol media using a statistical model. Variables under study were temperature, pH and enzyme to substrate ratio and their effects were evaluated on cephalexin yield, ratio of initial rates of cephalexin synthesis to phenylglycine methyl ester hydrolysis, volumetric and specific productivity of cephalexin synthesis, that were used as response parameters. Results obtained in both reaction media were modeled using surface of response methodology and optimal operation conditions were determined in terms of an objective function based on the above parameters. At very high substrates concentrations the use of organic co-solvents was not required to attain high yields and actually almost stoichiometric yields were obtained in a fully aqueous media with the advantages of higher productivities than in an organic co-solvent media and compliance with the principles of green chemistry.     

聚丙烯腈纤维固定化青霉素酰化酶合成头孢氨苄的研究

将巨大芽孢杆菌胞外青霉素酰化酶通过共价键结合到聚丙烯腈纤维的衍生物上。制成的丝状固定化青霉素酰化酶表现活力达 1 5 3U g(湿重 )。固定化酶合成头孢氨苄的最适pH为 6 5 ,最适温度为 40℃。 7 ADCA的投料浓度以 4%为好 ,7 ADCA与PGME的投料量比率为1∶2 ,最佳用酶量为 1 70U g 7 ADCA。在pH6 5、温度 3 0℃时 ,固定化酶对 7 ADCA的表观米氏常数K7 ADCA为 0 1 6 2mol L ,对PGME的表观米氏常数KPGME为 0 3 6 4mol L ,最大反应速度Vmax为0 0 4 6 2mol·L- 1·min- 1,用固定化酶合成头孢氨苄 ,使用 5 0次保留酶活力 83 9%     

氨基酸酯水解酶产生菌的筛选及其合成头孢立新的研究

From ten genera and 146 bacterial strains, 22 strains producing alpha-amino acid ester hydrolase were selected. Among them, AS 1.586 and 41-2 were the best. The optimal conditions for synthesis of cephalexin by pseudomonas aeruginosa 1.204 were investigated. The optimal pH and temperature for enzymatic synthesis reaction was pH 6.8 and 25 degrees C, respectively. By using 1% 7-ADCA, 3% PGME and 4% biomass, about 70% of 7-ADCA was converted to cephalexin under the mentioned conditions.     

Physico-chemical properties of 7-aminodesacetoxycephalosporanic acid]

7-Aminodesacetoxycephalosporanic acid (7-ADCA) of 99 per cent purity was prepared by enzymatic hydrolysis of 7-phenylacetamidodesacetoxycephalosporanic acid. Its isoelecti point was determined by the electrophoretic method. Potentiometric titration of zwitterion of 7-ADCA was performed and the constants of its ionization were calculated. Minimum solubility of 7-ADCA zwitterion was determined and the curve of 7-ADCA solubility at wide pH ranges was estimated. Equilibrium of 3 forms of 7-ADCA was estimated.     

Evaluation of the performance of immobilized penicillin G acylase using active-site titration

Penicillin G acylase from Escherichia coli was immobilized on Eupergit C with different enzyme loading. The activity of the immobilized preparations was assayed in the hydrolysis of penicillin G and was found to be much lower than would be expected on the basis of the residual enzyme activity in the immobilization supernatant. Active-site titration demonstrated that the immobilized enzyme molecules on average had turnover rates much lower than that of the dissolved enzyme. This was attributed to diffusion limitations of substrate and product inhibition. Indeed, when the immobilized preparations were crushed, the activity increased from 587 U g-1 to up to 974 U g-1. The immobilized preparations exhibited up to 15% lower turnover rates than the dissolved enzyme in cephalexin synthesis from 7-ADCA and D-(-)-phenylglycine amide. The synthesis over hydrolysis ratios of the immobilized preparations were also much lower than that of the dissolved enzyme. This was partly due to diffusion limitations but also to an intrinsic property of the immobilized enzyme because the synthesis over hydrolysis ratio of the crushed preparations was much lower than that of the dissolved enzyme.     

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.     

Kinetic modeling analysis of maleic acid-catalyzed hemicellulose hydrolysis in corn stover

Maleic acid-catalyzed hemicellulose hydrolysis reaction in corn stover was analyzed by kinetic modeling. Kinetic constants for Saeman and biphasic hydrolysis models were analyzed by an Arrhenius-type expansion which include activation energy and catalyst concentration factors. The activation energy for hemicellulose hydrolysis by maleic acid was determined to be 83.3 +/- 10.3 kJ/mol, which is significantly lower than the reported E(a) values for sulfuric acid catalyzed hemicellulose hydrolysis reaction. Model analysis suggest that increasing maleic acid concentrations from 0.05 to 0.2 M facilitate improvement in xylose yields from 40% to 85%, while the extent of improvement flattens to near-quantitative by increasing catalyst loading from 0.2 to 1 M. The model was confirmed for the hydrolysis of corn stover at 1 M maleic acid concentrations at 150 degrees C, resulting in a xylose yield of 96% of theoretical. The refined Saeman model was used to evaluate the optimal condition for monomeric xylose yield in the maleic acid-catalyzed reaction: low temperature reaction conditions were suggested, however, experimental results indicated that bi-phasic behavior dominated at low temperatures, which may be due to the insufficient removal of acetyl groups. A combination of experimental data and model analysis suggests that around 80-90% xylose yields can be achieved at reaction temperatures between 100 and 150 degrees C with 0.2 M maleic acid.     

Kinetically controlled synthesis of ampicillin with immobilized penicillin acylase in the presence of organic cosolvents

Penicillin acylase (PA) is used in the industrial production of 6-amino penicillanic acid (6-APA). However, by proper control of reaction medium, the enzyme can be used in the reverse synthesis of β-lactam antibiotics from the corresponding β-lactam nuclei and suitable acyl donors. Under thermodynamically controlled strategy, the use of organic cosolvents can favor synthesis over hydrolysis by lowering water activity and favoring the non-ionic reactive species. Under kinetically controlled strategy using activated acyl donors, organic solvents can favor synthesis by depressing hydrolytic reactions. Results are presented on the synthesis of ampicillin from phenylglycine methyl ester and 6-APA with immobilized Escherichia coli PA in the presence of organic cosolvents. Several solvents were tested in terms of enzyme stability and solubility of substrates. Ethylene glycol, glycerol, 1–2 propanediol and 1–3 butanediol were selected accordingly and ampicillin synthesis was performed in all of them. Best results in terms of yield and productivity were obtained with ethylene glycol, with which further studies were conducted. Variables studied were enzyme to limiting substrate ratio, acyl acceptor to acyl donor ratio, organic solvent concentration, pH and temperature. Experimental design based on a two-level fractional factorial design was conducted. pH was determined as the most sensitive variable and was further optimized. The best conditions for ampicillin synthesis in terms of productivity, within the range of values studied for those variables, were pH 7.4, 28°C, 36 U_S PA/mmol 6-APA, 3 mol PGME/mol 6-APA and 45 % (v/v) ethylene glycol concentration. Productivity was 7.66 mM ampicillin/h, which corresponds to a specific productivity of 7.02 μmol ampicillin/h U_S at 55 % yield. Productivity was lower than in buffer but product yield was higher because of the much lower relative hydrolysis rates.