Single-pot conversion of cephalosporin C to 7-aminocephalosporanic acid in the absence of hydrogen peroxide

In this study, d-amino acid oxidase (DAAO) and catalase (CAT) in the permeabilized recombinant Pichia pastori cells were well investigated. It appeared that their thermal stability was negatively correlated with the apparent enzymatic activities. The frozen-melted cells presented the best stability and the lowest apparent activities of DAAO and CAT, whereas the cetyltrimethylammonium bromide (CTAB) permeabilized cells displayed the weakest stability and the highest apparent activities of the two enzymes. Simultaneous action of DAAO and CAT in the CTAB-permeabilized cells and glutaryl-7-aminocephalosporanic acid acylase (GA) immobilized on carrier contributed to the conversion of cephalosporin C (CPC) to 7-aminocephalosporanic acid (7-ACA) with a yield of 76.2%. During such a reaction cycle, no visible activity loss occurred at the immobilized GA, whereas the loss rates of DAAO and CAT activities were about 0.029 and 1.13 U min⁻¹, respectively. Nevertheless, this problem could be easily solved by continuous feeding of the new permeabilized cell suspension at the rate of 6 ml h⁻¹ to the reactor. Following such a fed-batch strategy, these permeabilized cells and the immobilized GA could be efficiently reused for 6 and 15 reaction cycles, respectively, yielding around 76% 7-ACA at each reaction cycle.     

Two-step immobilized enzyme conversion of cephalosporin C to 7-aminocephalosporanic acid

The first large-scale production of 7-aminocephalosporanic acid (7ACA) from cephalosporin C (CPC) using a wholly enzymatic synthesis method is reported here. We produced 7ACA from CPC in as high a molar yield as 85% using the immobilized enzymes D-amino acid oxidase (D-AOD) and glutaryl-7-ACA acylase (GL-acylase). In the first reactor, CPC is converted to keto-adipyl-7-aminocephalosporanic acid (keto-7ACA) using an immobilized D-AOD isolated from a yeast, Trigonopsis variabilis. The keto-7ACA is then spontaneously converted to glutaryl-7-aminocephalosporanic acid (GL-7ACA) via a chemical reaction with hydrogen peroxide. The hydrogen peroxide is also a product of the D-AOD reaction. Near quantitative conversion of the keto-7ACA to GL-7ACA was observed. The second reactor converts GL-7ACA to 7ACA using an immobilized GL-acylase, which was isolated from a reconbinant Escherichia coli. The final 7ACA crystalline product is a high quality product. The reactions are conducted under very mild aqueous conditions: pH 8.0 and 20 degrees to 25 degrees C. The production of desacetyl side products is minimal. This process is currently being implemented on an industrial scale to produce 7ACA. (c) 1995 John Wiley & Sons, Inc.     

Fusion protein of Vitreoscilla hemoglobin with D-amino acid oxidase enhances activity and stability of biocatalyst in the bioconversion process of cephalosporin C

In this study we constructed an artificial flavohemoprotein by fusing Vitreoscilla hemoglobin (VHb) with D-amino acid oxidase (DAO) of Rhodotorula gracilis to determine whether bacterial hemoglobin can be used as an oxygen donor to immobilized flavoenzyme. This chimeric enzyme significantly enhanced DAO activity and stability in the bioconversion process of cephalosporin C. In a 200-mL bioreactor, the catalytic efficiency of immobilized VHb-DAO against cephalosporin C was 12.5-fold higher than that of immobilized DAO, and the operational stability of the immobilized VHb-DAO was approximately threefold better than that of the immobilized DAO. In the scaled-up bioprocess with a 5-L bioreactor, immobilized VHb-DAO (2500 U/L) resulted in 99% bioconversion of 120 mM cephalosporin C within 60 min at an oxygen flow rate of 0.2 (v/v) x min. Ninety percent of the initial activity of immobilized VHb-DAO could be maintained at up to 50 cycles of the enzymatic reaction without exogenous addition of H(2)O(2) and flavin adenine dinucleotide (FAD). The purity of the final product, glutaryl-7-aminocephalosporanic acid, was confirmed to be 99.77% by high-performance liquid chromatography (HPLC) analysis. Relative specificity of immobilized VHb-DAO on D-alpha-aminoadipic acid, a precursor in cephalosporin C biosynthesis, increased twofold, compared with that of immobilized DAO, suggesting that conformational modification of the VHb-DAO fusion protein may be altered in favor of cephalosporin C.     

Interaction between 1,4-thiazine derivatives and D-amino-acid oxidase

Aminoethylcysteine-ketimine (2H-1,4-thiazine-5,6-dihydro-3-carboxylic acid) strongly inhibits D-amino-acid oxidase (D-amino-acid:oxygen oxidoreductase (deaminating), EC 1.4.3.3). The inhibition is purely competitive (Ki = 3.3 X 10(-7) M). Aminoethylcysteine-ketimine modifies the visible spectrum of the enzyme: the absorption maxima of bound FAD shift from 375-455 nm to 385-445 nm with a definite shoulder at 465 nm; the appearance of a large absorption band centered at 750 nm may be due to a charge-transfer complex formation. The dissociation constant for the aminoethylcysteine-ketimine-enzyme complex, calculated by a photometric procedure (4 X 10(-7) M), is in good agreement with kinetic data. The dicarboxylic analogue of this inhibitor (lanthionine-ketimine) is ineffective in D-amino-acid oxidase inhibition and does not produce any spectral modification of the enzyme. These results confirm structural requirements for D-amino-acid oxidase inhibitor reported by other researchers. Ketimine reduced forms (thiomorpholine-2-carboxylic acid and thiomorpholine-2,6-dicarboxylic acid) are chemically synthesized and checked as D-amino-acid oxidase substrates: only thiomorpholine-2-carboxylic acid is oxidized to aminoethylcysteine-ketimine (Km = 2 X 10(-4) M).     

Renaturation studies of free and immobilized D-amino-acid oxidase

The renaturation of free and Sepharose-immobilized D-amino-acid oxidase (D-amino-acid:oxygen oxidoreductase (deaminating), EC 1.4.3.3), after its denaturation with 6 M guanidine hydrochloride, was investigated. No reactivation, or extremely limited reactivation (less than or equal to 4+), was obtained with the free enzyme, is spite of various attempts including the use of dialysis or buffers containing cofactors, different types of anions, surfactants and low concentrations of denaturing agents. The main obstacle to renaturation appeared to be the interaction among denatured or partially renatured monomers giving rise to inactive aggregates. In contrast, using the immobilized enzyme approach, substantial renaturation (up to 50%) of D-amino-acid oxidase was achieved. The denaturation-renaturation process was followed by monitoring the catalytic activity as well as the intrinsic protein fluorescence. An inverse correlation was found to exist between the degree of matrix activation by CNBr and the yield of enzyme reactivation. The anions of the lyotropic series markedly influenced the reactivation, showing an effectiveness opposite to their salting-out potential (thiocyanate congruent to iodide greater than chloride greater than phosphate congruent to sulphate congruent to citrate). Instead, the anions considerably increased the activity and stability of free and immobilized enzyme, according to their salting-out potential. Immobilized monomers of D-amino-acid oxidase, which in solution undergoes self-association, showed poor capacity to interact with the free enzyme: thus they appear unsuitable for analytical and preparative purposes.     

Construction of an acetylcholinesterase-choline oxidase biosensor for aldicarb determination

In this study, acetylcholinesterase and choline oxidase were co-immobilized on poly(2-hydroxyethyl methacrylate) membranes and the change in oxygen consumption upon aldicarb introduction was measured. Immobilization of the enzymes was achieved either by entrapment or by surface attachment via a hybrid immobilization method including epichlorohydrin and Cibacron Blue F36A activation. Immobilized enzymes had a long-storage stability (only 15% activity decrease in 2 months in wet storage and no activity loss in dry storage). Aldicarb detection studies showed that a linear working range of 10-500 and 10-250 ppb aldicarb could be achieved by entrapped and surface immobilized enzymes, respectively. Enzymes immobilized on membrane surfaces responded to aldicarb presence more quickly than entrapped enzymes. Aldicarb concentrations as low as 23 and 12 ppb could be detected by entrapped and surface immobilized enzymes, respectively, in 25 min.     

Catalytic properties of D-amino acid oxidase in cephalosporin C bioconversion: a comparison between proteins from different sources

Lacking an efficient process to produce 7-aminocephalosporanic acid from cephalosporin C in a single step, d-amino acid oxidase (DAAO) is of foremost importance in the industrial, two-step process used for this purpose. We report a detailed study on the catalytic properties of the three available DAAOs, namely, a mammalian DAAO and two others from yeast (Rhodotorula gracilis and Trigonopsis variabilis). In comparing the kinetic parameters determined for the three DAAOs, with both cephalosporin C and d-alanine as substrate, the catalytic efficiency of the two enzymes from microorganism is at least 2 orders of magnitude higher than that of pig kidney DAAO. Furthermore, the mammalian enzyme is more sensitive to product inhibition (from hydrogen peroxide and glutaryl-7-aminocephalosporanic acid). Therefore, enzymes from microorganisms appear to be by far more suitable catalysts for bioconversion, although some different minor differences are present between them (e.g., a higher activity of the R. gracilis enzyme when the bioconversion is carried out at saturating oxygen concentration). The mammalian DAAO, even being a poor catalyst, is more stable with respect to temperature than the R. gracilis enzyme in the free form. In any case, for industrial purposes DAAO is used only in the immobilized form where a strong enzyme stabilization occurs.     

The Application of Chemiluminescence of a Cypridina Luciferin Analog to Immobilized Enzyme Sensors

Chemiluminescence of a Cypridina luciferin analog, 2-methyl-6-phenyl-3,7-dihydro-imidazo[l,2-a]pyrazin-3-one, was applied to immobilized enzyme sensors. Xanthine oxidase, peroxidase, glucose oxidase, uricase and cholesterol oxidase were immobilized by using photo-crosslinkable resin prepolymer or ion-exchangeable cellulose beads. The immobilized enzyme sensor system was composed of a photoncounter and a test tube in which the immobilized enzyme membrane or particles were placed. A linear relation between the concentration of substrates and luminescence rate was obtained on a logarithmic scale. This immobilized enzyme sensor system could be used repeatedly. Hydrogen peroxide, xanthine and hypoxanthine were measured sensitively and rapidly within 100 sec. Glucose, cholesterol and uric acid were measured sensitively within 10 min but could be measured within 100 sec, although less sensitive. The detection limits for xanthine, hypoxanthine, hydrogen peroxide, glucose, cholesterol and uric acid were 0.02, 0.02, 0.2, 0.4, 2 and 2 μM, respectively. Concentrations of hypoxanthine in tuna muscle, and glucose and cholesterol in serum measured using this sensor system were comparable with those measured by the standard methods.     

Batch production of deacetyl 7-aminocephalosporanic acid by immobilized cephalosporin-C deacetylase

Bacillus subtilis SHS0133 cephalosporin-C deacetylase (CAH) overexpressed in Escherichia coli was immobilized on an anion-exchange resin, KA-890, using glutaraldehyde. The activity yield of immobilized enzyme was approximately 55% of the free enzyme. The pH range for stability of the immobilized enzyme (pH 5–10) was broader than that for free enzyme. The K_m^app value of immobilized enzyme for 7-aminocephalosporanic acid (7-ACA) was similar to that of the free enzyme. This immobilized enzyme obeyed Michaelis–Menten kinetics similar to those of the free enzyme. A batch-type reactor with a water jacket was employed for deacetylation of 7-ACA using CAH immobilized on KA-890. Ten kilograms of 7-ACA were completely converted to deacetyl 7-ACA at pH 8.0 within 90 min. The reaction kinetics agreed well with a computer simulation model. Moreover, the immobilized enzyme exhibited only a slight loss of the initial activity even after repeated use (52 times ) over a period of 70 days. This reaction will thus be useful for the production of cephalosporin-type antibiotics.     

Immobilization of -glucose oxidase onto a hydrogen peroxide permselective membrane and application for an enzyme electrode

A hydrogen peroxide permselective membrane with asymmetric structure was prepared and -glucose oxidase (EC 1.1.3.4) was immobilized onto the porous layer. The activity of the immobilized -glucose oxidase membrane was 0.34 units cm⁻² and the activity yield was 6.8% of that of the native enzyme. Optimum pH, optimum temperature, pH stability and temperature stability were found to be pH 5.0, 30–40°C, pH 4.0–7.0 and below 55°C, respectively. The apparent Michaelis constant of the immobilized -glucose oxidase membrane was 1.6 × 10⁻³ mol l⁻¹ and that of free enzyme was 4.8 × 10⁻² mol l⁻¹. An enzyme electrode was constructed by combination of a hydrogen peroxide electrode with the immobilized -glucose oxidase membrane. The enzyme electrode responded linearly to -glucose over the concentration 0–1000 mg dl⁻¹ within 10 s. When the enzyme electrode was applied to the determination of -glucose in human serum, within day precision (CV) was 1.29% for -glucose concentration with a mean value of 106.8 mg dl⁻¹. The correlation coefficient between the enzyme electrode method and the conventional colorimetric method using a free enzyme was 0.984. The immobilized -glucose oxidase membrane was sufficiently stable to perform 1000 assays (2 to 4 weeks operation) for the determination of -glucose in human whole blood. The dried membrane retained 77% of its initial activity after storage at 4°C for 16 months.     

Characterization of an industrial biocatalyst: immobilized glutaryl-7-ACA acylase

A batch of the immobilized industrial biocatalyst glutaryl-7-ACA acylase (GA), one of the two enzymes involved in the biotransformation of cephalosporin C (CefC) into 7-aminocephalosporanic acid (7-ACA), was characterized. K(m) value for glutaryl-7-ACA was 5 mM. Enzyme activity was found to be optimal at pH between 7 and 9.5 and to increase with temperature and in buffered solutions. To avoid product degradation, optimal reaction conditions were obtained working at 25 degrees C using a 50-mM phosphate buffer, pH 8.0. Immobilized GA showed good stability at pH value below 9 and at temperature up to 30 degrees C. The inactivation of immobilized GA in the presence of different amounts of H(2)O(2), a side product that might be present in the plant-scale industrial solutions of glutaryl-7-ACA, was also investigated, but the deactivation rates were negligible at H(2)O(2) concentration that might be reached under operative conditions. Finally, biocatalyst performance in the complete two-step enzymatic conversion process from CefC to 7-ACA was determined on a laboratory scale. Following the complete conversion of a 75 mM solution of CefC into glutaryl-7-ACA catalyzed by an immobilized D-amino acid oxidase (DAAO), immobilized GA was used for the transformation of this intermediate into the final product 7-ACA. This reaction was repeated for 42 cycles. An estimation of the residual activity of the biocatalyst showed that 50% inactivation of immobilized GA was reached after approximately 300 cycles, corresponding to an enzyme consumption of 0.4 kU per kg of isolated 7-ACA.     

Physical Properties and Kinetic Behavior of a Cephalosporin Acetylesterase Produced by Bacillus subtilis

An esterase that deacetylates cephalosporins was recovered from the supernatant of a Bacillus subtilis culture. It was partially purified by ammonium sulfate fractionation and ultrafiltration. The enzyme had a temperature optimum between 40 and 50 C and a pH optimum of 7.0. The molecular weight was estimated by gel filtration to be 190,000. The enzyme was very stable and retained greater than 80% of its activity after storage in solution at 25 C for 1 month. The esterase exhibited Michaelis-Menton kinetics with the substrates 7-aminocephalosporanic acid (7-ACA) and 7-(thiophene-2-acetamido)cephalosporanic acid (cephalothin); the K(m) values were 2.8 X 10(-3) and 8.3 X 10(-3) M, respectively. The products of 7-ACA deacetylation were weak competitive inhibitors, and a K(i) value of 5.0 X 10(-2) M was determined for acetate and of 3.6 X 10-2 M for deacetyl-7-ACA. Weak product inhibition did not prevent the deacetylation reaction from going to completion. A 5-mg/ml solution of partially purified esterase completely hydrolyzed (greater than 99.5%) a 24-mg/ml solution of 7-ACA in 3 h. Because of the kinetic properties and excellent stability, this enzyme may be useful in an immobilized form to prepare large quantities of deacetylated cephalosporin derivatives.     

Immobilization of d-glucose oxidase onto a hydrogen peroxide permselective membrane and application for an enzyme electrode

A hydrogen peroxide permselective membrane with asymmetric structure was prepared and d-glucose oxidase (EC 1.1.3.4) was immobilized onto the porous layer. The activity of the immobilized d-glucose oxidase membrane was 0.34 units cm^?2 and the activity yield was 6.8% of that of the native enzyme. Optimum pH, optimum temperature, pH stability and temperature stability were found to be pH 5.0, 30–40°C, pH 4.0–7.0 and below 55°C, respectively. The apparent Michaelis constant of the immobilized d-glucose oxidase membrane was 1.6 × 10^?3 mol l^?1 and that of free enzyme was 4.8 × 10^?2 mol l^?1. An enzyme electrode was constructed by combination of a hydrogen peroxide electrode with the immobilized d-glucose oxidase membrane. The enzyme electrode responded linearly to d-glucose over the concentration 0–1000 mg dl^?1 within 10 s. When the enzyme electrode was applied to the determination of d-glucose in human serum, within day precision (CV) was 1.29% for d-glucose concentration with a mean value of 106.8 mg dl^?1. The correlation coefficient between the enzyme electrode method and the conventional colorimetric method using a free enzyme was 0.984. The immobilized d-glucose oxidase membrane was sufficiently stable to perform 1000 assays (2 to 4 weeks operation) for the determination of d-glucose in human whole blood. The dried membrane retained 77% of its initial activity after storage at 4°C for 16 months.     

Steady-state generation of hydrogen peroxide: kinetics and stability of alcohol oxidase immobilized on nanoporous alumina

Alcohol oxidase from Pichia pastoris was immobilized on nanoporous aluminium oxide membranes by silanization and activation by carbonyldiimidazole to create a flow-through enzyme reactor. Kinetic analysis of the hydrogen peroxide generation was carried out for a number of alcohols using a subsequent reaction with horseradish peroxidase and ABTS. The activity data for the immobilized enzyme showed a general similarity with literature data in solution, and the reactor could generate 80 mmol H₂O₂/h per litre reactor volume. Horseradish peroxidase was immobilized by the same technique to construct bienzymatic modular reactors. These were used in both single pass mode and circulating mode. Pulsed injections of methanol resulted in a linear relation between response and concentration, allowing quantitative concentration measurement. The immobilized alcohol oxidase retained 58 % of initial activity after 3 weeks of storage and repeated use.     

Enzymatic conversion of cephalosporin C into glutaryl 7-aminocephalosporanic acid. A study in different reactor configurations

Conversion of cephalosporin C into glutaryl 7-aminocephalosporanic acid was catalysed by D-aminoacid oxidase from Trigonopsis variabilis, covalently immobilized on the polystyrenic resin Duolite A365. Spontaneous degradation of substrates was limited without depressing enzymatic activity at the optimum reaction pH 8.0. The highest product yield was 1.77 mmol per g of biocatalyst, attained at 15¡C in both batch stirred and fluidized-bed reactors.     

A simple purification procedure of D-amino-acid oxidase from <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

D-amino-acid oxidase (EC 1.4.3.3) was purified about 1480-fold from the yeast Candida guilliermondii using chromatofocusing method. The purification procedure gave an enzyme preparation which is greater than 90% homogenous on SDS-polyacrylamide gels with a specific activity of 11.54 U/mg at 30°C with D-proline as substrate with the yield of total activity 9.3%. The molecular weights of subunit and native enzyme were determined to be 38.4 and 78.6 kDa by SDS-polyacrylamide gel electrophoresis and gel-filtration, respectively, suggesting that the native enzyme exists as a homodimer. A single molecular form with an isoelectric point of 6.85 was detected in analytical isoelectrofocusing. The optimum pH and temperature were 8.0 and 33°C. An enzyme shows stability in the pH range from 7.4 to 9.0 and at the temperature no higher than 38°C. Activation energy for D-amino-acid oxidase reaction was calculated to be 60 kJ/mol at 30°C. The strict D-isomer specificity of the enzyme is confirmed, since no reaction could be detected with L-amino acids, and a large number of D-amino acids could be substrates for this enzyme. K _m and V _max values were determined for D-proline and D-alanine, which, among 22 tested, were the best substrates of the enzyme. D-amino-acid oxidase from the yeast C. guilliermondii is a flavoprotein oxidase in which the prosthetic group is tightly, but not covalently, bound FAD. The enzyme is completely inhibited by sodium benzoate, SH-oxidizing agents, but not by sodium azide, toluene or chloroform.     

三角酵母整细胞酶促转化头孢菌素C为戊二酰—7—氨基头孢烷酸

研究了利用含D－氨基酸氧化酶(D-amino acid oxidase,DAO EC1.4.3.3）的透性化三角酶母多倍体FA10（Trigonopsis variabilis FA10）细胞酶促转化头孢菌素C（cephalosporin C,CPC）为戊二酰－7－氨基头孢烷酸（Glutaryl-7-ACA,GL-7ACA）的反应过程和细胞中同时存在的过氧化氢酶（Catalase,CAT）通过水解H2O2而对转化反应产生的干扰作用及其对策。实验证明适量添加外源H2O2（6％）或在反应体系中加入过氧化氢酶抑制剂NaN3(0.13mg/mL )可使GL－7ACA生成率分别为73.0％和70.1％。如果将透性化的FA10细胞在pH10.5-11.0,20℃条件下保温30min,CAT被不可逆性完全钝化,以无过氧化氢酶的FA10细胞进行CPC的酶促转化反应GL－7ACA的生成率可达84％。     

Immobilization of Brevibacterium flavum with carrageenan and its application for continuous production of l-malic acid

Extensive experiments were carried out to improve the productivity ofl-malic acid from fumaric acid using Brevibacterium flavum immobilized with carrageenan. The most favourable preparation for the continuous production ofl-malic acid was obtained when 16 g of B. flavum cells was entrapped in 100 ml 3.4% carrageenan gel. However, the immobilized cells produced an unwanted by-product, succinic acid. Treatment of the immobilized cells with 0.6% bile extract suppressed the side reaction and gave the highest operational stability of fumarase activity. By the immobilization of intact cells, the optimal temperature of the enzyme reaction shifted to 10°C higher, the optimal pH became broader, and the operational stability of fumarase activity increased. The effect of temperature on the stability of fumarase activity in the immobilized cell column was investigated under conditions of continuous enzyme reaction. The decay of fumarase activity during continuous enzyme reaction was expressed by an exponential relationship. The productivity of the immobilized B. flavum using carrageenan was as high as 5.2 times that of the conventional immobilized B. ammoniagenes using polyacrylamide.     

Entrapment of lipase into K-carrageenan beads and its use in hydrolysis of olive oil in biphasic system

The porcine pancrease lipase was immobilized by entrapment in the beads of K-carrageenan and cured by treatment with polyethyleneimine (PEI) in the phosphate buffer. The retention of hydrolytic activity of lipase and compressive strength of the beads were examined. The activity of free and immobilized lipase was assessed by using olive oil as the substrate. The immobilized enzyme exhibited a little shift towards acidic pH for its optimal activity and retained 50% of its activity after 5 cycles. When the enzyme concentration was kept constant and substrate concentration was varied the K_m and V_max were observed to be 0.18 × 10⁻² and 0.10, and 0.10 × 10⁻² and 0.09 respectively, for free and for entrapped enzymes. When the substrate concentration was kept constant and enzyme concentration was varied, the values of K_m and V_max were observed to be 0.19 × 10⁻⁷ and 0.41, and 0.18 × 10⁻⁷ and 0.41 for free and entrapped enzymes. Though this indicates that there is no conformational change during immobilization, it also shows that the reaction velocity depends on the concentration. Immobilized enzyme showed improved thermal and storage stability. Hydrolysis of olive oil in organic–aqueous two-phase system using fixed bed reactor was carried out and conditions were optimized. The enzyme in reactor retained 30% of its initial activity after 480 min (12 cycles).     

Study of an enzyme membrane reactor with immobilized fumarase for production of L-malic acid

The conversion of fumaric acid into L-malic acid by fumarase immobilized in a membrane reactor was analyzed experimentally. The enzyme was entrapped in asymmetric capillary membranes made of polysulfone. The performance of the reactor was evaluated in terms of conversion degree, reaction rate, and stability. The influence of operating conditions, such as amount of immobilized enzyme, substrate concentration, residence time, and axial flow rate, were investigated. The kinetic parameters K(m), V(max), and k(+2) were also measured. The stability of the immobilized enzyme was very good, showing no activity decay during more than 2 weeks of continuous operation.