Characteristic of immobilized cephalosporin C acylase and its application in one-step enzymatic conversion of cephalosporin C to 7-aminocephalosporanic acid

Cephalosporin C (CPC) acylase is an enzyme which hydrolyzes CPC to 7-aminocephalosporanic acid (7-ACA) directly, and therefore has great potential in industrial application. In this study, the CPC acylase from a recombinant Escherichia coli was purified to high purity by immobilized metal affinity chromatography, and the CPC acylase was covalently attached to three kinds of epoxy supports, BB-2, ES-V-1 and LX-1000EP. The immobilized CPC acylase with LX-1000EP as the support shows the highest activity (81 U g⁻¹) suggesting its potential in industrial 7-ACA production. The activity of immobilized enzyme was found to be optimal at pH between 8.5 and 9.5 and to increase with temperature elevation until 55 °C. Immobilized CPC acylase showed good stability at pH between 8.0 and 9.5 and at temperature up to 40 °C. To avoid product degradation, the production of 7-ACA utilizing immobilized enzyme was carried out at 25 °C, pH 8.5 in a designed reactor. Under optimal reaction conditions, a very high 7-ACA yield of 96.7% was obtained within 60 min. In the results of repeated batch production of 7-ACA, 50% activity of the initial cycle was maintained after being recycled 24 times and the average conversion rate of CPC reached 98%.     

Chitosan–SiO2–multiwall carbon nanotubes nanocomposite: A novel matrix for the immobilization of creatine amidinohydrolase

A matrix made up of chitosan–SiO₂–multiwall carbon nanotubes (CHIT–SiO₂–MWCNTs) nanocomposite was fabricated to investigate the immobilization of creatine amidinohydrolase (CAH). CAH enzyme was covalently immobilized with the CHIT–SiO₂–MWCNTs matrix using glutaraldehyde as a linker. The resulting CAH/CHIT–SiO₂–MWCNTs biomatrix was characterized with Fourier transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM) and cyclic voltammetry (CV) taking CHIT–SiO₂–MWNTs as a reference. The influence of various parameters on CAH enzyme activity within the matrix was investigated including pH, temperature, and time. The Michaelis–Menten constant and apparent activities for the CAH enzyme were calculated to be 0.58 mM and 83.16 mg/cm², respectively; indicating CHIT–SiO₂–MWCNTs nanocomposite matrix has a high affinity to immobilize CAH enzyme.     

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.     

Inversion of sucrose with β- -fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose: Batch process

The inversion of sucrose with β- -fructofuranosidase (EC 3.2.1.26) immobilized by an ionic bond on bead cellulose containing weak basic N,N-diethylamino-2-hydroxypropyl groups has been investigated. The immobilized enzyme is strongly bound at an ionic strength up to 0.1 M in the pH range 3–6. The amount adsorbed is proportional to porosity and to the exchange capacity of the ion exchange cellulose, reaching values up to 200 mg/g dry carrier, with an activity in 10% sucrose solution at 30°C, pH 5, >8000 μmol min⁻¹ g⁻¹. The inversion of sucrose with immobilized β- -fructofuranosidase was carried out in a stirred reactor. The dependence of activity on pH (3–7), temperature (0–70°C) and concentration of the substrate (2–64 wt%) were determined, and the inversion was compared with that obtained using non-immobilized enzyme under similar conditions. The rate of inversion at low substrate concentration (2–19 wt%) was described by Michaelis-Menten kinetics.     

Catalytic properties of the immobilized Aspergillus tamarii xylanase

Xylanase from Aspergillus tamarii was covalently immobilized on Duolite A147 pretreated with the bifunctional agent glutaraldehyde. The bound enzyme retained 54.2% of the original specific activity exhibited by the free enzyme (120 U/mg protein). Compared to the free enzyme, the immobilized enzyme exhibited lower optimum pH, higher optimum reaction temperature, lower energy of activation, higher K_m (Michaelis constant), lower V_max (maximal reaction rate). The half-life for the free enzyme was 186.0, 93.0, and 50.0 min for 40, 50, and 60°C, respectively, whereas the immobilized form at the same temperatures had half-life of 320, 136, and 65 min. The deactivation rate constant at 60°C for the immobilized enzyme is about 6.0 × 10⁻³, which is lower than that of the free enzyme (7.77 × 10⁻³ min). The energy of thermal deactivation was 15.22 and 20.72 kcal/mol, respectively for the free and immobilized enzyme, confirming stabilization by immobilization. An external mass transfer resistance was identified with the immobilization carrier (Duolite A147). The effect of some metal ions on the activity of the free and immobilized xylanase has been investigated. The immobilized enzyme retained about 73.0% of the initial catalytic activity even after being used 8 cycles.     

Immobilization of a cephalosporin acetylesterase by containment within an ultrafiltration device

A cephalosporin acetylesterase produced by Bacillus subtilis catalyzes the deacetylation of 7-aminocephalosporanic acid (7-ACA). Previous reports from our laboratory described the kinetic constants that characterize the reaction: K_m = 2.8 × 10^?3M, K_ia acetate = 5 × 10^?2M, and K_id deacetyl-7-ACA = 3.6 × 10^?2M. These constants were used to predict the time course of the reaction using the following equation for dual competitive product inhibition. where S_t = mg/ml 7-ACA, A_t = mg/ml acetate, D_t = mg/ml deacetyl-7-ACA. The predicted time course closely matched the time course measured experimentally. The equation also was solved without the inhibition terms and the solution indicated that product inhibition caused about a 30% increase in the time required for complete (>97%) hydrolysis of a 24 mg/ml 7-ACA solution. The esterase was immobilized by containment within an ultrafiltration device. With this technique the enzyme was reused 20 times over an 11 day span to deacetylate 7-ACA solutions containing 4 to 24 mg/ml 7-ACA. The specific activity after the 20th use was the same as the activity prior to the first use, indicating little enzyme inactivation occurred.     

A process for bioconversion of cephalosporin C by Rhodotorula gracilis D-amino acid oxidase

Summary A process for the production (in a stirred tank reactor) of glutaryl-7-ACA from cephalosporin C using immobilized D-amino acid oxidase is described. Results so obtained under optimal conditions (1.2 mg coupled enzyme/L, pH 8.5, 2 mM cephalosporin C) point to a system which shows high conversion efficiency and a remarkable operational stability. No exogenous H₂O₂ is requested to shift the reaction equilibrium toward glutaryl-7-ACA production, nor any side product is detected. The immobilized system productivity was 54 g/day/mg of enzyme. This process represents the first reported case of a reactor successfully developed with a DAAO for bioconversion of cephalosporin C.     

Catalytic properties of the immobilized Talaromyces thermophilus β-xylosidase and its use for xylose and xylooligosaccharides production

The present study explores the efficiency of Talaromyces thermophilus β-xylosidase, in the production of xylose and xylooligosaccharides. The β-xylosidase was immobilized by different methods namely ionic binding, entrapment and covalent coupling and using various carriers. Chitosan, pre-treated with glutaraldehyde, was selected as the best support material for β-xylosidase immobilization; it gave the highest immobilization and activity yields (94%, 87%, respectively) of initial activity, and also provided the highest stability, retaining 94% of its initial activity even after being recycled 25 times. Shifts in the optimal temperature and pH were observed for the immobilized β-xylosidase when compared to the free enzyme. The maximal activity obtained for the immobilized enzyme was achieved at pH 8.0 and 53 °C, whereas that for the free enzyme was obtained at pH 7.0 and 50 °C. The immobilized enzyme was more thermostable than the free β-xylosidase. We observed an increase of the K_m values of the free enzyme from 2.37 to 3.42 mM at the immobilized state. Native and immobilized β-xylosidase were found to be stimulated by Ca²⁺, Mn²⁺ and Co²⁺ and to be inhibited by Zn²⁺, Cu²⁺, Hg²⁺, Fe²⁺, EDTA and SDS. Immobilized enzyme was found to catalyze the reverse hydrolysis reaction, forming xylooligosaccharides in the presence of a high concentration of xylose. In order to examine the synergistic action of xylanase and β-xylosidase of T. thermophilus, these two enzymes were co-immobilized on chitosan. A continuous hydrolysis of 3% Oat spelt xylan at 50 °C was performed and better hydrolysis yields and higher amount of xylose was obtained.     

Kinetic and thermodynamic properties of purified alkaline protease from Bacillus pumilus Y7 and non‐covalent immobilization to poly(vinylimidazole)/clay hydrogel

The characterization of the hydrogel was performed using Fourier‐transform infrared spectroscopy, X‐ray diffraction, and scanning electron microscopy. Purified Bacillus pumilus Y7‐derived alkaline protease was immobilized in Poly (vinylimidazole)/clay (PVI/SEP) hydrogel with 95% yield of immobilization. Immobilization decreased the pH optimum from 9 to 6 for free and immobilized enzyme, respectively. Temperature optimum 3°C decreased for immobilized enzyme. The K_m, V_m, and k_cat of immobilized enzyme were 4.4, 1.7, and 7.5‐fold increased over its free counterpart. Immobilized protease retained about 65% residual activity for 16^th reuse. The immobilized protease endured its 35% residual activity in the material after six cycle's batch applications. The results of thermodynamic analysis for casein hydrolysis showed that the ΔG^≠ (activation free energy) and ΔG^≠_E‐T (activation free energy of transition state formation) obtained for the immobilized enzyme decreased in comparison to those obtained for the free enzyme. On the other hand, the value of ΔG^≠_ES (free energy of substrate binding) was observed to have increased. These results indicate an increase in the spontaneity of the biochemical reaction post immobilization. Enthalpy value of immobilized enzyme that was 2.2‐fold increased over the free enzyme indicated lower energy for the formation of the transition state, and increased ΔS^≠ value implied that the immobilized form of the enzyme was more ordered than its free form.     

Cloning and high expression of glutaryl 7-aminocephalosporanic acid acylase gene from Pseudomonas diminuta

The gene coding for the glutaryl 7-aminocephalosporanic acid (GL 7-ACA) acylase from Pseudomonas diminuta KAC-1 was cloned and expressed in Escherichia coli. The acylase gene was composed of 2160 base pairs and encoded a polypeptide of 720 amino acid residues. The E. coli BL21 carrying pET2, the plasmid construct for high expression of GL 7-ACA acylase gene, produced this enzyme at approx. 30% of the total proteins with 3.2 units activity mg protein^–1. Growth at temperature below 31 °C and deletion of signal peptide increased the processing of precursor acylase to active enzyme in the recombinant E. coli cells.     

Silanized palygorskite for lipase immobilization

Lipase from Candida lipolytica has been immobilized on 3-aminopropyltriethoxysilane-modified palygorskite support. Scanning electron micrographs proved the covalently immobilization of C. lipolytica lipase on the palygorskite support through glutaraldehyde. Using an optimized immobilization protocol, a high activity of 3300 U/g immobilized lipase was obtained. Immobilized lipase retained activity over wider ranges of temperature and pH than those of the free enzyme. The optimum pH of the immobilized lipase was at pH 7.0–8.0, while the optimum pH of free lipase was at 7.0. The retained activity of the immobilized enzyme was improved both at lower and higher pH in comparison to the free enzyme. The immobilized enzyme retained more than 70% activity at 40 °C, while the free enzyme retained only 30% activity. The immobilization stabilized the enzyme with 81% retention of activity after 10 weeks at 30 °C whereas most of the free enzyme was inactive after a week. The immobilized enzyme retains high activity after eight cycles. The kinetic constants of the immobilized and free lipase were also determined. The K_m and V_max values of immobilized lipase were 0.0117 mg/ml and 4.51 μmol/(mg min), respectively.     

Immobilization of catalase via adsorption onto -histidine grafted functional pHEMA based membrane

Poly(2-hydroxyethylmethacrylate) (pHEMA) based flat sheet membrane was prepared by UV-initiated photopolymerization technique. The membrane was then grafted with -histidine. Catalase immobilization onto the membrane from aqueous solutions containing different amounts of catalase at different pH was investigated in a batch system. The maximum catalase immobilization capacity of the pHEMA–histidine membrane was 86 μg cm⁻². The activity yield was decreased with the increase of the enzyme loading. It was observed that there was a significant change between V_max value of the free catalase and V_max value of the adsorbed catalase on the pHEMA–histidine membrane. The K_m value of the immobilized enzyme was higher 1.5 times than that of the free enzyme. Optimum operational temperature was 5°C higher than that of the free enzyme and was significantly broader. It was observed that enzyme could be repeatedly adsorbed and desorbed without loss of adsorption capacity or enzyme activity.     

Thermal and Operational Characteristics of Glutaryl-7-aminocephalosporanic acid Acylase Immobilized on Silica Gel Modified by Epoxide Silanization

Summary In this study, an investigation was performed into the thermal and operational characteristics of glutaryl-7-aminocephalosporanic acid (GL-7-ACA) acylase (EC 3.5.1.-) immobilized on silica gel that had been modified by epoxide silanization. The pH values for the optimum activity of free and immobilized GL-7-ACA acylase were almost the same. However, the pH-dependent activity profile for the immobilized GL-7-ACA acylase is considerably expanded. Both free and immobilized enzymes generally had the highest activity at 50 °C. In thermodynamic studies, it was found that immobilization using epoxide silanization made GL-7-ACA acylase thermodynamically stable. In the results of repeated batch production of 7-ACA, 89.0 and 83.5% of the 7-ACA produced at the initial cycle were maintained after 20 times of recycle at 25 °C and 30 °C, respectively. Hence it was suggested that mass production of 7-ACA at 25 °C using immobilized GL-7-ACA acylase by epoxide silanization would be possible on a large scale.     

Immobilization of yeast alcohol dehydrogenase on magnetic nanoparticles for improving its stability

Yeast alcohol dehydrogenase (YADH) was immobilized covalently on Fe₃O₄ magnetic nanoparticles (10.6 nm) via carbodiimide activation. The immobilization process did not affect the size and structure of magnetic nanoparticles. The YADH-immobilized magnetic nanoparticles were superparamagnetic with a saturation magnetization of 61 emu g^–1, only slightly lower than that of the naked ones (63 emu g^–1). Compared to the free enzyme, the immobilized YADH retained 62% activity and showed a 10-fold increased stability and a 2.7-fold increased activity at pH 5. For the reduction of 2-butanone by immobilized YADH, the activation energies within 25–45 °C, the maximum specific activity, and the Michaelis constants for NADH and 2-butanone were 27 J mol^–1, 0.23 mol min^–1 mg^–1, 0.62 mM, and 0.43 M, respectively. These results indicated a structural change of YADH with a decrease in affinity for NADH and 2-butanone after immobilization compared to the free enzyme.     

Cloning and co-expression of D-amino acid oxidase and glutaryl-7-aminocephalosporanic acid acylase genes in Escherichia coli

To convert cephalosporin C to 7-aminocephalosporin (7-ACA), a D-amino acid oxidase (DAAO) gene from Trigonopsis variabilis and a glutaryl-7-aminocephalosporanic acid acylase (GL-7-ACA acylase) gene from Pseudomonas were cloned and expressed in recombinant Escherichia coli. For DAAO recombinant strain BL21(DE3)/pET-DAAO, a high DAAO activity of 250 U ml⁻¹ was obtained by a fed-batch culture. A GL-7-ACA acylase gene, in which the signal peptide sequence was deleted, was also successfully expressed in a recombinant E. coli BL21(DE3)/pET-ACY with a high expression level of 3000 U l⁻¹. A novel recombinant strain, BL21(DE3)/pET-DA, harboring both genes of DAAO and GL-7-ACA acylase, was further constructed, and a rather high DAAO activity of 140 U ml⁻¹ and GL-7-ACA acylase activity of 950 U l⁻¹ were simultaneously obtained. This recombinant strain, in which two genes are co-expressed, made it possible to catalyze cephalosporin C into 7-ACA directly.     

Comparison of characteristics of levan produced by different preparations of levansucrase from Zymomonas mobilis

The characteristics of levan formation by different preparations of levansucrase (free and immobilized enzyme and toluene-permeabilized whole cells), derived from recombinant levansucrase from Zymomonas mobilis expressed in Escherichia coli, were investigated. The maximal yield of levan by the three preparations were similar and were about 70–80% on a fructose-released basis with sucrose as nutrient at 100 g l^–1. Immobilized enzyme and toluene-permeabilized whole cells produced low molecular weight levan (2–3 × 10⁶), as determined by HPLC while high molecular weight levan (>6 × 10⁶) was the major product with the free levansucrase. The size of levan can thus be controlled by immobilized levansucrase and toluene-permeabilized whole cells in high yield.     

Characterization of cross‐linked immobilized arylesterase from Gluconobacter oxydans 621H with activity toward cephalosporin C and 7‐aminocephalosporanic acid

Cross‐linked enzyme aggregates (CLEAs) were prepared from several precipitant agents using glutaraldehyde as a cross‐linking agent with and without BSA, finally choosing a 40% saturation of ammonium sulfate and 25 mM of glutaraldehyde. The CLEAs obtained under optimum conditions were biochemically characterized. The immobilized enzyme showed higher thermal activity and a broader range of pH and organic solvent tolerance than the free enzyme. Arylesterase from Gluconobacter oxydans showed activity toward cephalosporin C and 7‐aminocephalosporanic acid. The CLEAs had a Kcat/K_M of 0.9 M^?1/S^?1 for 7‐ACA (7‐aminocephalosporanic acid) and 0.1 M^?1/S^?1 for CPC (cephalosporin c), whereas free enzyme did not show a typical Michaelis–Menten kinetics. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:36–42, 2016     

Effect of pH on the Steady State Kinetics of Bovine Heart NADH: Coenzyme Q Oxidoreductase

Complete initial steady state kinetics of NADH-decylubiquinone (DQ) oxidoreductase reaction between pH 6.5 and 9.0 show an ordered sequential mechanism in which the order of substrate bindings and product releases is NADH-DQ–DQH₂-NAD⁺. NADH binding to the free enzyme is accelerated by protonation of an amino acid (possibly a histidine) residue. The NADH release is negligibly slow under the turnover conditions. The rate of DQ binding to the NADH-bound enzyme and the maximal rate at the saturating concentrations of the two substrates, which is determined by the rates of DQH₂ formation in the active site and releases of DQH₂ and NAD⁺ from the enzyme, are insensitive to pH, in contrast to clear pH dependencies of the maximal rates of cytochrome c oxidase and cytochrome bc ₁ complex. Physiological significances of these results are discussed.     

Production of L-tartaric acid by immobilized bacterial cells Nocardia tartaricans

Nocardia tartaricans converted sodium cis-epoxysuccinate to L-tartrate. The highest cis-epoxysuccinate hydrolase activity (37.7 U mg^–1) was obtained with 0.02% (w/v) sodium deoxycholate, but this inactivated the cells. Immobilized N. tartaricans in pectate gel showed higher enzyme activity (51 U mg ^–1) compare to the free cells (8.9 U mg ^–1). After 450 days, the immobilized cells still possessed 0.65 U mg ^–1, i.e. 30% of the initial enzyme activity.     

Degradation kinetics of phenol by immobilized cells of Candida tropicalis in a fluidized bed reactor

Degradation kinetics of phenol by free and agar-entrapped cells of Candida tropicalis was studied in batch cultures. The initial phenol degradation rate achieved with free cells was higher than that obtained with immobilized cells, when phenol concentrations up to 1000 mg l^–1 were used. However, at higher phenol concentrations, the behaviour was quite different. The initial degradation rate of the immobilized yeast cells was about 10 times higher than that of the free cells, at a phenol concentration of 3500 mg l^–1. The semicontinuous and continuous degradation of phenol by immobilized yeast cells was also investigated in a multi-stage fluidized bed reactor. The highest phenol removal efficiencies and degradation rates as well as the lowest values of residual phenol and chemical oxygen demand were obtained in the semicontinuous culture when phenol concentrations up to 1560 mg l^–1 were used.