Peptide antibiotic production through immobilized biocatalyst technology

The use of immobilized biocatalysts for producing known or new antibiotics is presented. An evaluation of the applicability of this concept in the fascinating field of peptide antibiotic bioconversions and fermentations is also given.The use of immobilized enzymes, organelles and cells to synthesize antibiotics as an alternative method to conventional fermentation is discussed. In vitro total enzymatic antibiotic synthesis is illustrated with the ‘multienzyme thiotemplate mechanism’ of Bacillus brevis, the producer of gramicidin S. Total synthesis of peptide antibiotics, based on immobilized living cells, has recently been demonstrated with penicillin, bacitracin, nisin and a few other antibiotics.As an industrial example of the use of enzymes or cells to convert peptide antibiotics into therapeutically useful derivatives, free and immobilized penicillin acylases, producing the penicillin nucleus 6-aminopenicillanic acid (6-APA), are reviewed as well as their potential to synthesize semisynthetic β-lactams (penicillins, cephalosporins).Acylases, acetylesterases and α-amino acid ester hydrolases acting on cephalosporin-compounds and yielding valuable intermediary or end products have also gained wide interest. Stereospecific enzymic side-chain preparations for semisynthetic penicillin and cephalosporin production have recently reached the industrial stage. Bioconversion possibilities with the novel β-lactam compounds are suggested.These examples of simple single-step, as well as complex multi-step, enzyme reactions point to the vast potential of immobilized biocatalyst technology in fermentation science, in organic synthesis and in biotechnological processes in general.     

A new technique for the production of immobilized biocatalyst in large quantities

A new technique is presented for the production of immobilized biocatalysts in large quantities. It consists of breaking up a jet of the biocatalyst/presupport mixture in uniform droplets by means of a resonance technique. Entrapment of yeast and plant cells in calcium alginate has been used as the model. The production capacity of the nozzles used (0.5, 0.8, and 1.1 mm exit diameters) is two orders of magnitude larger than the production capacity of the conventional techniques (maximum capacity with a 1.1-mm nozzle diameter is 24 L/h). Depending on frequency, nozzle diameter, and volumetric flow rate, the bead size varies between 1 and 2 mm, with standard deviations of 3-5% for yeast immobilization and 10-15% for plant cells. The deactivation of both yeast and plant cells is small and comparable to that found in the corresponding conventional procedures.     

Production of L-Phenylacetyl Carbinol by Immobilized Cells of Saccharomyces Cerevisiae

Conversion of benzaldehyde to L-phenylacetyl carbinol (L-PAC) was achieved with immobilized, growing cells of Saccharomyces cerevisiae in different reactors. Product formation increased (31%) with the subsequent initial reuses of the entrapped cells. Biomass production and PAC formation depleted (40 and 57%, respectively) after 4-5 continuous growth and biotransformation cycles. With the regeneration of the biocatalysts, catalytic activity of the cells was resumed. The highest yields were in a stirred tank reactor (29 g PAC) from 77 g benzeldehyde with 14 repeated uses of entrapped cells.     

Novel immobilized biocatalyst for microbiological synthesis of pharmaceutical steroids

Applied Biochemistry and Microbiology - The steroid-transforming activity of free and immobilized cells of Pimelobacter simplex VKPM Ac-1632 entrapped in an operationally stable macroporous...     

Biooxidation of 2-phenylethanol to phenylacetic acid by whole-cell Gluconobacter oxydans biocatalyst immobilized in polyelectrolyte complex capsules

A high-performance biocatalyst in the form of encapsulated cells of Gluconobacter oxydans have been developed for production of phenylacetic acid (PAA) as a natural flavor component. Polyelectrolyte complex (PEC) capsules consisting of sodium alginate, cellulose sulfate, poly(methylene-co-guanidine), CaCl₂, and NaCl were used for highly controlled and mild encapsulation of cells. Utilization of encapsulated G. oxydans cells was a significant improvement on existing data on operational stability of cells and cumulative product concentration during biocatalytic production of PAA from 2-phenylethanol. Concerning operational stability, encapsulated cells were active over 12 cycles with a high biotransformation rate, while free cells were inactive after 7 cycles of use. The biocatalytic properties of encapsulated G. oxydans were tested in a bubble column reactor over 7 days with a final cumulative product concentration of 25 g/L. High cell viability (90%) was observed within PEC capsules by confocal laser scanning microscopy, performed before and after repetitive PAA production in the bubble column reactor. The surface microstructure of fully hydrated capsules with and without G. oxydans cells was investigated and compared using an environmental scanning electron microscope.     

High solids fermentation of hydrolysates of wheat starch B in a continuous dynamic immobilized biocatalyst bioreactor

Summary A simple and efficient method of conversion of wheat starch B to ethanol was investigated. Employing a two-stage enzymatic saccharification process, 95% of the wheat starch was converted to fermentable sugars in 40 h. From 140 g/l total sugars in the feed solution, 63.6 g/l ethanol was produced continuously with a residence time of 3.3 h in a continuous dynamic immobilized biocatalyst bioreactor by immobilized cells ofSaccharomyces cerevisiae. The advantages and the application of this bioreactor to continuous alcoholic fermentation of industrial substrates are presented.     

Rigorous model for spherical cell-support aggregate

The activity of immobilized cell-support particle aggregates is influenced by physical and biochemical elements, mass transfer, and physiology. Accordingly, the mathematical model discussed in this study is capable of predicting the steady state and transient concentration profiles of the cell mass and substrate, plus the effects of the substrate and product inhibition in an immobilized cell-support aggregate. The overall mathematical model is comprised of material balance equations for the cell mass, major carbon source, dissolved oxygen, and non-biomass products in a bulk suspension along with a single particle model. A smaller bead size and higher substrate concentration at the surface of the particle, resulted in a higher supply of the substrate into the aggregate and consequently a higher biocatalyst activity.     

A simple correlation for predicting effective diffusivities in immobilized cell systems

A simple correlation method has been developed to predict effective diffusivities of small molecules in heterogeneous materials such as immobilized cell systems. This correlation uses a single diffusivity measurement at one cell volume fraction to predict diffusivities for any other volume fraction of cell. The method has been applied to 20 sets of published diffusivity measurements in immobilized cell systems and accurately predicts affective diffusivities of molecules for the full range of cell fractions. It may also be used to predict effective diffusivities in heterogeneous materials in which the diffusivity of a molecule in each phase and the volume fraction of each phase are known. (c) 1996 John Wiley & Sons, Inc.     

Effect of biocatalyst swelling on the operation of packed-bed immobilized enzyme bioreactor

A general mathematical model was developed for predicting the performance and simulation of a packed-bed immobilized enzyme reactor performing a reaction that follows Michaelis–Menten kinetics with competitive product inhibition. The performance of a packed-bed immobilized enzyme reactor was analyzed taking into account the effect of bed swelling on various diffusional phenomena such as axial dispersion, internal and external mass transfer limitations. The numerical solutions were compared with experimental data obtained for a packed-bed reactor operating with β-galactosidase entrapped in Ca-alginate-K-κ-carrageenan gels for lactose hydrolysis.     

Enzymatic synthesis of cefazolin using immobilized recombinant cephalosporin-acid synthetase as the biocatalyst

Bioprocess and Biosystems Engineering - A method for the synthesis of β-lactam antibiotic cefazolin (CEZ) by enzymatic acylation of...     

Periodic operation of immobilized live cell bioreactor for the production of candicidin

A lumped model for cell growth and secondary metabolite production in an immobilized live cell bioreactor has been developed. This model is applied here to simulate the performance of an immobilized bioreactor under steady-state conditions and under conditions of periodically varying concentration of a growth-limiting substrate. The results of the simulation study were experimentally verified in the case of the production of the antibiotic candicidin by Streptomyces griseus in an immobilized bioreactor with forced periodic operation. The results of the studies suggest that periodically operated immobilized live cell bioreactors can provide a potent alternative for the production of non-growth-associated biochemicals, as compared to free cell fermentations, pulsed fermentations with process cycle regeneration, and nonregenerated bioreactors. This work has demonstrated that by frequent pulsing of the growth limiting nutrient, stable extended production can be obtained at high specific cellular productivities.     

Environmental metagenomics: An innovative resource for industrial biocatalysis

The current existing enzymes have been identified from cultivable micro-organisms, most frequently from bacteria. These bacterial biocatalytic capabilities have been widely used for biotransformations, resulting in the development of profitable industrial bioprocesses in the fields of feed and food processing, textiles, agro-chemistry, cosmetics, pharmaceuticals and fine chemistry. However, the originality of this bioresource is progressively drying up, while requests from industry for novel biocatalytic activities are increasing in the face of economic and environmental pressure. Metagenomics, through access to the huge reservoir of uncultivated bacteria which represents the majority of the present biodiversity, opens the door to new industrial sources of enzymes. Surmounting hurdles encountered with this technology (e.g. DNA extraction to obtain high quality DNA libraries with proper statistical representativity, setting up of relevant high throughput screenings assays, combining functional and genome-based identifications), gives unique opportunities to access novel biocatalysts that better fit with the required industrial specifications, thus providing new biocatalysis tool boxes.     

Production of precursors for anti-Alzheimer drugs: Asymmetric bioreduction in a packed-bed bioreactor using immobilized D. carota cells

(S)-1-Phenylethanol derivatives, which are the precursors of many pharmacological products, have also been used as anti-Alzheimer drugs. Bioreduction experiments were performed in a batch and packed-bed bioreactor. Then, the kinetics constants were determined by examining the reaction kinetics in the batch system with free and immobilized carrot cells. Also, the effective diffusion coefficient (D_e) of acetophenone in calcium alginate-immobilized carrot cells was investigated. Kinetics constants for free cells, which are intrinsic values, are reaction rate V_max?=?0.052?mmol?L^?1?min^?1, and constants of the Michaelis–Menten K_M?=?2.31?mmol?L^?1. Kinetics constants for immobilized cells, which are considered apparent values, are V_{max, app}?=?0.0407?mmol?L^?1 min^?1, K_{M, app}?=?3.0472?mmol?L^?1 for 2?mm bead diameter, and V_{max, app}?=?0.0453?mmol?L^?1 min^?1, K_{M, app}?=?4.9383?mmol?L^?1 for 3?mm bead diameter. Average value of effective diffusion coefficient of acetophenone in immobilized beads was determined as 1.97?×?10^?6?cm²?s^?1. Using immobilized carrot cells in an up-flow packed-bed reactor, continuous production of (S)-1-phenylethanol through asymmetric bioreduction of acetophenone was performed. The effects of the residence time and concentrations of substrate were investigated at pH 7.6 and 33°C. Enantiomerically pure (S)-1-phenylethanol (ee?>?99%) was produced with 75% conversion at 4-hr residence time.     

Biocomposite of subtilisin Carlsberg with chitosan as an effective biocatalyst for hydrolysis and synthesis of peptides

New biocatalysts, preparations of subtilisin Carlsberg immobilized on chitosan (a deacetylated derivative of chitin), were obtained. The enzyme content, hydrolytic activity, and ability to catalyze peptide bond formation in organic solvents were characterized for these preparations. The influence of the form and composition of the biocomplosite (content of the enzyme and glutaraldehyde, the cross-linking agent) and buffer pH on the biocatalytic properties of the immobilized enzyme was studied in the reactions of peptide bond hydrolysis. The synthase activity of the preparations was investigated in the reaction of synthesis of Z-Ala-Ala-Leu-Phe-pNA in a 6:4 DMF-acetonitrile mixture in dependence on the reaction time. The yield of this product was 100% after only 40 min.     

固定化酵母连续发酵生产酒精工业应用的研究

本实验以海藻酸钠为基本载体,选择性地加入适量化学物质,制备新型复合载体。该载体能较好地避免单纯海藻酸钠载体易降解、易软化［１］以及颗粒上浮的问题。经反复使用不发粘、弹性好,无毒并能保持较高的发酵水平。     

Use of Saccharomyces cerevisiae cells immobilized on orange peel as biocatalyst for alcoholic fermentation

A biocatalyst was prepared by immobilizing a commercial Saccharomyces cerevisiae strain (baker's yeast) on orange peel pieces for use in alcoholic fermentation and for fermented food applications. Cell immobilization was shown by electron microscopy and by the efficiency of the immobilized biocatalyst for alcoholic fermentation of various carbohydrate substrates (glucose, molasses, raisin extracts) and at various temperatures (30-15 degrees C). Fermentation times in all cases were low (5-15 h) and ethanol productivities were high (av. 150.6 g/ld) showing good operational stability of the biocatalyst and suitability for commercial applications. Reasonable amounts of volatile by-products were produced at all the temperatures studied, revealing potential application of the proposed biocatalyst in fermented food applications, to improve productivities and quality.     

Transient response method for evaluating the rate constants of reactions over immobilized enzymes

The transient response method was utilized to evaluate the rate constants of reaction over immobilized enzyme. Glucose oxidation catalyzed by the immobilized glucose oxidase in a fixed-bed reactor was selected as an example. A theoretical model including the effects of axial dispersion, film diffusion, and intraparticle diffusion was established for the reactor. The individual rate constant of each elementary step of this enzymatic reaction was determined through direct fitting of the experimental response data to the model.     

New enzymatic immobilized biocatalysts for detoxification of organophosphorus compounds

New immobilized biocatalysts based on phosphotriesterase and porous fabric materials impregnated with chemically cross-linked chitosan and sulphate chitosan gels were investigated. Analysis of the rheological characteristics of enzyme-containing gels confirmed their high plasticity and mechanical strength, while scanning electron microscopy verified their macroporous structure. The fabric matrix could absorb and retain a large amount of liquid thereby increasing its own weight 3.5-4.5 fold. The catalytic characteristics of the immobilized biocatalyst hydrolyzing Paraoxon, Coumaphos, Chlorpyrifos and Diisopropyl fluorophosphate were investigated. The catalytic efficacy of the soluble enzyme was 3.0-5.5-times higher compared to the immobilized form mainly due to the lower K_m values. With constant 55-60% humidity the biocatalyst retained 77% and 67-70% activity after 50-day storage at 4°C and 23°C, respectively. Benzalkonium chloride appeared to be an appropriate preservative for long-term storage of immobilized biocatalyst in a wet state.     

Preparation of immobilized enzyme with high activity using affinity tag based on proteins A and G

Affinity tag AG consisting of immunoglobulin G (lgG)-binding domains of protein A from Staphylococcus aureus (EDABC) and those of protein G from Streptococcus strain G148 (C2C3) were used to facilitate immobilization of beta-galactosidase (betagal) from Escherichia coli. Poly(methylmethacrylate/N-isopropylacrylamide/methacrylic acid) [P(MMA/NIPAM/MAA)] and poly(styrene/N-isopropylacrylamide/methacrylic acid) [P(St/NIPAM/MAA)] latex particles, which show thermosensitivity, were used as support materals to prepare affinity adsorbents. Human gamma-globulin (HgammaGb), whose major fraction is lgG, was used as an affinity ligand and was covalently immobilized onto the both latex particles by the carbodiimide method under various conditions. A fusion protein, AGbetagal, was immobilized at pH 7.3 by the specific binding of affinity tag to these affinity adsorbents. The amount of adsorbed AGbetagal per unit amount of immobilized HgammaGb, namely, efficiency of ligand utilization, was strongly affected by the type of latex particles and pH value for HgammaGb immobilization. The efficiency of ligand utilization was maximum in the affinity adsorbents prepared at pH 6.0 to 7.0, and that in the HgammaGb-P(MMA/NIPAM/MAA) latex particles was high. This result could be explained by the conformation and orientation of immobilized HgammaGb molecules. Immobilized AGbetagal retained approximately 75% of its activity in solution and the binding is stable enough to allow repeated use. These results clearly demonstrate that combination of the affinity tag AG and the affinity adsorbents, based on the thermosensitive latex particles, offers a simple and widely applicable method for preparation of immobilized enzyme with high activity. (c) 1995 John Wiley & Sons, Inc.     

A fast bioassay for phytotoxicity measurements using immobilized photosynthetic membranes

The potential of thylakoid membranes immobilized in an albumin-glutaraldehyde crosslinked matrix in a fast bioassay for phytotoxicity measurements in aqueous samples is studied. Free and immobilized preparations are compared for their electron transport activity measured as the initial rate of oxygen evolution with 2,5-cichlorobenzoquinone as the artificial electron acceptor. Immobilized thylakoids were much stable under storage conditions; in the dark, at 4 degrees C, they were fully stable in terms of photosynthetic activity for a period of 200 h. The immobilized membranes were as sensitive as the free thylakoids for the detection of most of the compounds tested (metal cations, sulfite, nitrite, and herbicides), all known as inhibitors of photosynthetic electron transport. In some instances, the immobilized preparations were even more sensitive than the free counterparts. The sensitivity could be further increased by lowering chlorophyll concentration in the assay. The short incubation period required ( approximately 10 to 15 min) and the small volume of the assay (3 mL) suggest that this type of material should be useful in the detection of locations or effluents with phytotoxic character. (c) 1994 John Wiley & Sons, Inc.