Microbial transformation of semisynthetic derivatives of daunomycinone modified in ring a

Semisynthetic derivatives of daunomycinone with 7,9-isopropylacetal, 7-O-methyl, 7-O-(4-penten-2-yl), and 7-O-(2-hydroxyethyl) substituents were converted byStreptomyces peucetius var.caesius (an adriamycin-blocked mutant) into 7-deoxy-13-dihydrodaunomycinone, while daunomycinone was transformed into 13-dihydrodaunomycinone (predominantly) and 7-deoxy-13-dihydrodaunomycinone.S. coeruleorubidus mutants 24–74 (accumulating aclavinone derivatives instead of daunomycin and related compounds) and 96-85 (producing no anthracycline substances), andS. aureofaciens B-96 (a tetracycline-blocked mutant) transformed the above substrates into the corresponding 13-dihydro derivatives, with the exception of 7,9-isopropylacetal daunomycinone which remained intact. 7-O-Propyn-1-yl daunomycinone was not transformed by any of the strains used under the conditions.     

Biotransformations of anthracyclinones inStreptomyces coeruleorubidus andStreptomyces galilaeus

The ability to transorm biologically exogenous daunomycinone, 13-dihydrodaunomycinone, aklavinone, 7-deoxyaklavinone, epsilon-rhodomycinone, epsilon-isorhodomycinone and epsilon-pyrromycinone was studied in submerged cultures of the following strains: wild Streptomyces coeruleorubidus JA 10092 (W1) and its improved variants 39-146 and 84-17 (type P1) producing glycosides of daunomycinone and of 13-dihydrodaunomycinone, together with epsilon-rhodomycinone, 13-dihydrodaunomycinone and 7-deoxy-13-dihydrodaunomycinone; in five mutant types of S. coeruleorubidus (A, B, C, D, E) blocked in the biosynthesis of glycosides and differing in the production of free anthracyclinones; in the wild Streptomyces galilaeus JA 3043 (W2) and its improved variant G-167 (P2) producing glycosides of epsilon-pyrromycinone and of aklavinone together with 7-deoxy and bisanhydro derivatives of both aglycones; in two mutant types S. galilaeus (F and G) blocked in biosynthesis of glycosides and differing in the occurrence of anthracyclinones. The following bioconversions were observed: daunomycinone leads to 13-dihydrodaunomycinone and 7-deoxy-13-dihydrodaunomycinone (all strains); 13-dihydrodaunomycinone leads to 7-deoxy-13-dihydrodaunomycinone (all strains); daunomycinone or 13-dihydrodaunomycinone leads to glycosides of daunomycinone and of 13-dihydrodaunomycinone, identical with metabolites W1 and P1 (type A), or only a single glycoside of daunomycinone (type E); aklavinone leads to epsilon-rhodomycinone (types A and B); aklaviinone leads to 7-deoxyaklavinone and bisanhydroaklavinone (type C); epsilon-rhodomycinone leads to zeta-rhodomycinone (types C, E); epsilon-rhodomycinone leads to glycosides of epsilon-rhodomycinone (types W2, P2); epsilon-isorhodomycinone leads to glycosides of epsilon-isorhodomycinone (types W2, P2); epsilon-pyrromycinone leads to a glycoside of epsilon-pyrromycinone (types W1, P1). 7-Deoxyaklavinone remained intact in all tests. Exogenous daunomycinone suppressed the biosynthesis of its own glycosides in W1 and P1; it simultaneously increased the production of epsilon-rhodomycinone in P1.     

Studies on the production of daunomycinonederived glycosides and related metabolites inStreptomyces coeruleorubidus andStreptomyces peucetius

Strains ofStreptomyces coeruleorubiduě ISP 5145,JA 10092 and 39–146, differing mutually in antibiotic activity, were found to produce identical spectrum of metabolites (at least nine antibiotically active glycosides, 13-dihydrodaunomycinone, ε-rhodomycinone and a larger number of unidentified compounds); only trace quantities of daunomycin and daunomycinone could be detected. A fraction of glycosides with a higher R_f (0.4–0.7), isolated from strain 39–146, could be transformed to daunomycin by mild hydrolysis and to daunomycinone by total hydrolysis.Streptomyces peucetius IMI 101 335 differed fromStreptomyces coeruleorubidus in an increased production of ε-rhodomycinone and a lower content of glycosides; the zone of daunomycin was most pronounced among the glycoside spots.Streptomyces coeruleorubidus 39-146 exhibited the highest activity in a medium containing 3.5% soluble starch, 3.0% soybean meal, 0.3% NaCl and 0.3% CaCo₃; glucose was a more useful carbon source for the remaining strains The activity ofStreptomyces coeruleorubidus was inhibited by 1-propanol, Na-propionate,5,5-diethylbarbiturate and bacitracin. Ferrous sulphate stimulated the production of glycosides only in strain JA 10092, decreasing simultaneously the production of aglycones.     

Continuous production ofL-malic acid by immobilizedBrevibacterium ammoniagenes cells

Summary Continuous production ofL-malic acid from fumaric acid using immobilized microbial cells was investigated. Several microorganisms having fumarase activity were immobilized into a polyacrylamide gel lattice. Among the microorganisms tested, immobilizedBrevibacterium ammoniagenes IAM 1645 showed the highest enzyme activity, but produced an unwanted by-product, succinic acid. Conditions for suppression of this side reaction were investigated, and bile extract treatment of immobilized cells was found to be effective.The bile extract treatment of immobilized cells also resulted in a marked increase of reaction rate forL-malic acid formation.No difference was observed between the native enzyme and immobilized cells in optimal pH and temperature of the enzyme reaction.The effect of temperature on the reaction rate and the stability of fumarase activity of an immobilized cell column were investigated under conditions of continuous enzyme reaction. The decay of enzyme activity during continuous enzyme reaction was expressed by an exponential relationship. Half-life of the fumarase activity of the immobilized cell column at 37°C was calculated to be 52.5 days.Presented at the Annual Meeting of the Society of Fermentation Technology, Japan, Osaka, Japan, October 30, 1975.     

Intra- and interspecific cosynthetic activity of mutants ofStreptomyces coeruleorubidus andStreptomyces galilaeus impaired in the biosynthesis of anthracyclines

Cosynthesis of anthracycline compounds was followed in five phenotypic groups of mutants of Streptomyces coeruleorubidus (A--E), blocked in the biosynthesis of the daunomycine complex, and in two mutant types of Streptomyces galilaeus (F, G) blocked in the biosynthesis of glycosides of epsilon-pyrromycinone and aklavinone. Glycosides of daunomycinone and 13-dihydrodaunomycinone were produced in combinations A+B, A+C, A+D, A+E and A+F, epsilon-rhodomycinone was synthesized in combinations A+E, A+F, B+E and B+F. During the cultivation of types B--E with type G or F non-anthracycline compounds, typical of S. galilaeus, were cosynthesized. No cosynthesis could be observed in other combinations of the mutant types. Negative results were also obtained with combinations of mutants of the same group and during cultivation of all mutant types with streptomycetes not producing anthracyclines. A scheme illustrating metabolic pathways leading to the biosynthesis of daunomycinone, aklavinone, epsilon-rhodomycinone in S. coeruleorubidus and S. galilaeus was constructed.     

7-Deoxy-13-dihydrodaunomycinone in cultures ofStreptomyces coeruleorubidus

7-Deoxy-13-dihydrodaunomycinone was isolated from three strains ofStreptomyces coeruleorubidus. Its production was found to rise at the end of cultivation and to be stimulated by lowered aeration intensity.     

Soluble and immobilized phenol oxidase of the fungusMycelia sterilia IBR 35219/2: A comparative study

Phenol oxidase (EC 1.14.18.1) from the microscopic fungusMycelia sterilia IBR 35219/2 was immobilized using glutaraldehyde on macroporous silica carriers. The enzyme immobilized on amino-Silochrome SKh-2 or aminopropyl-Silochrome 350/80 exhibited maximum activity. Soluble and immobilized phenol oxidases were compared. Compared to the soluble enzyme, the activity of which was optimum at pH 5.5, immobilized phenol oxidase exhibited optimum activity under slightly more acidic conditions (pH 5.2). Immobilization considerably increased enzyme stability. Both soluble and immobilized forms of phenol oxidase fromM. sterilia IBR 35 219/2 catalyze oxidative conversion of phenolic compounds of green tea extract.     

Production of palatinose using<Emphasis Type="Italic"> Serratia plymuthica</Emphasis> cells immobilized in chitosan

In recent decades, the production of palatinose has aroused great interest since this structural isomer of sucrose has interesting potential. We describe a simple and effective method of immobilizing Serratia plymuthica cells in chitosan. The sucrose isomerase activity of immobilized preparations was enhanced many times by activation with fresh nutrient medium and subsequent drying. The preparations obtained were physically very stable with high enzyme activity and excellent operational stability. The effect of temperature, pH and substrate concentration on enzyme activity of the immobilized cells was investigated. Using immobilized cells, a complete conversion of sucrose (40% solution) into palatinose was achieved in 4 h in a "batch"-type enzyme reactor. The use of free or immobilized cells had no effect on the composition of the solution, in particular the sugar content. The palatinose content was 80% and that of trehalulose 7%.     

Enzymatic Synthesis of Carbohydrate Derivatives Using β-Glycosidase of Sulfolobus Solfataricus

Enzymatic synthesis of different β-D-glycosides was obtained using as biocatalyst immobilized cells, crude homogenate, and homogeneous native and recombinat β-glycosidase activity of the thermophilic archaeon Sulfolobus solfataricus. In particular our investigation was concerned with the selectivity in the glycosylation of hydroxybenzyl alcohols, salicin, 1,2-propanediol, and more complex polyols as well as the use of immobilized cells for the synthesis of hexyl-β-D-glucoside. The aromatic glucosides obtained by enzyme-catalyzed transglucosylation were used for kinetic studies of purified Sulfolobus solfataricus enzyme in the hydrolysis reaction.     

Continuous alpha-amylase production using Bacillus amyloliquefaciens adsorbed on an ion exchange resin

Summary A method for the continuous production of extracellular alpha amylase by surface immobilized cells of Bacillus amyloliquefaciens NRC 2147 has been developed. A large-pore, macroreticular anionic exchange resin was capable of initially immobilizing an effective cell concentration of 17.5 g DW/1 (based on a total reactor volume of 160 ml). The reactor was operated continuously with a nutrient medium containing 15 g/l soluble starch, as well as yeast extract and salts. Aeration was achieved by sparging oxygen enriched air into the column inlet. Fermentor plugging by cells was avoided by periodically substituting the nutrient medium with medium lacking in both soluble starch and yeast extract. This fermentor was operated for over 200 h and obtained a steady state enzyme concentration of 18700 amylase activity units per litre (18.7 kU/l), and an enzyme volumetric productivity of 9700 amylase activity units per litre per hour (9.7 kU/l-h). Parallel fermentations were performed using a 2 l stirred vessel fermentor capable of operation in batch and continuous mode. All fermentation conditions employed were identical to those of the immobilized cell experiments in order to assess the performance of the immobilized cell reactor. Batch stirred tank operation yielded a maximum amylase activity of 150 kU/l and a volumetric productivity of 2.45 kU/l-h. The maximum cell concentration obtained was 5.85 g DW/l. Continuous stirred tank fermentation obtained a maximum effluent amylase activity of 6.9 kU/l and a maximum enzyme volumetric productivity of 2.73 kU/l-h. Both of these maximum values were observed at a dilution rate of 0.345 l/h. The immobilized cell reactor was observed to achieve larger volumetric productivities than either mode of stirred tank fermentation, but achieved an enzyme activity concentration lower than that of the batch stirred tank fermentor.     

Immobilization and characterization of a thermostable β-galactosidase from a thermophilic anaerobe on a porous ceramic support

A thermostable -galactosidase (EC 3.2.1.23) from a thermophilic anaerobe, strain NA10, was purified from the crude extract of the Escherichia coli transformant harboring the lacN gene. The purified enzyme was physically and covalently immobilized to a porous ceramic support, SM-10. Among the supports tested, the highest residual activity after 3 h incubation at 70° C was obtained when the enzyme was covalently immobilized to silanized SM-10 with 3-[2-(2-amino-ethylaminoethylamino)propyl]trimethoxysilane. The amount of the enzyme immobilized was about 60 mg/g of this support. The enzymatic properties were almost the same as those of the free enzyme. The half-life of this immobilized enzyme was estimated to be approximately 450 h at the pasteurization temperature (65° C).On leave from Aichi Institute of Technology, Yakusa-cho, Toyota 470-03, Japan Correspondence to: T. Saito     

Kinetcs and decay of fumarase activity of immobilized Brevibacterium ammoniagenes cells for continuous production of L-malic acid

The kinetics of the reversible fumarase reaction of immobilized Brevibacterium ammoniagenes cells and the decay behavior of enzyme activity were investigated in a plug flow system. The time course of the reaction in the immobilized cell column was well explained by the time-conversion equation including the apparent kinetic constants of the immobilized cell enzyme. The decay rate of fumarase activity was faster in the upper sections of the column (inlet side of the substrate solution) compared with the lower sections when 1M sodium fumarate (pH 7.0) was continuously passed through the column at 37°C. It was shown that the decay rate of the fumarase activity in the immobilized cell column depends on the flow rate of the substrate solution. The effect of flow rate on the decay rate of enzyme activity was considered to be related to the rate of contamination of enzyme with poisonous substances derived from the substrate solution or to the rate of leakage of enzyme stabilizers and/or enzyme itself from the immobilized cells.     

Scanning electron microscopy of immobilizedHumicola lutea during semicontinuous production of acid proteinases

The morphology of the fungusHumicola lutea (strain 120–5), immobilized in polyacrylamide and polyhydroxyethylmethacrylate and used for the semicontinuous production of acid proteinases, was examined by scanning electron microscopy. The fungus developed a dense mycelium below the bead surface as well as in the bead interior after precultivation of entrapped spores. During maximal semicontinuous enzyme biosynthesis, formation of numerous large bulbous cells with a different shape was observed. Lysis of the cells was observed mainly in the centre of the gel beads after 13 successive fermentations with polyacrylamide-immobilized cells or after 21 re-uses of polyhydroxyethylmethacrylate-immobilized mycelia, respectively. Growth and changes in the cellular morphology of immobilizedH. lutea, accompanying biosynthesis of acid proteinases, were comparable in both gel matrices but mycelia immobilized in polyhydroxyethylmethacrylate maintained their productivity twice as long.     

Characterization of microbial endo-β-glucanase immobilized in alginate beads

Endo-β-glucanase (endo-β-1,4-glucano-glucanase EC 3.2.1.4), isolated from Trichoderma reesei, was immobilized in calcium alginate beads, retaining 75% of its original activity. The polyanionic moiety surrounding the immobilized enzyme displaced the pH-activity profile to alkaline regions with respect to that of the free enzyme. The enzyme was inhibited by carboxymethylcellulose, but this inhibition appeared to be decreased by immobilizatíon. The enzyme immobilized in alginate beads showed a K_m value (1.02% w/v) lower than that of the enzyme (1.31%). The apparent V_max of immobilized cellulase preparations (238.3 μmol glucose/ml × h) decreased by a factor of 0.59 with respect to that of the soluble enzyme. The optimum temperature (60°C) of the free and entrapped enzymes remained unaltered. In contrast, the half-life of the endoglucanase immobilized in calciumalginate beads was 4.6 h at 55°C and 5.4 h at 60°C, while that of the free enzyme was 3.0 h at 55°C and 1.2 h at 60°C. A technological application of the immobilized enzymes was tested using wheat straw as a source of fermentable sugars. The hydrolytic degradation of straw, by means of a crude extract of free and immobilized cellulases and β-glucosidase, released a large amount of reducing sugars from wheat straw after 48 h (between 250–720 mg glucose/g straw), carrying out more than a 90% saccharification. A mixture of immobilized β-glucosidase and free cellulases maintained 80% of the activity of the soluble counterparts, and the co-immobilization of both types of enzymes reduced by hydrolytic efficiency to half.     

Continuous production of urocanic acid by immobilized Achromobacter liquidum cells

Several microorganisms having higher L -histidine ammonia-lyase activity were immobilized into polyacrylamide gel lattice. The yield of enzyme activity by immobilization was highest in Achromobacter liquidum IAM 1667. As A. liquidum has urocanase activity, the cells were heat-treated at 70°C for 30 min to inactivate the urocanase. Enzymatic properties of the immobilized A. liquidum cells were investigated and compared with those of the intact cells. No difference was observed between the pH activity curve and optimal temperature for the intact and immobilized cells. The permeability of substrate or product through the cell wall was increased by immobilization of the cells. When an aqueous solution of 0.25M L -histidine (pH 9.0) containing 1mM Mg²⁺ was passed through a column packed with the immobilized A. liquidum cells at a flow rate of SV = 0.06 at 37°C, L -histidine was completely converted to urocanic acid. The L -histidine ammonia-lyase activity of the immobilized cell column was stable over 40 days at 37°C. From the effluent of the immobilized cell column, Urocanic acid was easily obtained in a good yield.     

Immobilization ofPenicillium raistrickii spores and mycelium growth for 15α-hydroxylation of 13-ethylgon-4-en-3,17-dione

Spores ofPenicillium raistrickii immobilized by gel entrapment, microencapsulation and surface adsorption were allowed to grow into mycelial form, in order to accomplish hydroxylation of 13-ethylgon-4-en-3,17-dione at the 15α-position. The hydroxylating activity of both free and immobilized cells at different pH and substrate concentration as well as under starvation conditions was studied. The productivity of cells immobilized by several techniques is compared.     

Improvement of cell lysis activity of immobilized lysozyme with reversibly soluble-insoluble polymer as carrier

Summary Hen egg white lysozyme was immobilized by covalent binding to a polymer showing reversibly soluble-insoluble characteristics with pH change. The retention of the specific activity of the immobilized enzyme can be as high as 41% of that of the free enzyme. The immobilized enzyme could be used in repeated batch lysis of M. lysodeikticus cells and to enhance the release of intracellular proteins 1.4 folds when compared with batch operation.     

Purification of His6–organophosphate hydrolase using monolithic supermacroporous polyacrylamide cryogels developed for immobilized metal affinity chromatography

Organophosphate hydrolase containing hexahistidine tag at the N-terminus of recombinant protein (His₆-OPH) and expressed in Escherichia coli cells was purified using supermacroporous polyacrylamide-based monolith columns with immobilized metal affinity matrices [Me²⁺-iminodiacetic acid (IDA)–polyacrylamide cryogel (PAA) and Me²⁺-N,N,N’-tris (carboxymethyl) ethylendiamine (TED)–PAA]. Enzyme preparation with 50% purity was obtained by direct chromatography of nonclarified cell homogenate, whereas the combination of addition of 10 mM imidazole to buffers for cell sonication and sample loading, the use of precolumn with IDA–PAA matrix noncharged with metal ions, and the application of high flow rate provided the 99% purity of enzyme isolated directly from crude cell homogenate. Co²⁺-IDA–PAA provided the highest level of selectivity for His₆-OPH. Comparative analysis of purification using Co²⁺-IDA–PAA and Ni-nitrilotriacetic acid–agarose showed obvious advantages of the former in process time, specific activity of purified enzyme, and simplicity of adsorbent regeneration.     

Enhancement of operational stability of immobilized whole cell D-hydantoinase

Summary A bacteriumPseudomonas sp. KBEL 101 isolated from soil was immobilized within polyacrylamide gel and used for the synthesis of D-p-hydroxyphenylglycine from DL-5-substituted hydantoin. The half-life of immobilized whole cell D-hydantoinase was found to be about 50 hrs. In order to increase the operational stability of immobilized whole cell D-hydantoinase, a carbon or nitrogen source was supplied with the reaction mixture in the continuous stirred tank reactor. As a sole source of carbon, glycerol was found to be most effective, and the activity of immobilized whole cell enzyme was maintained stably during 7 days when 0.1%(W/V) glycerol solution was provided. In the case of nitrogen source, supplying of 0.1%(W/V) yeast extract prolonged the half-life of immobilized whole cell D-hydantoinase to about 25 days.     

Production of acrylamide using immobilized cells of<Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> M33

The cellsof Rhodococcus rhodochrous M33, which produce a nitrile hydratase enzyme, were immobilized in acrylamide-based polymer gels. The optimum pH and temperature for the activity of nitrile hydratase in both the free and immobilized cells were 7.4 and 45°C, respectively, yet the optinum temperature for acrylamide production by the immobilized cells was 20°C. The nitrile hydratase of the immobilized cells was more stable with acrylamide than that of the free cells. Under optimal conditions, the final acrylamide concentration reached about 400 g/L with a conversion yield of almost 100% after 8 h of reaction when using 150 g/L of immobilized cells corresponding to a 1.91 g-dry cell weight/L. The enzyme activity of the immobilized cells rapidly decreased with repeated use. However, the quality of the acrylamide produced by the immobilized cells was much better than that produced by the free cells in terms of color, salt content, turbidity, and foam formation. The quality of the aqueous acrylamide solution obtained was found to be of commercial use without further purification.