Continuous production ofL-isoleucine using immobilized growing Serratia marcescens cells

An immobilized growing cell system was applied to the continuous L -isoleucine production by Serratia marcescens. In the new immobilized-cell systems using the carrageenan gel method. S. marcescens cells in the gel required nutrients and oxygen for growth, and the numbers of living cells per milliliter of gel increased to the levels of that of free cells in the liquid medium. This immobilized growing cell system exhibited high and stable activity for isoleucine production under steady-state conditions. Continuous isoleucine production was carried out by feeding the nutrient medium under aeration into a fluidized bed reactor containing the immobilized cells. In the continuous operation, an efficient production was maintained by automatically controlling the pH of the reaction mixture at 7.5. The productivity of isoleucine increased using multibed reactors. In a two-bed reactor system, the effluent L -isoleucine concentration reached 4.5 mg/ml at a retention time of 10 hr, and a steady state was maintained for longer than 30 days.     

Continuous production of ethanol using immobilized growing yeast cells

Summary Immobilized growing yeast cells were prepared in kappa-carra-geenan gel. Gel beads containing a small number of cells were incubated in a complete medium. The cells grew very well in the gel and the number of living cells per ml of gel increased to over 10 times that of free cells per ml of culture medium. After growing in the gel, the cells formed a dense layer of cells near the gel surface and produced large amounts of ethanol. The conditions for continuous production of ethanol using immobilized growing yeast cells were investigated. The supply of appropriate nutrients for growth was essential for the continuous production. The living cells in the gel were maintained at the high level of 10⁹ per ml of gel and continuous production of ethanol using the complete medium containing 10% glucose was carried out with a retention time of 1 h. In this operation, a stable steady state was maintained for longer than 3 months. The ethanol concentration was 50 mg/ml and the conversion of glucose utilized to ethanol produced was almost 100% of the theoretical yield.     

Comparative study of d-xylose conversion to ethanol by immobilized growing or non-growing cells of the yeast Pachysolen tannophilus

Summary The direct conversion of d-xylose to ethanol was investigated using immobilized growing and non-growing cells of the yeast Pachysolen tannophilus. Both preparations produced ethanol from d-xylose, however the d-xylose conversion to ethanol was much better with immobilized growing cells. Ethanol concentration up to 22.9 g/l and ethanol yield of 0.351 g/g of d-xylose were obtained in batch fermentation by immobilized growing cells whereas only 17.0 g/l and 0.308 g/g of d-xylose were obtained by immobilized non-growing cells. With continuous systems, immobilized growing cells were necessary for the long-term operation, since a steady state ethanol concentration of 17.7 g/l was maintained for only one week by immobilized non-growing cell reactor. With simultaneous control of aeration rate and concentrations of nitrogen sources in feed medium, immobilized growing cells of P. tannophilus showed excellent performance. At a residence time of 25 h, the immobilized cell reactor produced 26.9 g/l of ethanol from 65 g/l of d-xylose in feed medium.     

Influence of oxygen supply on the stability of recombinant plasmid pTG201 in immobilized E. coli cells

Summary Cells of Escherichia coli K12, carrying the recombinant plasmid pTG201, were immobilized in -carrageenan gel in order to improve the following plasmid parameters: (i) maintenance of a high level of plasmid copy number, (ii) good plasmid stability and (iii) good expression of plasmid encoded gene. The experiments were carried out on LB medium without antibiotic selection in continuous and batch cultures supplied with air or pure oxygen. Parallel experiments with free cells were also performed. In all the cases immobilized cells presented better plasmid stability parameters than free cells. Best results were obtained with immobilized cells supplied with pure oxygen. In this case, an average plasmid copy number of 60 and a value of plasmid-carrying cells close to 100% were maintained with little change during more than 200 generations. In addition, an optical microscopy analysis is proposed to allow the quantitation of cell growth in gel beads.     

Continuous production of l-serine by immobilized growing Corynebacterium glycinophilum cells

Summary Auxotrophic mutant cells of Corynebacterium glycinophilum with high l-serine production activity were immobilized by entrapment with various gel materials, such as synthetic prepolymers and natural polysaccharides. The entrapped cells were used for estimation of l-serine productivity in a medium supplemented with glycine as a precursor. Based on the above criteria, including cell growth in gels and cell leakage from gels, calcium alginate was the most suitable gel material. Continuous l-serine fermentation with calcium alginate-entrapped growing cells was successfully achieved in an air-bubbled reactor for at least 13 days.     

Continuous production of ethanol in high concentration using immobilized growing yeast cells

Summary Application of an immobilized growing yeast cell system to continuous production of ethanol in high concentration (10%) was investigated using Saccharomyces cerevisiae IFO 2363. When a medium containing 25% glucose was fed, the growth of yeast cells in gel was inhibited. The inhibitory effect was found to be reduced by a stepwise increase in concentration of glucose in the feed medium. The stepwise operation resulted in constant growth of cells in the gel even in the medium containing 25% glucose. By this stepwise feeding system, continuous production of ethanol of 114 mg/ml was maintained at a retention time of 2.6 h for over 2 months and a conversion rate of glucose to ethanol of over 95% of theoretical, was achieved.     

Synthesis of l-tyrosine by immobilized Escherichia intermedia cells

Summary Cells of Escherichia intermedia were immobilized by entrapment in a polyacrylamide gel and used for the enzymatic production of l-tyrosine from phenol, pyruvate, and ammonia. A preparation containing 50 mg of cells/g of gel retained 60% of its original activity. The effect of temperature, pH and substrate concentration on the activity of free cells was almost identical with the effect on immobilized cells. Phenol showed inhibition and inactivation of the catalyst at high concentration. Synthesis of l-tyrosine (up to 10 g/l) was demonstrated in batch reactors with high conversion yields (95–100%) and a maximal productivity of 2 g/l/h. In continuous reactor the catalyst showed a very high operational stability (more than 54 days without losses).     

Modulation of striatal dopamine release in cerebral ischemia byL-arginine

The effect ofL-arginine, the precursor of nitric oxide, on ischemic dopamine release from the striatum was investigated in Mongolian gerbils subjected to bilateral carotid artery occlusion (15 min) alone or with reflow (2 h). Dopamine and its metabolites were measured in the striatal extracellular space dialysate after continuous perfusion (2 l/min) of artificial extracellular fluid in the presence or absence of 15 mmol/literL- orD-arginine or 1 mmol/liter nitro-L-arginine.L-Arginine but notD-arginine increased the striatal content of dopamine in pre- and postischemia whereas it lowered the levels of dopamine and 3-methoxytyramine induced by ischemia. In contrast, nitro-L-arginine reduced the preischemic levels of dopamine and 3,4-dihydroxyphenyl-acetic acid, and had no effect on the ischemic release of dopamine. These findings indicate thatL-arginine stereospecifically modified the ischemic release and metabolism of dopamine. The data also suggest that the basal level of nitric oxide is not involved in dopamine release during ischemia but may participate in regulating dopamine release under physiological conditions.Presented in part at the 19th International Joint Conference on Stroke and Cerebral Circulation, San Diego, California, February 17–19, 1994.     

Enzymes of arginine utilization and their formation in Aeromonas formicans NCIB 9232

In Aeromonas formicans two inducible catabolic pathways of L-arginine have been characterized. The arginine decarboxylase is induced by arginine which also induces the three enzymes of the arginine deiminase pathway but only in stress conditions such as a shift from aerobic growth conditions to very low oxygen tension. Addition of glucose to medium containing arginine leads to repression of the enzymes involved in the arginine deiminase pathway while exogenous cAMP prevents that repression of enzyme synthesis by glucose. This suggests that the induction of arginine deiminase pathway is regulated by carbon catabolite repression and the energetic state of the cell.     

Influence of copper and zinc ions on toxicity of sodium N-methyldithiocarbamate to Fusarium oxysporum f. sp. lycopersici

Summary It was found that dl-lactate, acetate, pyruvate, succinate, fumarate, malate, oxalacetate and L-aspartate stimulated considerably the production of the antitumor L-asparaginase EC-2 by a colicinogenic strain of E. coli in Tryptone medium. While in the absence of these stimulative substances enzyme production was about 0.01 IU/mg dry weight, it reached 0.57–1.18 IU/mg in the presence of the substances named above. Maximum effects were obtained at the concentrations 0.025–0.1 M; at higher concentrations enzyme production decreased. L-asparagine raised the enzyme production from 0.05 IU/mg to 0.70 IU/mg; in order to obtain this effect, however, it was necessary to lower the oxygen absorption rate. Citrate and -ketoglutarate had no stimulatory effect; the effect of L-glutamate was negligible. In the cases of dl-lactate, pyruvate and L-aspartate the dependence of stimulatory effects on the time of addition of the stimulants was studied. It was found that in the case of pyruvate and especially of dl-lactate enzyme production increased rapidly between the 4 and 6 h of cultivation, i.e. at the end of the exponential growth phase; it did not matter whether the stimulant had been added at zero, 2 or 4 h of cultivation. In the case of L-aspartate the situation was principally similar, though the enzyme production started later and increased more slowly.     

Applicability of pectate-entrapped <Emphasis Type="Italic">Lactobacillus casei</Emphasis> cells for <Emphasis Type="SmallCaps">l</Emphasis>(+) lactic acid production from whey

Lactic acid is a versatile organic acid, which finds major application in the food, pharmaceuticals, and chemical industries. Microbial fermentation has the advantage that by choosing a strain of lactic acid bacteria producing only one of the isomers, an optically pure product can be obtained. The production of l(+) lactic acid is of significant importance from nutritional viewpoint and finds greater use in food industry. In view of economic significance of immobilization technology over the free-cell system, immobilized preparation of Lactobacillus casei was employed in the present investigation to produce l(+) lactic acid from whey medium. The process conditions for the immobilization of this bacterium using calcium pectate gel were optimized, and the developed cell system was found stable during whey fermentation to lactic acid. A high lactose conversion (94.37%) to lactic acid (32.95 g/l) was achieved with the developed immobilized system. The long-term viability of the pectate-entrapped bacterial cells was tested by reusing the immobilized bacterial biomass, and the entrapped bacterial cells showed no decrease in lactose conversion to lactic acid up to 16 batches, which proved its high stability and potential for commercial application.     

Production of l (+) lactic acid by Lactobacillus delbrueckii immobilized in functionalized alginate matrices

The role of functionalized alginate gels as immobilized matrices in production of l (+) lactic acid by Lactobacillus delbrueckii was studied. L. delbrueckii cells immobilized in functionalized alginate beads showed enhanced bead stability and selectivity towards production of optically pure l (+) lactic acid in higher yields (1.74Yp/s) compared to natural alginate. Palmitoylated alginate beads revealed 99% enantiomeric selectivity (ee) in production of l (+) lactic acid. Metabolite analysis during fermentation indicated low by-product (acetic acid, propionic acid and ethanol) formation on repeated batch fermentation with functionalized immobilized microbial cells. The scanning electron microscopic studies showed dense entrapped microbial cell biomass in modified immobilized beads compared to native alginate. Thus the methodology has great importance in large-scale production of optically pure lactic acid.     

Production of NO and N2O by the Heterotrophic Nitrifier Alcaligenes faecalis parafaecalis under Varying Conditions of Oxygen Saturation

Production of NO and N ₂ O by the heterotrophic nitrifier Alcaligenes faecalis subsp. parafaecalis was studied during growth in batch and continuous culture on peptone-meat extract medium. Depending on oxygen saturation level, medium redox status and amount of substrate supplied, the microorganisms produced 0.002–0.25 mg NO-N h^{- 1} (g protein)^{- 1} and 0.16–2.4 mg N ₂ O-N h^{- 1} (g protein)^{- 1} . Maximum rates of nitrogen oxides production were observed during peak events initiated by sudden changes of oxygen supply in the medium and were due to combined nitrification/denitrification taking place simultaneously within the cells. Based on model simulations of enzymatic kinetics of denitrification, possible mechanisms of increased nitrogen oxides production during periods of changes in oxygen supply are suggested.     

The effects of immobilization on the biochemical,physiological and morphological features of Anabaena azollae

Anabaena azollae, a presumptive isolate from Azolla filiculoides, was immobilized in polyurethane foam, hydrophilic polyvinyl foam and alginate. When viewed by low-temperature scanning electron microscopy a thick mucilage layer covered the surface of both cells and matrix; this closely resembles the mode of attachment of the symbiont Anabaena in the Azolla leaf cavity. The heterocyst frequency of the immobilized A. azollae doubled relative to free-living cells and reached a level of 14–17%. Immobilization induced increases in both hydrogen production via nitrogenase or hydrogenase and in the rates and stabilization of acetylene reduction (N₂-fixation). Ammonia production by immobilized cells with L-methionine-D,L-sulfoximine (MSX) is greater than that of freeliving cells. Immobilized cells without MSX were, however, able to excrete ammonium at lower rates thus emulating the characteristic of the symbiotic cyanobacteria (A. azollae) in the leaf cavity of Azolla.Abbreviations Chl chlorophyll - GS glutamine synthetase - MSX L-methionine-D,L-sulfoximine - SEM scanning electron microscopy - PU polyurethane - PV polyvinyl     

Production of propene oxide in an organic liquid-phase immobilized cell reactor

Some major restrictions of the production of propene oxide in an organic liquid-phase immobilized cell packed-bed reactor were quantified, and techniques were investigated to enhance the epoxide production rates. Propene-epoxidizing Mycobacterium cells were entrapped in calcium alginate gel and contacted with the substrates, propene and oxygen, which were dissolved in a continuous organic phase, n-hexadecane. The effects of product inhibition by the toxic epoxide—microbial consumption of propene oxide and immobilized cell deactivation—restricted severely the accumulation of the epoxide in the recirculation reactor system and could be predicted using a simple mathematical model. Epoxide inhibition was reduced by absorbing the product in the gas phase in old di-n-octyl phthalate. The resulting increase in propene oxide production agreed with model calculations. An alternating supply of propene and a co-substrate (ethene) prolonged the half-life of the immobilized cells. Using 50 g dry weight of cells, 1.5 g stereospecific propene oxide was produced in two days, of which 1.0 g was absorbed in the di-n-octyl phthalate phase.     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

Production of tylosin and nikkomycin by immobilized Streptomyces cells

Summary Mycelia of Streptomyces sp. T 59-235 and Streptomyces tendae Tü 901 (producing the antibiotics tylosin and nikkomycin, resp.) were immobilized in different carriers. With both organisms best antibiotic production was observed in calcium alginate gel.Influence of aeration, cell density and flow rate on antibiotic production was investigated in batch fermentation and in a continuous system (air-bubbled reactor).In batch fermentation, immobilization prolongued the production phase from 72 to 120 h (Streptomyces T 59-235) and from 72 to 96 h (S. tendae). The relative productivity of immobilized cells was 40 to 50% compared to that of free mycelia in both cases.In continuous tylosin fermentation highest production rate was observed in a medium nearly saturated with oxygen.Nikkomycin production by immobilized S. tendae could be maintained for longer than 350 h in a continuous system. The production rate depended on cell density and flow rate of the medium. The maximum specific productivity was 100% compared to that of free mycelium in batch culture.     

Effector molecules from antitumor macrophages induced with OK-432 and cyclophosphamide

Summary The present study was designed to determine whether antitumor activity of macrophages induced with OK-432 and cyclophosphamide was mainly dependent on their ability to produce a soluble factor, that is,l-arginine-dependent nitric oxide as measured by nitrite concentration. Nitrite production by peritoneal macrophages from NIH Swiss mice pretreated with OK-432 (125 KE/kg) i.p. twice at 1-week intervals and with cyclophosphamide (200 mg/kg) i.p. 2 days before the second OK-432 treatment, increased with time for 24 h, and proportionally depended on macrophage numbers. Nitrite production was inhibited by actinomycin D and puromycin but not by mitomycin C.N ^G-Monomethyl-l-arginine, a specific competitive inhibitor ofl-arginine-dependent nitric oxide synthesis, also inhibited production. There was a close correlation between nitrite production and antitumor activity in macrophages from mice pretreated with either OK-432 and cyclophosphamide, OK-432, or thioglycolate broth. OK-432 increased both nitrite production and antitumor activities when added to the macrophage from mice pretreated with OK-432 but not with thioglycolate broth. Both activities of macrophages from mice pretreated with OK-432 and cyclophosphamide were enhanced with increasing concentrations ofl-arginine (0.125–1 mM) in the culture medium.d-Arginine, however, did not substitute forl-arginine. Neither activity was affected by contact between the macrophage and the EL4 cell. The macrophage showed antitumor activity through a membrane filter though the activity was greatly reduced. This antitumor activity of macrophages through a membrane was also inhibited byN ^G-Monomethyl-l-arginine, and increased by OK-432. However, conditioned media, obtained by culturing macrophages induced with OK-432 and cyclophosphamide, inhibited growth of EL4 cells. This activity was carried out by dialysable and non-dialysable factors. One of the dialysable factors was nitrite, an oxidized product of nitric oxide. The antitumor activity of non-dialysable factors was heat-stable and production of factors was increased byN ^G-Monomethyl-l-arginine and OK-432. Also, non-dialysable factors increased both antitumor and nitrite production activities of OK-432-elicited macrophages, when incubated with factors. Such activity of factors was also heat-stable. The production of factors increased with incubation time of macrophages, and was not inhibited byN ^G-Monomethyl-l-arginine. These results indicate that in vitro antitumor activity of macrophages induced with OK-432 and cyclophosphamide was mainly dependent onl-arginine-dependent nitric oxide, and that macrophageassociated soluble factors other than nitric oxide were also needed to inhibit fully tumor growth in vitro.     

Enzymatic Synthesis and Antioxidant Properties of <Emphasis Type="SmallCaps">L</Emphasis>-Ascorbyl Oleate and <Emphasis Type="SmallCaps">L</Emphasis>-Ascorbyl Linoleate

L-Ascorbyl oleate and L-ascorbyl linoleate were synthesized by an immobilized lipase from Candida antarctica with yields of 38% and 44%, respectively. L-Ascorbyl oleate was stable in sterile culture medium over 12 h at 37 °C but L-ascorbyl linoleate degraded by 17%. Ascorbyl oleate had a better protective effect on human umbilical cord vein endothelial cells treated with H₂O₂ than of L-ascorbic acid-2-phosphate-6-palmitate (Asc2P6P).Revisions requested 21 July 2004/26 August 2004; Revisions received 20 August 2004/27 September 2004     

Synthesis of l-dopa by escherichia intermedia cells immobilized in a polyacrylamide gel

Summary Escherichia intermedia cells were immobilized by entrapment in a polyacrylamide gel and used for l-dopa synthesis from pyrocatechol, pyruvate and ammonia. An immobilized cell preparation containing 75 mg cells/g gel retained 45%–50% of the activity of free cells. The effect of temperature, pH and substrate concentration of the initial rate of l-dopa synthesis was very similar for free and immobilized cells. Substrate inhibition was observed for pyrocatechol, pyruvate and ammonia. In a batch reactor, 5.4 g·l^-1 l-dopa was obtained, with 100% conversion yield of pyrocatechol and l-dopa productivity of 0.18 g·l^-1·h^-1. The use of a pyrocatechol-borate complex decreased by-product formation and catalyst inactivation.