Cloning and nucleotide sequencing of the membrane-bound L-sorbosone dehydrogenase gene of Acetobacter liquefaciens IFO 12258 and its expression in Gluconobacter oxydans.

Cloning and expression of the gene encoding Acetobacter liquefaciens IFO 12258 membrane-bound L-sorbosone dehydrogenase (SNDH) were studied. A genomic library of A. liquefaciens IFO 12258 was constructed with the mobilizable cosmid vector pVK102 (mob+) in Escherichia coli S17-1 (Tra+). The library was transferred by conjugal mating into Gluconobacter oxydans OX4, a mutant of G. oxydans IFO 3293 that accumulates L-sorbosone in the presence of L-sorbose. The transconjugants were screened for SNDH activity by performing a direct expression assay. One clone harboring plasmid p7A6 converted L-sorbosone to 2-keto-L-gulonic acid (2KGA) more rapidly than its host did and also converted L-sorbose to 2KGA with no accumulation of L-sorbosone. The insert (25 kb) of p7A6 was shortened to a 3.1-kb fragment, in which one open reading frame (1,347 bp) was found and was shown to encode a polypeptide with a molecular weight of 48,222. The SNDH gene was introduced into the 2KGA-producing strain G. oxydans IFO 3293 and its derivatives, which contained membrane-bound L-sorbose dehydrogenase. The cloned SNDH was correctly located in the membrane of the host. The membrane fraction of the clone exhibited almost stoichiometric formation of 2KGA from L-sorbosone and L-sorbose. Resting cells of the clones produced 2KGA very efficiently from L-sorbosone and L-sorbose, but not from D-sorbitol; the conversion yield from L-sorbosone was improved from approximately 25 to 83%, whereas the yield from L-sorbose was increased from 68 to 81%. Under fermentation conditions, cloning did not obviously improve the yield of 2KGA from L-sorbose.     

Microbial production of L-ascorbic acid from D-sorbitol, L-sorbose, L-gulose, and L-sorbosone by Ketogulonicigenium vulgare DSM 4025

Ketogulonicigenium vulgare DSM 4025, known as a 2-keto-L-gulonic acid producing strain from L-sorbose via L-sorbosone, surprisingly produced L-ascorbic acid from D-sorbitol, L-sorbose, L-gulose, and L-sorbosone as the substrate under a growing or resting condition. As the best result, K. vulgare DSM 4025 produced 1.37 g per liter of L-AA from 5.00 g per liter of L-sorbosone during 4 h incubation time at 30 degrees C under the resting cell condition having 5.70 g per liter of wet cells. The precursor of L-AA formation from D-sorbitol and L-sorbose, except for L-gulose, was thought to be the putative furanose form of L-sorbosone. This is the first time it is reported that bacteria can produce vitamin C via L-sorbosone.     

Effect of toluene-permeabilization on oxidation of D-sorbitol to L-sorbose by Gluconobacter suboxydans cells immobilized in calcium alginate

Summary The effect of permeabilization of G. suboxydans cells with toluene on the oxidation of D-sorbitol to L-sorbose was investigated. Treatment of the cells with 10% toluene resulted in a three fold increase in the specific sorbitol dehydrogenase activity and a two fold increase in the efficiency of D-sorbitol conversion to L-sorbose of the free cell suspension. When the permeabilized cells were immobilized in calcium alginate, the operational stability during air-lift reactor operation was also found to increase with up to three times longer half-life(44 days) of catalytic activity compared with immobilized intact cells.     

具有谷氨酸脱羧酶的大肠杆菌固定化细胞

本文研究了用海藻酸钙包埋法制备含谷氨酸脱羧酶固定化细胞的方法以及研究了制备的条件和影响其制备的因素。该法具有包埋细胞活力回收高,方法简便等优点。比较研究了固定化细胞和自然细胞谷氨酸脱羧酶的一些生物化学性质。其中固定化细胞最适pH和pH稳定性增加,最适温度及热稳定性下降;表观米氏常数增大;二价金属离子Zn~(++)、Cu~(++)、Mg~(++)、Fe~(++),Sr~(++)程度不同的抑制酶活性,Ca~(++)激活固定化细胞酶活性,EDTA无抑制作用。对固定化细胞和自然细胞酶活力活化的研究中发现这两种细胞经蒸馏水保温处理后酶活性都上升,且自然细胞酶活的上升较固定化细胞大;而用底物溶液处理后,自然细胞无变化,固定化细胞酶活下降。     

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).     

醇醛脱氢酶的分离纯化及其基因文库的构建和筛选

在维生素C的发酵生产过程中,普通生酮基古龙酸菌S2(Ketogulonigenium vulgare)能产生醇醛脱氢酶,将L-山梨糖转化为VC的前体2-酮基-L-古龙酸(2-KLG)。通过超声波破碎菌体、硫酸铵分级沉淀、DEAE Sepharose Fast Flow阴离子交换层析,QSepharose High Performance柱层析等过程,从普通生酮基古龙酸菌S2发酵液中分离纯化了醇醛脱氢酶,并用该纯化酶免疫新西兰兔制备出了合格抗血清。同时,普通生酮基古龙酸菌S2基因组DNA经Sau3AⅠ部分酶切后,与黏粒载体pKC505连接,用包装蛋白进行包装,转染大肠杆菌DH5浕,构建了基因组文库。最后应用免疫酶斑点技术(Dot-ELISA)从12000个克隆子中筛选得到一个阳性克隆K719#。通过检测该基因工程菌的活性,表明K719#具有使L-山梨糖转化为2-KLG的功能,从而使醇醛脱氢酶在大肠杆菌中获得了高效表达,这为简化VC的生产工艺奠定了基础。     

Stimulation by organic solvents and detergents of conversion of L-sorbose to L-sorbosone by Gluconobacter melanogenus IFO 3293.

Treatment of Gluconobacter melanogenus IFO 3293 cells with benzene, carbon tetrachloride, cyclohexane, deoxycholate, toluene, or xylene stimulated their conversion of L-sorbose to L-sorbosone two- to threefold. The degree of stimulation depended upon the length of exposure time to the agent and the age of the G. melanogenus cells. A rapid decrease in viability of the cells and degradation of cell RNA was noted after treatment with the effective agents. The G. melanogenus cells were unable to absorb L-sorbose actively after toluene treatment.     

Efficient immobilization of epoxide hydrolase onto silica gel and use in the enantioselective hydrolysis of racemic para-nitrostyrene oxide

Epoxide hydrolase from Aspergillus niger (E.C. 3.3.2.3) was immobilized by covalent linking to epoxide-activated silica gel under mild conditions. A very easy procedure allowed to prepare an immobilized biocatalyst with more than 90% retention of the initial enzymatic activity. Immobilized and free enzyme showed very similar behaviour with respect to the effect of pH on activity and stability. One benefit of immobilizing epoxide hydrolase from A. niger on silica gel was the enhanced enzyme stability in the presence of 20% DMSO. The kinetic resolution of racemic para-nitrostyrene oxide was investigated by using this new immobilized biocatalyst. The enantioselectivity of the enzyme was not altered by the immobilization reaction: both unreacted epoxide and formed diol were obtained with very high ee (99 and 92%, respectively). In addition, the biocatalyst could be easily separated from the reaction mixture and re-used for over nine cycles without any noticeable loss of enzymatic activity or change in the enantioselectivity extent. The activity of immobilized AnEH was retained for several months.     

Comparative study of production of dextransucrase and dextran by cells of Leuconostoc mesenteroides immobilized on Celite and in calcium alginate beads

In fed-batch fermentation, cells of L. mesenteroides immobilized on three types of Celite were used to produce dextransucrase (DS) followed by production of dextran. A layer of calcium alginate on the porous Celite R630 particles improved their mechanical stability, increased the amount of soluble DS produced and decreased the cell leakage from the highly porous support. Enzyme production with the immobilized cell cultures was significantly affected by both pore and particle size. Immobilized cultures using Celite R648 (average particle radius of 200 mum and pore size of 0.14 mum) produced the highest total enzymatic activity, followed by Celite R633, alginate-coated Celite R630, Celite R630, and then calcium alginate beads. Culture of free cells produced about 18% more total enzymatic activity than immobilized cells in calcium alginate beads, but about 64% less than immobilized cells on Celite R630. It is expected that larger amounts of enzymatic activity than measured are immobilized inside the alginate-coated Celite R630 and calcium alginate beads due to the mass transfer limitation conferred by the dextran product formed therein. The dextran yield from conversion of sucrose to dextran and fructose with all such enzyme-enriched, immobilized-cell cultures was higher than that obtained from free-cell culture under similar conditions.     

Immobilization and characterization of Saccharomyces cerevisiae in crosslinked,prepolymerized polyacrylamide-hydrazide

Summary Baker's yeast (Saccharomyces cerevisiae) was immobilized in gels made of prepolymerized, linear, water soluble polyacrylamide, partially substituted with acylhydrazide groups. Gelation was effected by the addition of controlled amounts of dialdehydes (e.g. glyoxal). The immobilized yeasts retained full glycolytic activity. Moreover, the entrapped cells were able to grow inside the chemically corsslinked gel during continuous alcohol production. Glyoxal was found to be the most favourable crosslinking agent for this system. the system employed allowed for the free exchange of substrate and products. The gel surrounding the entrapped cells had no effect on temperature stability profile. On the other hand, substantial enhancement in survival of cells in presence of high ethanol concentrations was recorded for the entrapped yeast. The capability of the immobilized yeast to carry out continuous conversion of glucose to ethanol was demonstrated.     

Biotransformation of 3-methoxy-8,14-seco-1,3,5(10),9(11) estratetraen-14,17-dione (secodione) to its 17beta-hydroxy derivative (secol) using immobilized yeast cells (Pichia farinosa Y-118)

The yeast cells of Pichia farinosa Y-118 were immobilized in polyacrylamide gel and used for 17 beta-oxidoreduction of secondione to secol. The loss of hydroxysteroid oxidoreductase activity of cells was found to be insignificant during immobilization. The preparation exhibited greater temperature stability as compared to free cells. The ratio of reaction volume to the volume of immobilized biocatalyst in the range 1.4-1.9 was found to be satisfactory for the reaction conditions studied. This ratio played a significant role in the stability of the catalyst particle, since beyond a critical value the disintegration of gel granules was rapid resulting in sharp decline of activity. The immobilized cell preparation could be used 50 times over a period of 100 days without loss of activity. However, the activity declined in further reuses, leaving the preparation 50 and 35% active after its 60th and 70th uses, respectively.     

NADPH production from NADP+ with a glucose dehydrogenase system involving whole cells and immobilized cells of Gluconobacter suboxydans

Summary A convenient and efficient method of NADPH production from NADP⁺ has been established using a glucose dehydrogenase system involving whole cells and immobilized cells of Gluconobacter suboxydans IFO 3172. Using airdried cells of the bacterium, the optimum conditions for NADPH production were examined, including the cell and glucose concentrations, NADP⁺ concentration, pH, buffer and reaction temperature. Under suitable conditions, the conversion ratio and the amount of NADPH accumulated reached about 100% and 73 mg/ml of the reaction mixture, respectively, after 1-h reaction. Intact cells of the bacterium also showed high NADPH production even in the reaction mixture without a surfactant. The addition of Triton X-100 to the reaction mixture and freeze-thawing treatment of intact cells enhanced the production. The NADPH production method was further improved by using cells of the bacterium immobilized by entrapment in a -carrageenan gel lattice. The immobilized cells had almost the same enzymatic properties as the air-dried cells. The conditions for the continuous production of NADPH with an immobilized cell column were also investigated. NADPH was produced in a good yield (about 95%) with this continuous process.     

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.     

Stabilization of prostaglandin synthetase by immobilization of goat seminal microsomes on silica gel-G

Prostaglandin synthetase was immobilized by adsorption of goat vesicular microsomes on silica gel containing CaSO4 (silica gel G). Repeated cycles of enzymatic conversion of arachidonic acid to prostaglandin by the immobilized microsomes increased the product yield by 1.5 fold, in comparison to the same by free microsomal particles. The presence of Ca2+ in silica gel is responsible for this improved yield of prostaglandin as the divalent metal ion stabilized prostaglandin synthetase activity in a remarkable way. Microsomal particles immobilized on solid supports like alumina G and controlled pore glass were not very effective.     

Cellobiose hydrolysis using Pichia etchellsii cells immobilized in calcium alginate

The rate of celluose degradation, limited due to the inhibition by cellobiose, can be increased by the hydrolysis of cellobiose to glucose using immobilized beta-glucosidase. Production of beta-glucosidase in four yeasts was studied and a maximum activity of 1.22 IU/mg cells was obtained in cells of Pichia etchellsii when grown on 3% cellobiose as the sole carbon source. A study of the immobilization of beta-glucosidase containing cells of Pichia etchellsii on various solid supports was conducted and immobilization by entrapment in calcium alginate gel beads was found to be the most simple and efficient method. A retention of 96.5% of initial activity after ten sequential batch uses of the immobilized preparation was observed. The pH and temperature optima for free and immobilized cells were the same, i.e., 6.5 (0.05M Maleate buffer) and 50 degrees C, respectively. Even though the temperature optimum was found to be 50 degrees C, the enzyme exhibits a better thermal stability at 45 degrees C. Beads stored at 4 degrees C for six months retain 80% of their activity. Kinetic studies performed on free and immobilized cells shown that glucose is a noncompetitive product inhibitor.The immobilized preparation was found to be limited by pore diffusion but exhibited no film-diffusion resistance during packed bed column indicated by a low dispersion number of 0.1348. A model for reaction with pore diffusion for a noncompetitive type of inhibited system was developed and applied to the cellobiose hydrolysis system. The rate of reaction with diffusional limitations was determined by using the model and effectiveness factors were calculated for different particle sizes. An effectiveness factor of 0.49 was obtained for a particle diameter of 2.5 mm. The modified rate expression using the effectiveness factor represented batch and packed bed reactor operation satisfactorily. The productivity in the packed bed column was found to fall rapidly with increase in conversion rate indicating that the operating conditions of the column would have to be a compromise between high conversion rates and reasonable productivity. A half-life of over seven days was obtained at the operating temperature of 45 degrees C in continuous operation of the packed bed reactor. However, the half-life in the column was found to be greatly affected by temperature, increasing to over seventeen days at a temperature of 40 degrees C and decreasing to less than two days at 50 degrees C.     

Enzymatic synthesis of theanine from glutamic acid γ-methyl ester and ethylamine by immobilized Escherichia coli cells with γ-glutamyltranspeptidase activity

Theanine (γ-glutamylethylamide) is the main amino acid component in green tea. The demand for theanine in the food and pharmaceutical industries continues to increase because of its special flavour and multiple physiological effects. In this research, an improved method for enzymatic theanine synthesis is reported. An economical substrate, glutamic acid γ-methyl ester, was used in the synthesis catalyzed by immobilized Escherichia coli cells with γ-glutamyltranspeptidase (GGT) activity. The results show that GGT activity with glutamic acid γ-methyl ester as substrate was about 1.2-folds higher than that with glutamine as substrate. Reaction conditions were optimized by using 300 mmol/l glutamic acid γ-methyl ester, 3,000 mmol/l ethylamine, and 0.1 g/ml of immobilized GGT cells at pH 10 and 50°C. Under these conditions, the immobilized cells were continuously used ten times, yielding an average glutamic acid γ-methyl ester to theanine conversion rate of 69.3%. Bead activity did not change significantly the first six times they were used, and the average conversion rate during the first six instances was 87.2%. The immobilized cells exhibited favourable operational stability.     

Bioconversion of D-galactose to D-tagatose: continuous packed bed reaction with an immobilized thermostable L-arabinose isomerase and efficient purification by selective microbial degradation

The continuous enzymatic conversion of D-galactose to D-tagatose with an immobilized thermostable L-arabinose isomerase in packed-bed reactor and a novel method for D-tagatose purification were studied. L-arabinose isomerase from Thermoanaerobacter mathranii (TMAI) was recombinantly overexpressed and immobilized in calcium alginate. The effects of pH and temperature on D-tagatose production reaction catalyzed by free and immobilized TMAI were investigated. The optimal condition for free enzyme was pH 8.0, 60°C, 5 mM MnCl(2). However, that for immobilized enzyme was pH 7.5, 75°C, 5 mM MnCl(2). In addition, the catalytic activity of immobilized enzyme at high temperature and low pH was significantly improved compared with free enzyme. The optimum reaction yield with immobilized TMAI increased by four percentage points to 43.9% compared with that of free TMAI. The highest productivity of 10 g/L h was achieved with the yield of 23.3%. Continuous production was performed at 70°C; after 168 h, the reaction yield was still above 30%. The resultant syrup was then incubated with Saccharomyces cerevisiae L1 cells. The selective degradation of D-galactose was achieved, obtaining D-tagatose with the purity above 95%. The established production and separation methods further potentiate the industrial production of D-tagatose via bioconversion and biopurification processes.     

NADH production from NAD+ with a formate dehydrogenase system involving immobilized cells of a methylotrophic Arthrobacter strain.

A convenient and economical method of NADH production from NAD+ has been established using a formate dehydrogenase system involving immobilized cells of a methanol-utilizing bacterium. Arthrobacter sp, KM62. Four kinds of cell entrapment were studied. An immobilized cell preparation showing a high NADH production activity was obtained by entrapment in a kappa-carrageenan gel lattice. The NADH-producing activity of the immobilized cells was investigated under various conditions. The NADH-producing activity was evoked on the addition of Triton X-100 to the reaction mixture. The conditions for the continuous production of NADH with an immobilized cell column were also investigated. When a reaction mixture containing 10 mumol (6.63 mg) ml-1 NAD+ was passed through the column (1.2 x 20 cm) containing 1.62 g (as dry weight) of immobilized cells, at a space velocity of 0.125 at 35 degrees C, complete conversion was attained.     

Conversion of Glycerol to Dihydroxyacetone by Immobilized Whole Cells of Acetobacter xylinum

Enzymatic production of dihydroxyacetone (DHA) was studied by immobilization of the whole cells of acetic acid bacteria capable of oxidizing glycerol to DHA. Acetobacter xylinum A-9 cells immobilized in a polyacrylamide gel were selected as the most favorable enzyme preparation. The enzymatic properties of immobilized cells converting glycerol to DHA were investigated and compared with those of intact cells. The optimum pH for the immobilized cells was broad (4.0 to 5.5), whereas the intact cells had a narrow pH optimum at 5.5. The thermal stability of the immobilized cells was somewhat higher than that of the intact cells. Apparent K_m values for glycerol with both intact and immobilized cells were about equal, 6.3 × 10⁻² to 6.5 × 10⁻² M. The complete conversion of glycerol to DHA was achieved within 40 h under optimum conditions, and pure crystalline DHA was readily isolated from the reaction mixture with over 80% yield.     

Effect of environmental growth conditions on plasmid stability, plasmid copy number, and catechol 2,3-dioxygenase activity in free and immobilized Escherichia coli cells

In order to better understand the high plasmid stability in immobilized recombinant E. coli cells, the effects of dilution rate on the pTG201 plasmid stability, the copy number, and the catechol 2,3-dioxygenase (encoded by XyIE gene) production were, at first, studied in free E. coli W3101 continuous cultures in minimal media. It was found that decreasing specific growth rate increased the plasmid copy number and the catechol 2,3-dioxygenase activity but the stability decreased. In continuous culture with immobilized cells, an increase was shown in plasmid copy number and catechol 2,3-dioxygenase activity probably due to the distribution of growth in the gel beads. Besides mechanical properties of gel beads which may allow limited cell divisions, the increase in plasmid copy number is involved in enhanced plasmid stability in immobilized cells. In the same way, an experiment conducted in LB medium dealing with competition between pTG201-free and pTG201-containing E. coli B cells was described. It was shown that the competition was not more pronounced in gel bead compared to a free system. The effects of nutritional limitations on pTG201 plasmid stability and catechol 2,3-dioxygenase activity during chemostat cultivations in free and immobilized E. coli B cells were also investigated. It was found that immobilization of cells increased the stability of pTG201 even under glucose, nitrogen, or phosphate limited cultures. However in the case of magnesium depleted culture, pTG201 was shown to be relatively instable and a decrease in viable cell number during the immobilized continuous culture was observed. By contrast to the free system, the catechol 2,3-dioxygenase activity increased in immobilized cells under all culture conditions used.