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.     

Continuous production of 7-Aminocephalosporanic acid by immobilized cells of Pseudomonas diminuta

The continuous production of 7-ACA with immobilized whole cells of P. diminuta was carried out in a tubular glass reactor at optimal conditions. The biocatalyst was prepared by gel entrapment using chitosan, geletin and agar as immobilizing agents. The micro-organism was characterized in terms of cell-to-carrier ratios, diffusional properties, as well as storage and operational stability, etc., towards the production of 7-ACA. It was found that a cell to carrier ratio of 0.45 and a flow rate of 120 mL h^?1, respectively, were most suitable for the conversion of CPC to 7-ACA. Operational stability was highest with chitosan, with a half life of 2106 h followed by gelatin, then agar as immobilizing supports.     

Continuous production of L-aspartic acid by immobilized aspartase

Various methods were tried for the immobilization of aspartase, and the preparation having the highest activity was obtained when partially purified aspartase from Escherichia coli was entrapped into polyacrylamide gel Iattice. Enzymatic properties of the immobilized aspartase were investigated and compared with those of the native aspartase. With regard to optimum pH, temperature, concentration of Mn⁺⁺, kinetic constants and heat stability, no marked difference was observed between the native and immobilized aspartases. By employing an enzyme column packed with the immobilized aspartase, conditions for continuous production of L -aspartic acid from ammonium fumarate were investigated. When a solution of 1M ammonium fumarate (pH 8.5, containing 1mM MnCl₂) was passed through the aspartase column at the flow rate of SV = 0.08 at 37°C, the highest rate of reaction was attained. From the column effluents, L-aspartic acid was obtained in a good yield.     

Continuous production of 6-aminopenicillanic acid from penicillin by immobilized microbial cells

Summary For continuous production of 6-aminopenicillanic acid (6-APA) the microbial cells ofEscherichia coli ATCC 9637 having high penicillin amidase (penicillin amidohydrolase, E.C. 3. 5. 1. 11) activity were immobilized by entrapment in a polyacrylamide gel lattice.Enzymatic properties of penicillin amidase of the immobilizedE. coli cells were investigated and compared with those of the intact cells. With regard to optimal pH and temperature, no marked difference was observed. The heat stability was somewhat increased by immobilization of the cells.The enzyme activity of the immobilized cell column was stable, and its half-life was 17 days at 40°C and 42 days at 30°C. From the effluent of the column, 6-APA was easily obtained in a good yield.Abbreviations 6-APA 6-aminopenicillanic acid - BIS N,N-methylenebisacrylamide - DMAPN -dimethylaminopropionitrile - SV space velocity     

Continuous itaconic acid production by immobilized biocatalysts.

The continuous itaconic acid production from sucrose with Aspergillus terreus TKK 200-5-3 mycelium immobilized on polyurethane foam cubes was optimized in column bioreactors using statistical experimental design and empirical modelling. The highest itaconic acid product concentration calculated on the basis of the obtained model was 15.8 g l-1 in the investigated experimental area, when sucrose concentration was 13.5%, aeration rate 150 ml min-1 and residence time 178 h. From sucrose with immobilized A. terreus TKK 200-5-3 mycelium itaconic acid production was stable for at least 4.5 months in continuous column bioreactors. In comparison, using glucose as substrate and immobilized A. terreus TKK 200-5-1 mycelium as biocatalyst similar stability was obtained with higher product concentration. The omission of copper sulphate from the production medium gave the highest itaconic acid product concentration (26 g l-1) from 9% glucose with 0.25% ammonium nitrate and 0.095% magnesium sulphate.     

Enzymatic synthesis of L-malic acid from fumaric acid using immobilized Escherichia coli cells

Optimal conditions were chosen for cultivation of Escherichia coli 85 cells with a rather high fumarate-hydratase activity on a cheap medium containing no edible raw material. An active biocatalyst for the synthesis of L-malic acid from fumaric acid was obtained based on E. coli 85 cells immobilized in carrageenan. The enzymatic synthesis of L-malic acid from potassium fumarate was kinetically studied and optimized. Some thermodynamic parameters of fumaric acid hydration into malic acid were determined. A technique for assaying the reaction mixture was developed that involved high performance liquid chromatography.     

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.     

Continuous ethanol production by immobilized cells of Zymomonas mobilis

Summary Studies have been carried out with a highly productive strain of Zymomonas mobilis in an immobilized cell reactor using both Ca alginate and -carrageenan as supporting matrices. Productivities above 50 g/l/h have been found at ethanol concentrations in excess of 60 g/l. With immobilized cells of Z. mobilis, there was a decline of approximately 30s% in activity after 800 h operation.     

Continuous production of glutathione by immobilized Saccharomyces cerevisiae cells

Summary Glutathione was continuously produced by an immobilized Saccharomyces cerevisiae IFO 2044 cell column. The production of glutathione was strongly influenced by the level of activity of the glycolytic pathway. This activity was maintained constant by the addition of NAD.Abbreviations ADP adenosine-5-diphosphate - ATP adenosine-5-triphosphate - NAD nicothinamide adenine dinucleotide     

Continuous production of steroid glycoalkaloids by immobilized plant cells

Summary Non-permeablilized cells ofSolanum aviculare were immobilized by their adsorption and covalent linkage on activated polymeric adsorbent. The retention of extracellular production of steroid glycoalkaloids was studied in a packed-column recycle reactor.     

Acetic acid production by immobilized acetobacter cells

Summary Using a pulsed gas and liquid flow and with cells directly adsorbed on to a suitably-formed support, aerobic transformations can be carried out in a fixed-cell reactor with significant gain in efficiency. Immobilized cells of Acetobacter on cordierite can produce acetic acid at a high rate which, at different dilution rates, may be limited either by product inhibition or by oxygen transfer requirements.     

Study of an enzyme membrane reactor with immobilized fumarase for production of L-malic acid

The conversion of fumaric acid into L-malic acid by fumarase immobilized in a membrane reactor was analyzed experimentally. The enzyme was entrapped in asymmetric capillary membranes made of polysulfone. The performance of the reactor was evaluated in terms of conversion degree, reaction rate, and stability. The influence of operating conditions, such as amount of immobilized enzyme, substrate concentration, residence time, and axial flow rate, were investigated. The kinetic parameters K(m), V(max), and k(+2) were also measured. The stability of the immobilized enzyme was very good, showing no activity decay during more than 2 weeks of continuous operation.     

Continuous production of glucoamylase by immobilized growing cells ofAureobasidium pullulans

Summary Yeast-like cells ofAureobasidium pullulans were immobilized in Ca-alginate gel beads and employed for continuous production of glucoamylase in a fluidized-bed reactor (250 ml working volume). After an activation time of 48 h, to allow the in situ germination of the fungal blastospores, the reactor was operated continuously for over 150 h. A steady state enzyme concentration of 1.2–1.3 U ml^–1 of glucoamylase activity and an enzyme volumetric productivity of ca. 130 U ml^–1 h^–1 were obtained at a medium flow rate of 26 ml h^–1. Enzyme activity and volumetric productivity were influenced by fermentation conditions such as inoculum size and airflow rate.     

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 oxytetracycline by immobilized growing Streptomyces rimosus cells

Summary Streptomyces rimosus cells were immobilized with urethane prepolymers and used in the production of oxytetracycline. Based on the criteria for oxytetracycline productivity, cell growth in gels, cell leakage from gels and mechanical strength of gel, a hydrophilic prepolymer, PU-1, the main chain of which was polyethylene glycol (molecular weight, approximately 1500) was employed as gel material among 11 kinds of urethane prepolymers. Use of glucose-free medium for cultivation of PU-1-entrapped cells increased the production rate of oxytetracycline and minimized cell leakage from the gels. When the gel-entrapped cells lost activity, treatment of the cell-entrapping gels with saline or 70% ethanol resulted in recovery of the oxytetracycline productivity. Continuous oxytetracycline fermentation using PU-1-entrapped growing cells was successfully achieved in air-bubbled reactor for at least 35 days with reactivation of the cells.     

Continuous production of NADP by immobilized Brevibacterium ammoniagenes cells.

Whole cells of Brevibacterium ammoniagenes IAM 1645 having the polyphosphate NAD-kinase were successfully immobilized in a polyacrylamide gel lattice. The immobilized cells were activated by treatment with organic solvents or detergents. The pH optimum of the immobilized cells for the production of NADP was 7.0, and divalent metal ions were required to maintain the elevated activity of polyphosphate NAD-kinase. Highly pure NADP was continuously produced in high yield by the immobilized cell column. The half-life of this column was about eight days.     

Continuous production of NADP by immobilized Achromobacter aceris cells.

Several microorganisms having higher nicotinamide adenine dinucleotide kinase (NAD kinase, EC 2.7.1.23) activity were immobilized into polyacrylamide gel lattices. The enzyme activity field by immobilization was highest in Achromobacter aceris AKU 0120. By the incubation of the immobilized A. aceris cells at pH 4.0, the NAD kinase activity increased and the adenosine triphosphate (ATP)-degradation activity disappeared completely. Enzymatic properties of the immobilized A. aceris cells were investigated and compared with those of intact cells. The optimal pH and the optimal temperature of immobilized cells were the same as those of intact cells. Immobilized cell NAD kinase was more stable than that of intact cells. The operational half-life of immobilized cells was 20 days when the substrate solution was passed through a column packed with immobilized cells at a flow rate which gives a space velocity (SV) of 0.1 hr-1 at 37 degrees C. On the other hand, the half-life of the intact cells was only 6 hr.     

Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.     

Continuous production of Emmental cheese flavours and propionic acid starters by immobilized cells of a propionic acid bacterium

Summary Characteristics of a continuous reactor with Propionibacterium cells entrapped with Ca-alginate are described. For a dilution rate D=0.45 h^–1, the gel produced 8 g.l^–1 for volatile fatty acids and 0.18 g.l^–1 for diacetylacetoin. The fiability of the process and its ability to produce propionic acid bacterium starter at the rate 4.10⁹ cells.l^–1 gel.h^–1 maked it attractive for industrial applications.