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 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.     

Glycolytic pathway as an ATP generation system and its application to the production of glutathione and NADP

Efficient ATP generation is required to produce glutathione and NADP. Hence, the generation of ATP was investigated using the glycolytic pathway of yeast. Saccharomyces cerevisiae cells immobilized using polyacrylamide gel generated ATP from adenosine, consuming glucose and converting it to ethanol and carbon dioxide. Under optimal conditions, the ATP-generating activity of immobilized yeast cells was 7.0 μmol h^?1 ml^?1 gel. A column packed with these immobilized yeast cells was used for continuous ATP generation. The half-life of the column was 19 days at a space velocity of (SV) 0.3 h^?1 at 30°C. The properties of glutathione- and NADP-producing reactions coupled with the ATP-generating reaction were investigated. Escherichia coli cells with glutathione synthesizing activity and Brevibacterium ammoniagenes cells with NAD kinase activity were immobilized in a polyacrylamide gel lattice. Under optimal conditions, the immobilized E. coli cells and immobilized B. ammoniagenes cells produced glutathione and NADP at the rates of 2.1 and 0.65 μmol h^?1 ml^?1 gel, respectively, adding ATP to the reaction mixture. In order to produce glutathione and NADP economically and efficiently, the glutathione- and NADP-producing reactions were finally coupled with the ATP-generating reaction catalysed by immobilized S. cerevisiae cells. To compare the productivities of glutathione and NADP, and to compare the efficiency of ATP utilization for the production of these two compounds, the two reactor systems, co-immobilized cell system and mixed immobilized cell system, were designed. As a result, these two compounds were also found to be produced by these two kinds of reactor systems. Using the data obtained, the feasibility and properties of ATP generation by immobilized yeast cells are discussed in terms of the production of glutathione and NADP.     

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.     

Glutathione production coupled with an ATP regeneration system

Summary Escherichia coli cells possessing glutathione synthetase and acetate kinase activities were immobilized with carrageenan gel. To enhance the operational stability, immobilized cells were treated with hardening agent, glutaraldehyde in the presence of hexamethylenediamine. The continuous production of glutathione was investigated using the column packed with immobilized Escherichia coli cell preparations. Glutathione was continuously produced by this column in the presence of acetyl phosphate and the half-life of this column was calculated to be 8 days at the flow rate of S.V.=0.1 h^–1 at 37°C.     

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 l-phenylalanine from acetamidocinnamic acid using co-immobilized cells of Corynebacterium sp. and Paracoccus denitrificans

In order to produce l-phenylalanine efficiently from acetamidocinnamic acid with immobilized microbial cells, a two-step enzyme reaction using the acetamidocinnamate amidohydrolase activity of Corynebacterium sp. C-23 cells and the aminotransferase activity of Paracoccus denitrificans pFPr-1 cells was investigated. It was found that the useage of co-immobilized Corynebacterium sp. and P. denitrificans cells with κ-carrageenan was superior to that of the mixture of immobilized Corynebacterium sp. cells and immobilized P. denitrificans cells. When the space velocity was 0.06 h⁻¹ at 30°C, 147 mml-phenylalanine were produced with a 98% conversion ratio from acetamidocinnamic acid. The half-life of the l-phenylalanine-forming activity of the column was calculated to be ≈ 14 days at 30°C.     

A newly isolated fungal strain used as whole‐cell biocatalyst for biodiesel production from palm oil

A strain of Aspergillus niger isolated from atmospherically exposed bread and Jatropha curcas seed was utilized as a whole‐cell biocatalyst for palm oil methanolysis to produce fatty acid methyl esters (FAME), or biodiesel. The A. niger strain had a lipase activity of 212.58 mU mL^?1 after 144 h incubation at 25 °C with an initial pH value of 6.5, using 7% polypeptone (w/w on basal medium) as the nitrogen source and 3% olive oil (w/w on basal medium) as a carbon source. The A. niger cells spontaneously immobilized within polyurethane biomass support particles (BSPs) during submerged fermentation. Thereafter, the methanolysis of palm oil was achieved via a three‐step addition of methanol in the presence of BSPs‐immobilized with A. niger cells. The influence of water content, reaction temperature and enzyme concentration on reaction rate was investigated. An 8% water content and a temperature of 40 °C in the presence of 30 immobilized BSPs, resulted in an 87% FAME yield after 72 h.     

Microbial transformation of validamycin A to valienamine by immobilized cells

Immobilized Pseudomonas sp. HZ519 cells have been used for transformation of validamycin A to valienamine and the degradation pathway of validamycin A by Pseudomonas sp. HZ519 has also been studied. Substrate inhibition in immobilized cell system was avoided. An average of 8.6 g L^?1 valienamine concentration was obtained when concentration of validamycin A was increased up to 120 g L^?1. Through a treatment of the immobilized cells with 0.3 mol L^?1 substrate, the activity of the immobilized cells was increased distinctly. Compared with free cells, the productivity of valienamine by CA-immobilized cells was improved about three times. The reusability of the immobilized cells was evaluated with repeated–batch degradation experiments. The Tiele modulus was obtained from the experimental effectiveness factor. The result showed that the degradation process in the immobilized system was governed by intraparticle diffusion and chemical reaction.     

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.     

Continuous production of l-aspartic acid from ammonium fumarate using immobilized cells by capture on the surface of nonwoven cloth coated with a pyridinium-type polymer

Cells of Escherichia coli possessing aspartase activity were immobilized by capture on the surface of nonwoven cloth coated with 10 mg/g of poly (N-benzyl-4-vinylpyridinium chloride-co-styrene), a pyridinium-type polymer. Continuous operation of a fixed-bed column reactor containing 21.7 g/l of the immobilized cells produced l-aspartic acid in 95% yield from ammonium fumarate in the case where influent solution contained 0.1 mol/l of the fumarate and space velocity was 1.36 h⁻¹ at 30°C and pH 8.9. Immobilization on the coated nonwoven cloth insignificantly affected optimal pH of the biochemical reaction. Stability of enzymic activity of the immobilized cells was much improved by use of the coated nonwoven cloth as the supporting material instead of beads of insoluble pyridinium-type resin. l-Aspartic acid was obtained in 77% yield after 160 d of continuous operation, and the initial yield was estimated to require about 500 d for halving.     

Continuous production of isomalto-oligosaccharides from maltose syrup by immobilized cells of permeabilizedAureobasidium pullulans

Continuous production of isomalto-oligosaccharides from maltose syrup by the permeabilized cells ofAureobasidium pullulans immobilized into calcium alginate gel was studied using a column reactor. The immobilized cell column maintained its full activity over 45 days when the reactor was operated at a velocity of 0.1 h^–1 at 50°C using 60%(w/v) maltose syrup as a substrate, and the maximum productivity achieved was around 60 g/1h.     

Continuous production of fructooligosaccharides using fructosyltransferase immobilized on ion exchange resin

A continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized on a high porous resin, Diaion HPA 25. The optimum pH (5.5) and temperature (55°C) of the enzyme for activity was unaltered by immobilization, and the immobilized enzyme became less sensitive to the pH change. The optimal operation conditions of the immobilized enzyme column for maximizing the productivity were as follows: 600 g/L of sucrose feed concentration, flow rate of superficial space velocity 2.7 h^?1. When the enzyme column was run at 50°C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days of continuous operation, during which high productivity of 1174 g/L·h was achieved. The kinds of products obtained using the immobilized enzyme were almost the same as those using soluble enzymes or free cells.     

Catalytic properties of the immobilized Aspergillus tamarii xylanase

Xylanase from Aspergillus tamarii was covalently immobilized on Duolite A147 pretreated with the bifunctional agent glutaraldehyde. The bound enzyme retained 54.2% of the original specific activity exhibited by the free enzyme (120 U/mg protein). Compared to the free enzyme, the immobilized enzyme exhibited lower optimum pH, higher optimum reaction temperature, lower energy of activation, higher K_m (Michaelis constant), lower V_max (maximal reaction rate). The half-life for the free enzyme was 186.0, 93.0, and 50.0 min for 40, 50, and 60°C, respectively, whereas the immobilized form at the same temperatures had half-life of 320, 136, and 65 min. The deactivation rate constant at 60°C for the immobilized enzyme is about 6.0 × 10⁻³, which is lower than that of the free enzyme (7.77 × 10⁻³ min). The energy of thermal deactivation was 15.22 and 20.72 kcal/mol, respectively for the free and immobilized enzyme, confirming stabilization by immobilization. An external mass transfer resistance was identified with the immobilization carrier (Duolite A147). The effect of some metal ions on the activity of the free and immobilized xylanase has been investigated. The immobilized enzyme retained about 73.0% of the initial catalytic activity even after being used 8 cycles.     

Adsorptive immobilization of rhodococcal cells in hydrophobized derivatives of wide-pore poly(acrylamide) cryogel

Adsorption of Rhodococcus ruber cells on columns with poly(acrylamide) cryogel (cryoPAAG) partially hydrophobized by different quantities (0.2, 1, and 5, mol %) of chemically grafted n-dodecane residues has been studied. The adsorption capacity (1.1 × 10⁹ cells/g) of gel carrier for rhodococcal cells and the optimal content (1 mol %) of hydrophobizing groups were determined. The respirometric method showed the high catalytic activity and functional stability of immobilized bacterial cells. Respiratory activity of immobilized rhodococci in the presence of a model mixture of oil hydrocarbons exceeded the respective parameter for free cells by 12–17%. Viability of rhodococcal cells adsorptionally fixed in hydrophobized cryoPAAG was maintained at a level of 93–95% after a half-year period of storage. The results may be used for development of immobilized biocatalyst for directed transformation of hydrocarbon compounds and biological purification of oil-polluted water.     

Columnar denitrification of water by immobilized Pseudomonas denitrificans cells

Summary Whole cells of Pseudomonas denitrificans, immobilized in alginate gel, were used for columnar denitrification of ground water. Ethanol was selected as a suitable carbon source and the C/N-ratio necessary for satisfactory nitrate reduction was established (1.6 mg ethanol-C/mg nitrate-N). The course of the reaction and the diffusional limitations were investigated during columnar denitrification. The mechanical integrity of the gel matrix, as judged from leakage of cells was studied. The release of cells into the effluent was effectively inhibited (<10² cells/ml) by the use of different filter devices. The operational characteristics were determined by studying a column operating for nearly four months. Theoretically, the alginate gel column should, from high nitrate drinking water (22 mg NO ₃ ^– -N/1), produce 3 1 of denitrified water/kg gel/h (wet wt.) during a period of two months. The regeneration of nitrate reduction activity by means of activation in nutrient media proved a useful tool for restoring initial activity, the gel column having shown no loss in activity at the end of the operation period.     

Immobilization of yeast cells in hydroxyethylmethacrylate gels

Summary Whole cells of Saccharomyces cerevisiae were entrapped in polymers of 2-hydroxyethylmetha-crylate and sucrose hydrolysis catalysed by its invertase was investigated.Analysis of the experimental results confirmed that diffusional resistance to mass transfer of reactant and product was not induced by immobilization.For the yeast cells in the hydrogel, invertase activity obeyed a Michaelis-Menten kinetic and the value of Km (40 mM) was the same as that for yeast cells in bulk phase.The recovery of biocatalyst activity ranged between 17% and 23%, depending on immobilization temperature; the optimum pH range was found to be slightly wider.Storage stability at refrigerator temperature was quite satisfactory; invertase half-life was 267 days. Operational stability of immobilized cells at 45°C (half-life 110 days) was almost twice that of free cells.Finally, cell distribution in the polymer, observed with a scanning electron microscope, was found to be uniform.Symbols C Active cell concentration, g/mg - Ea Activation energy, cal/mol - Kd kinetic constant of the enzyme deactivation reaction, h - Km Michaelis constant, mM - Nc Active cell amount, mg - r Enzymatic reaction rate, mol/min - S Substrate concentration, mM - t Reaction time, h or days - T Reaction temperature, °C or °K - Tp Polymerization temperature, °C - V _max Kinetic constant of enzymatic reaction, mol/min     

Heterofunctional Magnetic Metal‐Chelate‐Epoxy Supports for the Purification and Covalent Immobilization of Benzoylformate Decarboxylase From Pseudomonas Putida and Its Carboligation Reactivity

In this study, the combined use of the selectivity of metal chelate affinity chromatography with the capacity of epoxy supports to immobilize poly‐His‐tagged recombinant benzoylformate decarboxylase from Pseudomonas putida (BFD, E.C. 4.1.1.7) via covalent attachment is shown. This was achieved by designing tailor‐made magnetic chelate–epoxy supports. In order to selectively adsorb and then covalently immobilize the poly‐His‐tagged BFD, the epoxy groups (300 µmol epoxy groups/g support) and a very small density of Co²⁺‐chelate groups (38 µmol Co²⁺/g support) was introduced onto magnetic supports. That is, it was possible to accomplish, in a simple manner, the purification and covalent immobilization of a histidine‐tagged recombinant BFD. The magnetically responsive biocatalyst was tested to catalyze the carboligation reactions. The benzoin condensation reactions were performed with this simple and convenient heterogeneous biocatalyst and were comparable to that of a free‐enzyme‐catalyzed reaction. The enantiomeric excess (ee) of (R)‐benzoin was obtained at 99 ± 2% for the free enzyme and 96 ± 3% for the immobilized enzyme. To test the stability of the covalently immobilized enzyme, the immobilized enzyme was reused in five reaction cycles for the formation of chiral 2‐hydroxypropiophenone (2‐HPP) from benzaldehyde and acetaldehyde, and it retained 96% of its original activity after five reaction cycles. Chirality 27:635–642, 2015. © 2015 Wiley Periodicals, Inc.     

Production of 6-aminopenicillanic acid by immobilized Pleurotus ostreatus

Summary 6-Aminopenicillanic acid from penicillin V is produced by Pleurotus ostreatus immobilized by entrapment in a chitosan matrix. In these carriers the cell concentration increases after network formation by irreversible shrinking of the biocatalyst. Specific activity of the biocatalyst for the hydrolysis reaction is 1,31 mol.min^-1. (g wet weight of catalyst)^-1 corresponding to a relative activity of 38%. Catalytic half-life of immobilized Pl. ostreatus is 25 days compared to 2.5 days for free suspended cells.This paper is part of the Dissertation of Michael Kluge, Technical University Braunschweig 1981.     

Degradation of 2,4,6-TCP and a mixture of isomeric chlorophenols by immobilized Streptomyces rochei 303

We investigated the degradation of 2,4,6-trichlorophenol (2,4,6-TCP) by cells of Streptomyces rochei 303 immobilized on various carriers. Polycaproamide fibre was chosen as the optimal carrier for immobilization. The cells immobilized on this carrier degraded high-concentrations of individual chlorophenols and their mixtures: from mono- to pentachlorophenol including the most persistent meta-substituted derivatives. During continuous fermentation in a column with continuous substrate and air flow at a maximal degraded concentration of 2,4,6-TCP of 1 g/l and the specific flow rate of 0.08 h^–1, the efficiency of degradation was 720 mg 2,4,6-TCP/day (36 mg 2,4,6-TCP/day per gram of carrier). The above system of immobilized cells was operated continuously without any loss of activity for 2.5 months, the amount of degraded 2,4,6-TCP being 54 g. At a lower concentration of the reagent (150 mg/l) the system was operated without any decrease in its degradability and without any additional carbon source for 11 months. Correspondence to: L. A. Golovleva