Hydrogen peroxide as an oxygen source for immobilized Gluconobacter oxydans converting glycerol to dihydroxyacetone

Summary A flow injection analysis (FIA) system with amperometric detection was developed for measuring hydrogen peroxide which was used as an oxygen source for immobilized cells. A constant concentration of peroxide in the reactor was maintained by processing the analytical signal in a computer programmed as a PI-regulator. The concentration of dissolved oxygen was followed using a commercial Clark-electrode. The simultaneous measurements of hydrogen peroxide and dissolved oxygen are discussed with respect to process control.Conversion of glycerol to dihydroxyacetone by Gluconobacter oxydans immobilized in calcium alginate was used as a model system.Initial specific productivity increased with increasing hydrogen peroxide concentration. However, decreases in viable counts, enzymatic activities and overall productivities were noted. Various techniques for improving operational stability are discussed.     

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.     

Oxygen supply to immobilized cells

Summary Oxygen supply is a critical point in technical processes when aerobic cells are used in immobilized preparations. In this study p-benzoquinone is used as a substitute for oxygen in the oxidation of glycerol to dihydroxyacetone by immobilized Gluconobacter oxydans cells. The reaction rate was much higher when p-benzoquinone was used compared to when oxygen was used. In an experiment with free cells p-benzoquinone gave a rate more than four times that of oxygen, and with immobilized cells the difference was even greater. p-benzoquinone is more effective than oxygen because it gives a higher maximal reaction rate (the reason for this fact is discussed) and because it is more soluble in water than oxygen. The operational stability of the process is comparatively good. In one experiment the productivity decreased from 60 to 10 mmol/h·g over an 8-day period when p-benzoquinone was used. When oxygen was used in a similar experiment the productivity decreased from 14 to 6 mmol/h·g. The byproduct formed from p-benzoquinone, hydroquinone, can be oxidized to p-benzoquinone which can be re-used. Seven succesive regenerations of p-benzoquinone were performed without any loss of efficiency.     

Oxygen supply to immobilized cells: 2. Studies on a coimmobilized algae—bacteria preparation with in situ oxygen generation

A coimmobilized mixed culture of algae, Chlorella pyrenoidosa, and bacteria, Gluconobacter oxydans, has been studied. The conversion of glycerol to dihydroxyacetone(1,3-dihydroxy-2-propanone), catalysed by the bacteria, was used to indicate the oxygen supply in the immobilized preparation. The oxygen produced by the algae in the coimmobilized preparation was used by the bacteria more effectively than when the cells were immobilized separately and mixed within the reactor. A preparation consisting of only bacteria and no algae was much less effective. The coimmobilized preparation was used in the continuous production of dihydroxyacetone for six days without any significant loss of activity.     

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 β-cyclodextrin from starch by highly stable cyclodextrin glycosyltransferase immobilized on chitosan

Cyclodextrin glycosyltransferase (CGTase) from Thermoanaerobacter sp. was covalently immobilized on glutaraldehyde-activated chitosan spheres and used in a packed bed reactor to investigate the continuous production of β-cyclodextrin (β-CD). The optimum temperatures were 75 °C and 85 °C at pH 6.0, respectively for free and immobilized CGTase, and the optimum pH (5.0) was the same for both at 60 °C. In the reactor, the effects of flow rate and substrate concentration in the β-CD production were evaluated. The optimum substrate concentration was 4% (w/v), maximizing the β-CD production (1.32 g/L) in a flow rate of 3 mL/min. In addition, the biocatalyst had good operational stability at 60 °C, maintaining 61% of its initial activity after 100 cycles of batch and 100% after 100 h of continuous use. These results suggest the possibility of using this immobilized biocatalyst in continuous production of CDs.     

Tagatose production by immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant in a packed-bed bioreactor

Using immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant (Gali 152), we found that the galactose isomerization reaction was maximal at 70 degrees C and pH 7.0. Manganese ion enhanced galactose isomerization to tagatose. The immobilized cells were most stable at 60 degrees C and pH 7.0. The cell and substrate concentrations and dilution rate were optimal at 34 g/L, 300 g/L, and 0.05 h(-1), respectively. Under the optimum conditions, the immobilized cell reactor with Mn2+ produced an average of 59 g/L tagatose with a productivity of 2.9 g/L.h and a conversion yield of 19.5% for the first 20 days. The operational stability of immobilized cells with Mn2+ was demonstrated, and their half-life for tagatose production was 34 days. Tagatose production was compared for free and immobilized enzymes and free and immobilized cells using the same mass of cells. Immobilized cells produced the highest tagatose concentration, indicating that cell immobilization was more efficient for tagatose production than enzyme immobilization.     

Transformation of rifamycin B with immobilized rifamycin oxidase of Curvularia lunata

Rifamycin oxidase of Curvularia lunata was immobilized on polyacrylamide gel. The optimum pH and temperature for immobilized enzyme reaction were 6.5 and 50 °C, respectively. Enzyme stability increased on immobilization and the half lives of immobilized enzyme preparations at 30 and 40 °C were 30 and 11.5 d, respectively. With 2.5 mm beads diffusional resistances were observed. Reusability studies showed that 1 mm size beads gave a higher rate of transformation in comparison with 2 or 2.5 mm beads.     

GLYCEROL KINASE AND DIHYDROXYACETONE KINASE IN RAT BRAIN

—The enzymatic phosphorylation of glycerol and dihydroxyacetone by ATP to sn-glycerol-3-phosphate and dihydroxyacetone phosphate respectively in various subcellular fractions of rat brain was studied. A sensitive radiochemical assay was used where the labelled phosphorylated products were separated from the radioactive substrates by high voltage paper electrophoresis and the radioactivity in these compounds determined. Using this assay the glycerol kinase (EC 2.7.1.30) activity was found to be associated with the mitochondrial fraction of the brain. Under optimum conditions 2.45 nmol of glycerol was phosphorylated/min per mg of protein. The K_m for glycerol was 70 μm at pH 7. This mitochondrial enzyme, like other glycerol kinases from different sources, also phosphorylated dihydroxyacetone. Under optimum conditions 1.7 nmol of dihydroxyacetone phosphate was formed/min per mg of mitochondrial protein. The K_m for dihydroxyacetone was 0.6 mm . Glycerol kinase activity was also present in the cytoplasm of brain. However, the specific activity of this enzyme in cytosol is about 15% of the mitochondrial glycerol kinase. Compared to glycerol, dihydroxyacetone was phosphorylated by ATP in cytoplasm at a much higher rate. The pH optimum for this soluble dihydroxyacetone kinase was much lower (pH 6.5) than that of the soluble or mitochondrial glycerol kinase (pH 10.0). Using ammonium sulfate, brain cytoplasm was fractionated to yield a fraction in which the dihydroxyacetone kinase was enriched 2–3 fold with no glycerol kinase activity. Under optimum conditions 1.0 nmol of dihydroxyacetone was phosphorylated/min per mg protein. The K_m for dihydroxyacetone was 60 μm . This cytosol fraction was also found to phosphorylate d -glyceraldehyde and l -glyceraldehyde at a rate of 30–40% to that of the dihydroxyacetone phosphorylation. The properties and the possible metabolic role of these enzymes in brain are discussed.     

Polyelectrolyte complex formation mediated immobilization of chitosan-invertase neoglycoconjugate on pectin-coated chitin

Saccharomyces cerevisiae invertase, chemically modified with chitosan, was immobilized on pectin-coated chitin support via polyelectrolyte complex formation. The yield of immobilized enzyme protein was determined as 85% and the immobilized biocatalyst retained 97% of the initial chitosan-invertase activity. The optimum temperature for invertase was increased by 10 °C and its thermostability was enhanced by about 10 °C after immobilization. The immobilized enzyme was stable against incubation in high ionic strength solutions and was 4-fold more resistant to thermal treatment at 65 °C than the native counterpart. The biocatalyst prepared retained 96 and 95% of the original catalytic activity after ten cycles of reuse and 74 h of continuous operational regime in a packed bed reactor, respectively.     

Regulation of exoprotease production by temperature and oxygen in Vibrio alginolyticus

The production of an extracellular collagenase and an alkaline protease by Vibrio alginolyticus during stationary phase was inhibited by a temperature shift from 30 to 37°C and by a lack of oxygen. The stability of the exoproteases was unaffected by incubation at 37°C and aeration. The optimum growth temperature for the V. alginolyticus strain was 33.5°C Aeration enhanced the rate of growth of exponential phase cells. Temperature and oxygen did not affect the growth of stationary phase cells when the exoproteases were being produced. Macromolecular synthesis in stationary phase cells was not affected by temperature. There was no rapid release of the exoproteases after temperature shift down and chloramphenicol inhibited the production of the enzymes when added at time of temperature shift down from 37 to 30°C. The regulation of exoprotease production by temperature and oxygen was specific and has implications regarding the ecology of V. alginolyticus. Cerulenin, quinacrine and O-phenanthroline inhibited the production of the exoproteases.     

Immobilization of Haloferax mediterranei aldolase by cross-linking in a proteinic matrix: stability and halophilic characteristics

Fructose-1,6-bisphosphate (FBP) aldolase (EC 4.1.2.13) of Haloferax mediterranei was immobilized by treating the cell extract in the presence of 10% BSA, with the cross-linking reagent, 0.5% glutaraldehyde for 15min, with the retention of 60% of its original activity. The immobilized preparation exhibited a shift in the temperature optimum from 55°C to 65°C. The enzyme showed enhanced stability towards inactivation by radiation and storage (0–5°C) on immobilization. Immobilization also made the enzyme less halophilic, reducing its denaturation on prolonged storage in a non-salt medium, as well as exhibiting optimal activity at a lower KCl concentration (0.5m) as compared to the soluble enzyme (1–2m).     

Chemical oxygen demand reduction in a whey fermentation

Summary Preparations of living Pseudomonas denitrificans cells immobilized in alginate gel were used in the denitrification of water. In the presence of an exogenous carbon source the entrapped microorganisms reduced nitrate and nitrite to gaseous products and to achieve complete reduction, carbon to nitrogen ratios of over two were required. The effects on denitrification of particle size and the number of bacteria in the gel were investigated. Apparent K_m values for nitrate and nitrite reduction were calculated for free and immobilized cells. When the immobilized cells were incubated in nutrient media, an increase in reduction rate was observed and this was shown to be caused by the growth of cells within the gel particles. Immobilized P. denitrificans cells retained 75% of their initial nitrate reduction capacity after 21 days of storage at +4°C. The operational stability of the alginate-immobilized cells was studied both in batch and in a column which was operated continuously. A column (45 g of alginate-cell fibers in 80 ml) denitrified a high nitrate drinking water (100 mg NO₃/l) with a rate of 300 ml of nitrate and nitrite free water/day/g of gel. The half life for nitrate reduction was estimated to be 30 days.     

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     

Production of adenine arabinoside by gel-entrapped cells of Enterobacter aerogenes in water-organic cosolvent system

Summary Gel-entrapped whole cells of Enterobacter aerogenes, which has a transglycosylation activity, were used to produce adenine arabinoside from uracil arabinoside and adenine, in an appropriate water-organic cosolvent system. Cells of E. aerogenes entrapped with a hydrophilic photo-crosslinkable resin prepolymer, ENT-4000, or a urethane prepolymer, PU-6, had a high and stable transglycosylation activity. To improve the poor solubility in water of the substrate (adenine) and product (adenine arabinoside), dimethyl sulfoxide was selected as the cosolvent based on the criteria of operational stability of the immobilized biocatalyst and solubility of both substrate and product. Addition of 40% dimethyl sulfoxide to the reaction mixture permitted use of a high substrate concentration range which gave high productivity under homogeneous reaction conditions. The immobilized cells of E. aerogenes exhibited a markedly improved operational stability, retaining their initial level of activity during repeated use for at least 35 days at 60°C in 40% dimethyl sulfoxide. When the reaction was carried out with 150 mM uracil arabinoside and 50 mM adenine as the substrates, the yield of adenine arabinoside was maintained at 100% based on the molar ratio of adenine, throughout the reaction.Abbreviations used AraA adenine arabinoside - AraU uracil arabinoside     

Glycerol production by immobilized cells of Saccharomyces cerevisiae

Summary Cells of Saccharomyces cerevisiae were immobilized in K-Carrageenan. Addition of sodium sulfite to the fermentation medium up to four percent led to glycerol yields of 25 to 27 g/l at temperatures below 31°C.These results demonstrate that it is possible to direct the metabolism of immobilized cells from ethanol fermentation to glycerol fermentation by sulfite.     

Kinetic behaviour of α-galactosidase produced by Absidia griseola: a comparison between free and immobilized forms of the enzyme

In this research the characteristics of free (partially purified) and immobilized (mould pellets of Absidia griseola) -galactosidase have been investigated. Inhibition studies of the enzyme showed that p-nitrophenol and sucrose do not have any inhibitory effect on the enzyme, but that galactose is a competitive inhibitor. In the immobilized form, inhibition was lower than in the free enzyme and the level of inhibition decreased as the temperature increased. The activity and stability of free and immobilized enzyme were investigated with respect to temperature, and the results showed that the optimal temperature range of the free enzyme was 45–50 °C, while the immobilized enzyme had an optimum at 55–60 °C. The optimum pH for the free enzyme was 6.0 and the value was decreased to 5.0 by immobilizing. The experimental effectiveness factors were found to be represented as a single function of the modified Thiele modulus, including parameters such as pellet size, enzyme concentration in the pellets and substrate concentration. Both experimental and theoretical data concerning effectiveness factors are nearly the same.     

EFFECT OF FERMENTATION PARAMETERS ON BIO-ALCOHOLS PRODUCTION FROM GLYCEROL USING IMMOBILIZED Clostridium pasteurianum: AN OPTIMIZATION STUDY

This article addresses the issue of effect of fermentation parameters for conversion of glycerol (in both pure and crude form) into three value-added products, namely, ethanol, butanol, and 1,3-propanediol (1,3-PDO), by immobilized Clostridium pasteurianum and thereby addresses the statistical optimization of this process. The analysis of effect of different process parameters such as agitation rate, fermentation temperature, medium pH, and initial glycerol concentration indicated that medium pH was the most critical factor for total alcohols production in case of pure glycerol as fermentation substrate. On the other hand, initial glycerol concentration was the most significant factor for fermentation with crude glycerol. An interesting observation was that the optimized set of fermentation parameters was found to be independent of the type of glycerol (either pure or crude) used. At optimum conditions of agitation rate (200 rpm), initial glycerol concentration (25 g/L), fermentation temperature (30°C), and medium pH (7.0), the total alcohols production was almost equal in anaerobic shake flasks and 2-L bioreactor. This essentially means that at optimum process parameters, the scale of operation does not affect the output of the process. The immobilized cells could be reused for multiple cycles for both pure and crude glycerol fermentation.     

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).