Hydrolysis of whey by whole cells of Kluyveromyces bulgaricus immobilized in calcium alginate gels and in hen egg white

Summary Whey hydrolysis was compared in column reactors containing whole yeast cells immobilized in Ca-alginate or in hen egg white in relation to cell -galactosidase activity, flow rates, temperature and time. With cells of 1.3 U/mg dry weight (ONPG method) immobilized in Ca-alginate, 80% hydrolysis was obtained at 4° and 20° C with, respectively 0.50 and 1.65 bed volume/H; the values were 0.2 and 0.74 with cells entrapped in hen egg white. When the flow rate was expressed as ml/H/g wet yeast, no significant difference was observed between both matrices and 80% hydrolysis was reached with a flow rate 1.7 and 5 according to the temperature. The best performance was achieved by the yeast egg white reactor. At 4°C, hydrolysis decreased by 10% after 13 days; by 20% after 17 days. The presence of lactose transport inhibitors in whey did not significantly influence lactose hydrolysis.M. Decleire et al.: Hydrolysis of whey by immobilized whole cells of Kluyveromyces bulgaricus     

Continuous penicillin production by Penicillium chrysogenum immobilized in calcium alginate beads

Summary A high penicillin-producing Penicillium chrysogenum strain immobilized in calcium alginate beads was used for continuous penicillin fermentation in a bubble column and in a conical bubble fermentor. The fermentation was limited by the growth rate, dilution rates and the stability of the alginate beads. The immobilized cells lost their ability to produce penicillin in the bubble column after 48 h from beginning of the continuous fermentation. In the conical bubble fermentor the immobilized cells remained active for more than 7 days. This bioreactor ensured a good distribution of nutrients and oxygen as well as a higher mechanical stability of the alginate beads.     

Unexpected distribution of immobilized microorganisms within alginate beads

Immobilization refers to the prevention of free cell movement by natural or artificial means. It has always been assumed that immediately after an immobilization procedure is performed, cells are distributed homogeneously in the beads that entrap them. However, in this study, Escherichia coli and Trichoderma asperellum distribution in alginate-gel beads was found to be nonhomogeneous. In fact, there was a greater presence of cells on the surface of the alginate beads than in their cores.     

Protease production by immobilized growing cells of Serratia marcescens and Myxococcus xanthus in calcium alginate gel beads

Summary Serratia marcescens and Myxococcus xanthus cells were immobilized in calcium alginate gel beads. Immobilization under various conditions had no effect on the extracellular proteolytic activity of S. marcescens cells. Protease production seemed rather to depend on the free cells in the medium. However, the stability over time of enzyme production was enhanced, as immobilization increased protease production half-life from 5 to 12 days. On the other hand, Myxococcus xanthus produced proteases inside the gel beads which could diffuse into the medium. The proteolytic activity increased as a function of the initial cell content of the beads and of the bead inoculum. Compared to free cells, immobilized cells of Myxococcus xanthus could produce 8 times more proteolytic activity, with a very low free-cell concentration in the medium.     

Culture parameters affecting xylitol production by Debaryomyces hansenii immobilized in alginate beads

Yeast immobilization offers operational advantages such as high cell concentration, and some drawbacks related to cell leaking and restricted mass transfer inside particles. The influence of bead size, chitosan, bead charge, volume of liquid media, and the use of corncob hydrolyzates and vinasses as culture medium were analyzed on xylitol production by Debaryomyces hansenii immobilized in alginate beads. The results showed a profuse growth of free cells, accounting 75–95% of total biomass, but electron micrographs revealed the generation of a dense biofilm with hyphal morphology at the bead surface and a very low intraparticular growth. Xylitol production was not affected by the size of particle; however chitosan had a negative effect. The use of corn cob as carbon source and twofold diluted vinasses as economic nutrients incremented xylitol concentration to 13.7 g L^?1 (Y_P/S = 0.56 g g^?1; Q_P = 0.29 g L^?1 h^?1). The best conditions corresponded to high bead charges and intermediate liquid volumes (44 g Na-alginate and 110 mL liquid medium). These results showed the feasibility of employing these cheap substrates, reflected the importance of the microaerobical conditions, and pointed to the favorable effect of cell immobilization on the metabolism of xylitol production.     

Biotransformation of cladribine using a stabilized biocatalyst in calcium alginate beads

Cladribine is a nucleoside analogue widely used in the pharmaceutical industry for the treatment of several neoplasms, including hairy-cell leukemia among others. This compound has also shown efficacy in the treatment of autoimmune diseases such as rheumatoid arthritis and multiple sclerosis. In this work, a green bioprocess for cladribine biosynthesis using immobilized Arthrobacter oxydans was developed. The microorganism was stabilized by entrapment immobilization in the natural matrix alginate. Different reaction parameters were optimized obtaining a biocatalyst able to achieve cladribine bioconversion values close to 85% after 1 hr, the shortest reaction times reported so far. The developed bioprocess was successfully scaled-up reaching a productivity of 138 mg L⁻¹ hr⁻¹. Also, the biocatalyst was stable for 5 months in storage and in 96 hr at operational conditions.     

Semicontinuous penicillin production by two Penicillium chrysogenum strains immobilized in calcium alginate beads

Summary The growth rates of immobilized Penicillium chrysogenum strains are important in their application to semicontinuous penicillin production. Immobilized P. chrysogenum strains produced about 10–15% less biomass but about 1–2 times more penicillin than free suspended mycelia.In a chemically defined medium an industrial P. chrysogenum strain, S₁, produced about 10–12 times more penicillin than strain ATCC 12690. In a complex medium the immobilized P. chrysogenum S₁ produced about 12% penicillin more than in shaken cultures. In bubble column fermentations, penicillin production was 163% higher in the complex medium than in the chemically defined medium.     

Production of glucoamylase using Aspergillus phoenicus immobilized in calcium alginate beads

Summary As a means of better exploiting the growth-dissociated nature of glucoamylase synthesis, a production process in which the growth phase was separated from the enzyme synthesis phase has been developed. Immobilized mycelia arising from a 6-day-old culture of conidia immobilized in calcium alginate beads could be subsequently used repeatedly to produce glucoamylase in a second step using a Dextran T-10 medium. Glucoamylase production was sustained over five sequential batches in a 19-day period and immobilized mycelia remained confined to the subsurface of the beads. Offprint requests to: C. Kuek     

Neutralization of acidic drainage by Cryptococcus sp. T1 immobilized in alginate beads

We isolated Cryptococcus sp. T1 from Lake Tazawa’s acidic water in Japan. Cryptococcus sp. T1 neutralized an acidic casamino acid solution (pH?3.0) and released ammonia from the casamino acids to aid the neutralization. The neutralization volume was estimated to be approximately 0.4 mL/h. The casamino acids’ amino acids decreased (1.24→0.15 mM); ammonia increased (0.22→0.99 mM). We neutralized acidic drainage water (1 L) from a Tamagawa River neutralization plant, which was run through the column with the T1-immobilized alginate beads at a flow rate of 0.5 mL/min, and observed that the viscosity, particle size and amounts of the alginate beads affected the acidic drainage neutralization with an increase of the pH value from 5.26 to 6.61 in the last fraction. An increase in the Al concentration decreased Cryptococcus sp. T1’s neutralization ability. After 48 h, the pH of acidic water with 50 mg/L Al was apparently lower than that without Al. Almost no pH increase was observed at 75 mg/L.     

Production of toluene cis-diol by immobilized pseudomonas putida UV4 cells in barium alginate beads

In the present study, we have investigated the biotransformation of toluene to its cis-dihydrodiol (cis-diol) with immobilized Pseudomonas putida UV4 cells using different conditions of immobilization with a view to improving its production. The choice of alginate and its concentration for the immobilization of the cells were found to be the most important factors affecting the production of toluene cis-diol. The concentration of minerals and oxygen in the reaction medium and the methodology of substrate addition were investigated and the optimal conditions were defined. Once the optimal conditions for biotransformations and entrapment were determined, a packed-bed and fluidized-bed reactor were evaluated for the biotransformation process. The results using air as the gas supply showed an increase in the total production from 0.15 mol cis-diol · g⁻¹ dry cell weight (dcw) in the packed-bed reactor to 0.28 mol cis-diol · g⁻¹ dcw in the fluidized-bed reactor. When pure oxygen was used in place of air in the fluidized-bed reactor, a dramatic increase in total production up to a maximum of 6.1 mol cis-diol · g⁻¹ dcw using a medium flow rate of 100 ml min⁻¹ was achieved. Under optimal conditions, a maximum rate of production of 86.9 mmol cis-diol g⁻¹ dcw h⁻¹ was achieved for 48 h. This was seven times higher than the rate previously reported in the literature and for a much longer period of time; consequently, the overall production observed was more than 75 times higher than the values reported in the literature.     

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.     

Biological ferrous sulfate oxidation by A. ferrooxidans immobilized on chitosan beads

The immobilization of Acidithiobacillus ferrooxidans cells on chitosan and cross-linked chitosan beads and the biooxidation of ferrous iron to ferric iron in a packed-bed bioreactor were studied. The biofilm formation was carried out by using a glass column reactor loaded with chitosan or cross-linked chitosan beads and 9 K medium previously inoculated with A. ferrooxidans cells. The immobilization cycles on the carrier matrix with the bioreactor operating in batch mode were compared. Then, the reactor was operated using a continuous flow of 9 K medium at different dilution rates. The results indicate that the packed-bed reactor allowed increasing the flow rate of medium approximately two fold (chitosan) and eight fold (chitosan cross-linked) without cells washout, compared to a free cell suspension reactor used as control, and to reach ferric iron productivities as high as 1100 and 1500 mg l(-1) h(-1) respectively. Scanning electron microscopy micrographs of the beads, infrared spectroscopy and the X-ray diffraction patterns of precipitates on the chitosan beads were also investigated.     

Steroid transformation by living cells immobilized in calcium alginate

Summary Whole cells of Arthrobacter simplex were immobilized in a living state in calcium alginate gel. The bacteria showed steroid-¹-dehydrogenase activity and the production of prednisolone from cortisol was investigated. The ¹-dehydrogenase activity of the immobilized cells could be increased about ten-fold by incubation in nutrient media (e.g., containing 0.5% peptone abd 0.2% glucose). The reason for this activation was examined and it was found that the immobilized cells were capable of multiplying when supplied with nutrients. Furthermore, provided that an inducer, cortisol, was present, the steroid-¹-dehydrogenase activity increased in proportion to the increase in the number of cells and it was thus concluded that microbial growth was the cause of activation.Experiments on repeated, batch-wise pseudocrystallofermentation with immobilized A. simplex cells also showed that immobilized cells could be advantageously used for pseudocrystallofermentation of steroids.     

Hydrolysis of lactose solutions and wheys by whole cells of Kluyveromyces bulgaricus

Summary Some factors affecting the hydrolysis of lactose solution and whey by whole cells of Kluyveromyces bulgaricus were studied. The K_m values were 59 mM and 32 mM for whole cells and cell-free extracts respectively. Optimum hydrolysis activity was observed at 48°C. At this temperature, 80% hydrolysis was obtained in lactose solution and whey after 3.5 and 9 min respectively by yeast cells (15 mg/ml) with an activity of 1.13 U/mg. Protein concentration in whey did not have an inhibitory effect. In whey permeate, cells were reused eight times with a hydrolysis degree of more than 80% but in lactose phosphate buffer, the hydrolysing capacity was lost quickly.     

Production of isomaltooligosaccharides by a-glucosidase immobilized in chitosan beads and by polyethyleneimine-glutaraldehyde treated mycelia of Aspergillus carbonarious

Partially purified a-glucosidase from Aspergillus carbonarious, immobilized on glutaraldehyde-activated chitosan beads in a packed bed reactor, produced isomaltooligosaccharides at a yield of 60% (w/w) using 30% (w/v) maltose solution. Using intact mycelia attached with polyethyleneimine-glutaraldehyde, produced isomaltooligosaccharides at a yield of 46% (w/w) using 30% (w/v) maltose solution. Batchwise reaction stabilities were improved for chitosan beads immobilized enzyme and polyethyleneimine-glutaraldehyde treated mycelia as compared to mycelia without any treatment.     

Direct electrochemistry and electrocatalysis of heme proteins immobilized on gold nanoparticles stabilized by chitosan

Three heme proteins, myoglobin, hemoglobin, and cytochrome c, have been adsorbed onto chitosan-stabilized gold nanoparticles (Chit-Aus) modified Au electrode via a molecule bridge like cysteine. UV-vis spectra indicated that the proteins on Chit-Aus films retained near-native secondary structures. The fabricated procedures and electrochemical behaviors of proteins on such an interface were characterized with electrochemical impedance spectra and cyclic voltammetric techniques. It was demonstrated that Chit-Aus film could not only offer a friendly environment to immobilize protein molecules but also enhance the electron transfer ability between protein molecules and underlying electrode. The effects of scan rate and pH on the electrochemical behaviors of each heme protein are discussed in detail. The resultant electrode displayed an excellent electrocatalytic response to the reduction of H(2)O(2), long-term stability, and good reproducibility.     

Comparison of some properties of free and immobilized alpha-amylase by Aspergillus sclerotiorum in calcium alginate gel beads

Some properties of immobilized alpha-amylase by Aspergillus sclerotiorum within calcium alginate gel beads were investigated and compared with soluble enzyme. Optimum pH and temperature were found to be 5.0 and 40 degrees C, respectively, for both soluble and immobilized enzymes. The immobilized enzyme had a better Km value, but kcat/Km values were the same for both enzymes. Entrapment within calcium alginate gel beads improved, remarkably, the thermal and storage stability of alpha-amylase. The half life values of immobilized enzyme and soluble enzyme at 60 degrees C were 164.2, and 26.2 min, respectively. The midpoint of thermal inactivation (Tm) shifted from 56 degrees C (for soluble enzyme) to 65.4 degrees C for immobilized enzyme. The percentages of soluble starch hydrolysis for soluble and immobilized alpha-amylase were determined to be 97.5 and 92.2% for 60 min, respectively.     

Ethanol production from whey permeate by immobilized yeast cells

The ability of two yeast strains to utilize the lactose in whey permeate has been studied. Kluyveromyces marxianus NCYC 179 completely utilized the lactose (9.8%), whereas Saccharomyces cerevisiae NCYC 240 displayed an inability to metabolize whey lactose for ethanol production. Of the two gel matrices tested for immobilizing K. marxianus NCYC 179 cells, sodium alginate at 2% (w/v) concentration proved to be the optimum gel for entrapping the yeast cells effectively. The data on optimization of physiological conditions of fermentation (temperature, pH, ethanol concentration and substrate concentration) showed similar effects on immobilized and free cell suspensions of K. marxianus NCYC 179, in batch fermentation. A maximum yield of 42.6 g ethanol l^?1 (82% of theoretical) was obtained from 98 g lactose l^?1 when fermentation was carried at pH 5.5 and 30°C using 120 g dry weight l^?1 cell load of yeast cells. These results suggest that whey lactose can be metabolized effectively for ethanol production using immobilized K. marxianus NCYC 179 cells.     

Semi-continuous lactic fermentation of whey by Lactobacillus bulgaricus

Semi-continuous tests of lactic fermentation of whey by Lactobacillus buigaricus were carried out using a mixture of hydrolysed milk and vitamins. The volume of the Inoculum varied from 20% to 50% of the reactor working volume. A Monod-like equation correlates the lactic acid productivity and the volume fraction of inoculum.The authors are with the Centro de Desenvolvimento Biotecnológico de Santa Catarina (Biotechnological Development Centre of Santa Catarina), R. Princesa isabel, 114, 89200, Joinville, SC, Brazil. CDEB. L.A. Kulay was an undergraduate student, in 1989, of the Escola de Engenharia Mauá (Mauá Engineering School), São Caetano do Sul, SP, Brazil. W. Borzani is the corresponding author.