Silicone-immobilized biocatalysts effective for bioconversions in nonaqueous media.

A hydrophobic silicone polymer could be effectively applied to immobilization of two kinds of biocatalysts operating in organic media. Horse liver alcohol dehydrogenase, which was solubilized in a small amount of water, or deposited on water-filled hydrophilic particles, was immobilized in this material. This configuration of the preparation involving finely dispersed aqueous phase permitted a simple packed-bed operation for the enzymatic oxidation of alcohol and reduction of aldehyde with a coupled-substrate NAD(H) recycling in n-hexane. Another example was the immobilization of Nocardia corallina which catalysed epoxidation of liquid alkenes such as 1-tetradecene, 1-octene, and styrene in the presence of n-hexadecane. In order to adjust the hydrophobicity-hydrophilicity balance of the support, it was effective to immobilize the cells in a mixed matrix composed of silicone polymer and Ca-alginate gel. The optimum composition of the mixed matrix, which yielded the highest productivity of epoxide, was 80-90% silicone + 20-10% alginate for the production of 1,2-epoxytetradecane, 40-50% silicone + 60-50% alginate for 1,2-epoxyoctane, and almost 0% silicone + 100% alginate for styrene oxide. This significant change of the optimum composition was primarily associated with the degree of substrate inhibition.     

Importance of solute partitioning in biphasic oxidation of benzyl alcohol by free and immobilized whole cells of pichia pastoris

Using free and immobilized whole cells of Pichia pastoris, the biocatalytic oxidation of benzyl alcohol was investigated in different two-phase systems. This reaction was strongly influenced by both the substrate and product inhibitions, and the production rate of benzaldehyde in the aqueous system became maximum at the initial substrate concentration of ca. 29 g/L with the aldehyde formation less than 4 to 5 g/L even after a longer reaction period. The reaction rates in the two-liquid phase systems were predominantly determined by the partitioning behaviors of the substrate and product between the two phases rather than by enzyme deactivation by the organic solvents. In the two-liquid phase systems, consequently, the organic solvent acted as a reservior to reduce these inhibitory effects, and it was essential to select the organic solvent providing the optimal partitioning of the substrate into the aqueous phase as well as the preferential extraction of the product into the organic phase. The whole cells immobilized in a mixed matrix composed of silicone polymer [>50% (v/v)] and Ca alginate gel (<50%) worked well in the xylene and decane media, providing comparable activities with the free cells. The production rate of aldehyde was also influenced by the solute partitioning into the hydrophilic alginate phase where the cells existed. (c) 1994 John Wiley & Sons, Inc.     

Enantioselective hydrolysis of epichlorohydrin using whole Aspergillus niger ZJB-09173 cells in organic solvents

The enantioselective hydrolysis of racemic epichlorohydrin for the production of enantiopure (S)-epichlorohydrin using whole cells of Aspergillus niger ZJB-09173 in organic solvents was investigated. Cyclohexane was used as the reaction medium based on the excellent enantioselectivity of epoxide hydrolase from A. niger ZJB- 09173 in cyclohexane. However, cyclohexane had a negative effect on the stability of epoxide hydrolase from A. niger ZJB-09173. In the cyclohexane medium, substrate inhibition, rather than product inhibition of catalysis, was observed in the hydrolysis of racemic epichlorohydrin using A. niger ZJB-09173. The racemic epichlorohydrin concentration was markedly increased by continuous feeding of substrate without significant decline of the yield. Ultimately, 18.5% of (S)-epichlorohydrin with 98 percent enantiomeric excess from 153.6 mM of racemic epichlorohydrin was obtained by the dry cells of A. niger ZJB-09173, which was the highest substrate concentration in the production of enantiopure (S)-epichlorohydrin by epoxide hydrolases using an organic solvent medium among the known reports.     

Production of propene oxide in an organic liquid-phase immobilized cell reactor

Some major restrictions of the production of propene oxide in an organic liquid-phase immobilized cell packed-bed reactor were quantified, and techniques were investigated to enhance the epoxide production rates. Propene-epoxidizing Mycobacterium cells were entrapped in calcium alginate gel and contacted with the substrates, propene and oxygen, which were dissolved in a continuous organic phase, n-hexadecane. The effects of product inhibition by the toxic epoxide—microbial consumption of propene oxide and immobilized cell deactivation—restricted severely the accumulation of the epoxide in the recirculation reactor system and could be predicted using a simple mathematical model. Epoxide inhibition was reduced by absorbing the product in the gas phase in old di-n-octyl phthalate. The resulting increase in propene oxide production agreed with model calculations. An alternating supply of propene and a co-substrate (ethene) prolonged the half-life of the immobilized cells. Using 50 g dry weight of cells, 1.5 g stereospecific propene oxide was produced in two days, of which 1.0 g was absorbed in the di-n-octyl phthalate phase.     

Optimization of the microbial synthesis of dihydroxyacetone in a semi-continuous repeated-fed-batch process by in situ immobilization of Gluconobacter oxydans

The effect of in situ immobilization of Gluconobacter oxydans on a novel carrier material in a repeated-fed-batch operated packed-bed bubble-column bioreactor for the production of the fine chemical dihydroxyacetone was investigated experimentally. The carrier material were biocompatible, durable, coated Ralu-rings. The coating was a porous silicone matrix with satisfactory wetting characteristics. Settling of cells was relatively rapid. The cells were protected from abrasion caused by shear forces. A sufficiently high oxygen supply rate to the immobilized cells was provided due to the high oxygen permeability of the silicone matrix. The immobilized biomass was estimated to be about 65% of the total biomass contained in the bioreactor after 18 days of operation. The observed space-time yield was approx. 76% higher compared to a similar process which was performed without an optimized fermentation medium. Compared to previous experiments with a trickle-bed bioreactor, the space-time yield was approx. 3.7 times higher. A typical time course of the immobilization process was observed: after an induction phase, a transition phase followed which later on gave way to a nearly linear accumulation phase. A stationary phase with regard to the amount of immobilized active cells, however, was not reached. Hence, a higher bioreactor performance than observed could be expected at longer operation times.     

Application of immobilized cells ofThermoanaerobium brockii for stereoselective reductions of oxo-acid esters

Summary Cells ofThermoanaerobium brockii were immobilized by entrapment methods as easy-to-handle biocatalyst for stereoselective reductions of oxo-acid esters. Different matrix materials were tested: agarose, k-carrageenan, alginate, polyacrylamide and polyurethanes. The two latter matrices allowed useful lifetimes of the immobilized biocatalysts of more than 2 months at thermophilic operation temperatures (around 65°C). Permeabilization of cells did not improve the catalytic activity. Immobilization of the cells did not enhance the thermostability. Only after a considerable period of operation could the immobilized biocatalysts be fed with medium lacking the complex substrates yeast extract and tryptone. Compared with freely suspended cells, reaction rates were lower. The immobilized system proved to be a relatively stable easy-to-handle biocatalyst, however, the freely suspended cells were superior with respect to flexibility of application and reaction velocity.     

Hybridoma cells in a protein-free medium within a composite gel perfusion bioreactor

A composite gel system has been developed combining the chemical and physical properties of calcium alginate and agarose gels. The results of growing composite gel immobilized hybridoma SPO1 cells in a protein-free medium within a fluidized-bed perfusion bioreactor are presented in this paper. During the continuous operation of this system, the total cell density reached 3.9×10⁷ cells per ml of beads (viability 79.6%). The specific productivity of monoclonal antibody of the immobilized hybridoma cells reached more than 1.5 g per 10⁶ viable cells per hour, compared with 0.5 for non-immobilized viable cells grown in a one liter agitated bioreactor with the same medium. Significant increases in cell metabolic activities, including substrate utilization and byproduct formation, were also observed. Leaching of materials from the beads was evident and the major fraction of released materials was alginate.     

Alginate as immobilization matrix and stabilizing agent in a two-phase liquid system: application in lipase-catalysed reactions.

Alginate was evaluated as an immobilization matrix for enzyme-catalyzed reactions in organic solvents. In contrast to most hydrogels, calcium alginate was found to be stable in a range of organic solvents and to retain the enzyme inside the gel matrix. In hydrophobic solvents, the alginate gel (greater than 95% water) thus provided a stable, two-phase liquid system. The lipase from Candida cylindracea, after immobilization in alginate beads, catalysed esterification and transesterification in n-hexane under both batch and continuous-flow conditions. The operational stability of the lipase was markedly enhanced by alginate entrapment. In the esterification of butanoic acid with n-butanol, better results were obtained in the typical hydrophilic calcium alginate beads than in less hydrophilic matrices. The effects of substrate concentration, matrix area, and polarity of the substrate alcohols and of the organic solvent on the esterification activity were examined. The transesterification of octyl 2-bromopropanoate with ethanol was less efficient than that of ethyl 2-bromopropanoate with octanol. By using the hydrophilic alginate gel as an immobilization matrix in combination with a mobile hydrophobic phase, a two-phase liquid system was achieved with definite advantages for a continuous, enzyme-catalysed process.     

Enhanced cell attachment and osteoblastic activity by P-15 peptide-coated matrix in hydrogels

The cells in bone grow on a composite matrix made up of mineral and organic (mainly type-I collagen) components. In this study, anorganic bone mineral (ABM) particles were coated with a cell-binding domain of type-I collagen (P-15 peptide) to mimic the bone matrix components and suspended in injectable hyaluronate (Hy) hydrogels. The ABM/P-15/Hy was compared to ABM/Hy-the same matrix without P-15 peptide. Osteoblast-like HOS cells migrated through the hydrogels around ABM/P-15 or ABM particles; however, more cells adhered to ABM/P-15/Hy particles, and the cells formed better surface coverage and had more stress fibers on ABM/P-15/Hy. HOS cells cultured on ABM/P-15/Hy had increased osteogenic gene expression for alkaline phosphatase and bone morphogenetic proteins, and deposited more mineralized matrix. Studies with two different hydrogels (carboxymethylcellulose and sodium alginate) showed similar enhanced cell attachment and mineralization. The studies suggest that the ABM/P-15 in hydrogels can be used as an injectable biomimetic matrix to facilitate bone repair.     

Bioacetylation of Seaweed Alginate

Seaweed alginate was acetylated by intact, resting cells of Pseudomonas syringae ATCC 19304. Maximum acetylation of this polymer occurred at a pH of 6.0 and a temperature of 25 deg C. Aeration and gluconic acid were required for an optimal reaction. A reactor which contained carbon-immobilized cells was constructed to continuously acetylate alginate. The maximal yield of acetylation was about 90%, and the half-life of this system was 6.5 days.     

Osteogenic Differentiation of Human Mesenchymal Stem Cells in Mineralized Alginate Matrices

Mineralized biomaterials are promising for use in bone tissue engineering. Culturing osteogenic cells in such materials will potentially generate biological bone grafts that may even further augment bone healing. Here, we studied osteogenic differentiation of human mesenchymal stem cells (MSC) in an alginate hydrogel system where the cells were co-immobilized with alkaline phosphatase (ALP) for gradual mineralization of the microenvironment. MSC were embedded in unmodified alginate beads and alginate beads mineralized with ALP to generate a polymer/hydroxyapatite scaffold mimicking the composition of bone. The initial scaffold mineralization induced further mineralization of the beads with nanosized particles, and scanning electron micrographs demonstrated presence of collagen in the mineralized and unmineralized alginate beads cultured in osteogenic medium. Cells in both types of beads sustained high viability and metabolic activity for the duration of the study (21 days) as evaluated by live/dead staining and alamar blue assay. MSC in beads induced to differentiate in osteogenic direction expressed higher mRNA levels of osteoblast-specific genes (RUNX2, COL1AI, SP7, BGLAP) than MSC in traditional cell cultures. Furthermore, cells differentiated in beads expressed both sclerostin (SOST) and dental matrix protein-1 (DMP1), markers for late osteoblasts/osteocytes. In conclusion, Both ALP-modified and unmodified alginate beads provide an environment that enhance osteogenic differentiation compared with traditional 2D culture. Also, the ALP-modified alginate beads showed profound mineralization and thus have the potential to serve as a bone substitute in tissue engineering.     

Hydrogel-perfluorocarbon composite scaffold promotes oxygen transport to immobilized cells

Cell encapsulation provides cells a three-dimensional structure to mimic physiological conditions and improve cell signaling, proliferation, and tissue organization as compared to monolayer culture. Encapsulation devices often encounter poor mass transport, especially for oxygen, where critical dissolved levels must be met to ensure both cell survival and functionality. To enhance oxygen transport, we utilized perfluorocarbon (PFC) oxygen vectors, specifically perfluorooctyl bromide (PFOB) immobilized in an alginate matrix. Metabolic activity of HepG2 liver cells encapsulated in 1% alginate/10% PFOB composite system was 47-104% higher than alginate systems lacking PFOB. A cubic model was developed to understand the oxygen transport mechanism in the alginate/PFOB composite system. The theoretical flux enhancement in alginate systems containing 10% PFOB was 18% higher than in alginate-only systems. Oxygen uptake rates (OURs) of HepG2 cells were enhanced with 10% PFOB addition under both 20% and 5% O2 boundary conditions, by 8% and 15%, respectively. Model predictions were qualitatively and quantitatively verified with direct experimental OUR measurements using both a perfusion reactor and oxygen sensing plate, demonstrating a greater OUR enhancement under physiological O2 boundary conditions (i.e., 5% O2). Inclusion of PFCs in an encapsulation matrix is a useful strategy for overcoming oxygen limitations and ensuring cell viability and functionality both for large devices (>1 mm) and over extended time periods. Although our results specifically indicate positive enhancements in metabolic activity using the model HepG2 liver system encapsulated in alginate, PFCs could be useful for improving/stabilizing oxygen supply in a wide range of cell types and hydrogels.     

Enhanced production of plumbagin in immobilized cells of Plumbago rosea by elicitation and in situ adsorption

Cell cultures of Plumbago rosea were immobilized in calcium alginate and cultured in Murashige and Skoog's basal medium containing 10 mM CaCl(2) for the production of plumbagin, an important medicinal compound. Studies were carried to find out the impact of immobilization on the increased accumulation of this secondary metabolite. Immobilization in calcium alginate enhanced the production of plumbagin by three, two and one folds compared to that of control, un-crosslinked alginate and CaCl(2) treated cells respectively. Cell loading at a level of 20% to the polymer volume (Na-alginate) was optimal and maximum plumbagin was obtained. At higher cell loading (40-50%), lower plumbagin accumulation was noticed. Addition of 200 mg l(-1) chitosan as an elicitor to the immobilized cells resulted in eight and two folds higher accumulation of plumbagin over control and immobilized cells. Also, more than 70% of the plumbagin was released into the medium, which is highly desirable for easy recovery of the product. Sucrose utilization rate of the cells was higher when cells were subjected to in situ product removal using Amberlite XAD-7. This may indicate that the toxicity of plumbagin was reduced on cells when it was removed from the medium. Cells subjected to combined treatments of chitosan, immobilization and in situ extraction showed a synergistic effect and yielded 92.13 mg g(-1) DCW of plumbagin which is 21, 5.7, 2.5 times higher than control, immobilized, immobilized and elicited cells respectively.     

Encapsulation of Ketoprofen and Ketoprofen Lysinate by Prilling for Controlled Drug Release

In this paper, ketoprofen and ketoprofen lysinate were used as model drugs in order to investigate release profiles of poorly soluble and very soluble drug from sodium alginate beads manufactured by prilling. The effect of polymer concentration, viscosity, and drug/polymer ratio on bead micromeritics and drug release rate was studied. Ketoprofen and ketoprofen lysinate loaded alginate beads were obtained in a very narrow dimensional range when the Cross model was used to set prilling operative conditions. Size distribution of alginate beads in the hydrated state was strongly dependent on viscosity of drug/polymer solutions and frequency of the vibration. The release kinetics of the drugs showed that drug release rate was related with alginate concentration and solubility of the drug. Alginate solutions with concentration higher than 0.50% (w/w) were suitable to prepare ketoprofen gastro-resistant formulation, while for ketoprofen lysinate alginate, concentration should be increased to 1.50% (w/w) in order to retain the drug in gastric environment. Differential scanning calorimetry thermograms and Fourier transform infrared analyses of drug-loaded alginate beads indicated complex chemical interactions between carboxyl groups of the drug and polymer matrix in drug-loaded beads that contribute to the differences in release profile between ketoprofen and ketoprofen lysinate. Total release of the drugs in intestinal medium was dependent on the solubility of the drug and was achieved between 4 and 6 h.     

Azotobacter vinelandii lacking the Na+-NQR activity: a potential source for producing alginates with improved properties and at high yield

The mutant ATCN4 strain of Azotobacter vinelandii, which lacks the Na(+)-NQR activity and results in an alginate overproduction (highly mucoid phenotype), was cultured in shake flasks in minimal and rich medium, and the chemical composition and rheological properties of the alginate were determined. Mutant ATCN4 exhibited a high efficiency for sucrose conversion to alginate and PHB accumulation, reaching yields that were 3.6- and 1.6-fold higher than those obtained from the wildtype cultures in minimal medium (Burk's sucrose, BS). The alginate produced by ATCN4 in the minimal medium had a high degree of acetylation (≥4 %) and a low G/M ratio (=2) with respect to the polymer synthesised in the rich medium (BS with yeast extract) (degree of acetylation = 0 % and G/M ratio of 4.5). The alginate produced in the minimal medium exhibited a pronounced pseudoplastic behaviour and a higher G* module in comparison to that observed in the alginate obtained in the cultures using a rich medium. The ATCN4 mutant culture in the minimal medium promoted the synthesis of a polymer of improved rheological quality in terms of its mechanical properties. These characteristics make this mutant a valuable source for producing alginates with improved or special properties.     

Manipulation of the acetylation degree of Azotobacter vinelandii alginate by supplementing the culture medium with 3-(N-morpholino)-propane-sulfonic acid

AIMS: The aim of this study was to characterize the influence of 3-(N-morpholino)-propane-sulfonic acid (MOPS) on alginate production by Azotobacter vinelandii and its chemical composition (particularly its acetylation degree), as well as on the rheological behaviour of alginate-reconstituted solutions. METHODS AND RESULTS: Cultures were grown in 500-ml flasks containing 90 ml of medium supplemented with MOPS in concentrations ranging from 0 to 13.6 mmol l(-1). The acetylation degree of the alginate was significantly influenced by the MOPS concentration, obtaining an alginate with an acetylation degree of 1.4% when 13.6 mmol l(-1) of MOPS was added to the medium. This value was twice as high as that obtained when no MOPS was used. The higher acetylation of the polymer resulted in higher viscosity of alginate solutions, having a more pronounced pseudoplastic behaviour. CONCLUSIONS: MOPS added to the culture medium determines the acetyl content of the alginate and thus, the physico-chemical properties of the polymer. SIGNIFICANCE AND IMPACT OF THE STUDY: These changes in the functional properties of the polymer can be very valuable in specific applications of alginate in the food and pharmaceutical fields.     

Effect of metal ion concentration on a biological reactor

Saccharomyces cerevisiae (yeast) cells were employed as a source of alcohol dehydrogenase in the NAD(+)-to-NADH reaction. The cells were immobilized in calcium alginate monofilament fibers and used in a biological reactor. The alginate could not be heat sterilized since temperatures above 80 degrees C caused the polymer chains to degrade. The same proved true for the high pH necessary for the reaction, but the alginate strength was increased by Ba(2+) solution treatment. X-ray probe analysis showed that about 30% of the Ca(2+) sites exchanged with the Ba(2+) ions. The Ba(2+) ions (as well as the Ca(2+) ions) permeabilized the cells and increased the reaction rate. Long term trials showed that Ba(2+) ions were slowly elutriated from the fiber biocatalyst, causing a drop in reaction rate. The trend certainly was reversible as far as the fiber was concerned. It is assumed that the permeabilization of the cells by the Ba(2+) ions was a reversible process.     

Silica nanotubes-doped alginate gel for yeast alcohol dehydrogenase immobilization

A novel alginate–silica nanotubes (ALG–SiNTs) composite was prepared through the incorporation of silica nanotubes (SiNTs) into the alginate (ALG) gel followed by Ca²⁺ cross-linking for encapsulating yeast alcohol dehydrogenase (YADH, EC 1.1.1.1) from Saccharomyces cerevisiae. Pre-adsorption of YADH onto the surface of SiNTs before encapsulating in alginate gel was adopted to circumvent the enzyme leakage. AFM and SEM characterization confirmed that YADH molecules were substantially adsorbed on the SiNTs. SEM and EDX studies showed that the SiNTs homogenously distributed in alginate matrix. The enzyme leakage from ALG–SiNTs–YADH composite was remarkably reduced about 50% compared to that of ALG–YADH composite. Meanwhile, the optimum reaction condition, catalytic activity and kinetic parameters of immobilized YADH in ALG–SiNTs composite were studied. The results showed that stronger affinity between substrates and enzyme, higher activity retention, improved storage and operational stability were achieved when YADH was immobilized in ALG–SiNTs composite instead of ALG–YADH composite.     

Selective alginate degradation by marine bacteria associated with the algal genusSargassum

Summary Alginase-secreting bacteria associated with actively growing tissues of the marine Phaeophyta speciesSargassum fluitans andS. natans have been isolated and evaluated for their ability to degrade alginate (ALG), carboxymethylcellulose, and agar. Of seven isolates selected for their ability to grow on 2% agar containing 1% sodium alginate, none were able to grow on either 2% agar or 2% agar supplemented with 0.1% carboxymethylcellulose. Two of these with fermentative potential, i.e., ALG-A and ALG-G, showed selective activities with respect to their ability to degrade native alginate and/or take up the products resulting from alginate degradation. The ALG-A isolate was able to rapidly degrade native alginate with the generation of a stable polymer fraction and small oligouronides, most of which were dissimilated for growth. The ALG-G isolate was able to completely degrade native alginate with the accumulation of significant quantities of unsaturated dimeric and trimeric oligouronides. A limit polymer was generated from the action of a polymannuronan-specific extracellular alginate lyase purified from exponential cultures of the ALG-A organism. This product proved to be an effective substrate for the alginate lyase activity obtained from the medium of exponential phase cultures of the ALG-G isolate, and upon incubation with concentrated and dialyzed ALG-G medium was converted to the products that were observed to accumulate in the medium of the ALG-G isolate grown on native alginate. These organisms represent examples of the microflora associated with actively growingSargassum tissues, each with a selective ability to degrade and dissimilate the biomass of the marine brown algae.     

Biological degradation of Ascophyllum nodosum

The alginate forms the major structural component of the cell wall and the intercellular matrix of the brown alga Ascophyllum nodosum. Successful biological degradation of A. nodosum would largely depend on the dissolution of the alginate, but reactive compounds in the alga such as polyphenols may also have toxic effects on the microbial population involved. Aerobic and anaerobic batch reactors, operated at 35°C and pH 7, were fed milled A. nodosum, nutrients and inocula adapted to seaweed degradation. The dominant factor for conversion of organic matter during anaerobic digestion was the inhibitory effect of the polyphenols on alginate lyases and methane production. Probably, the relative large fraction of high molecular weight polyphenols (>10 kDa) in this alga gave efficient binding of proteins during digestion. The anaerobic degradation was greatly stimulated when the polyphenols were fixed with low amounts of formaldehyde. An accumulated content of guluronate in the remaining alginate indicated that Ca-crosslinking also limited the guluronate lyase access to the polymer. In contrast, the aerobic digestion of alga gave no increase in the guluronate content of the residual alginate. Compared to anaerobic conditions, the phenols had a much lower influence on the hydrolytic rate of organic matter during aerobic conditions. This revised version was published online in August 2006 with corrections to the Cover Date.