Enhanced production of laccase activity by <Emphasis Type="Italic">Trametes versicolor </Emphasis>immobilized into alginate beads by the addition of different inducers

In the present paper the effect of adding veratryl alcohol and copper sulphate on laccase activity production by Trametes versicolor immobilized into alginate beads has been investigated. Employing copper sulphate as laccase inducer or supplementing the culture medium with veratryl alcohol, led to maximum values of laccase activity. However, the highest laccase activity (around 4,000 U l⁻¹) was obtained in cultures simultaneously supplemented with copper sulphate (3 mM) and veratryl alcohol (20 mM). These values implied a considerable enhancement in relation to␣control cultures without any inducer (around 200 U l⁻¹). The production of laccase by immobilized T. versicolor in a 2-l airlift bioreactor with the optimized inducer has been evaluated. Laccase activities around 1,500 U l⁻¹ were attained. The bioreactor operated for 44 days without operational problems and the bioparticles (fungus grows in alginate beads) maintained their shape throughout the fermentation. Moreover, the extracellular liquid obtained was studied in terms of pH and temperature activity and stability. On the other hand, anthracene was added in two-repeated batches in order to determine the efficiency of this process to degrade pollutants. Near complete degradation was reached in both batches. Moreover, in vitro degradation of several polycyclic aromatic hydrocarbons by crude laccase was also performed.     

Protein production using recombinant yeast in an immobilized-cell-film airlift bioreactor

A recombinant Saccharomyces cerevisiae C468/pGAC9 (ATCC 20690), which expresses Aspergillus awamori glucoamylase gene under the control of the yeast enolase I (ENO1) promoter and secretes glucoamylase into the extracellular medium, was used as a model system to investigate the effect of cell immobilization on bioreactor culture performance. Free suspension cultures in stirred-tank and airlift bioreactors confirmed inherent genetic instability of the recombinant yeast. An immobilized-cell-film airlift bioreactor was developed by employing cotton cloth sheets to immobilize the yeast cells by attachment. Enhanced enzyme productivity and production stability in the immobilized-cell system were observed. Experimental data indicated that the immobilized cells maintained a higher proportion of plasmid-bearing cells for longer periods under continuous operation. The higher plasmid maintenance with immobilized cells is possibly due to reduced specific growth rate and increased plasmid copy number. Double-selection pressure was used to select and maintain the recombinant yeast. The selected strain showed better production performance than the original strain. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 241-251, 1997.     

Production of thermostable and neutral glucoamylase using immobilized <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis>

Thermomucor indicae-seudaticae was immobilized in alginate, κ-carrageenan, agarose, agar, polyacrylamide and loofah (Luffa cylindrica) sponge (as such or coated with alginate/starch/Emerson YpSs agar), and used for the production of glucoamylase in submerged fermentation. The mycelium developed from alginate-immobilized sporangiospores secreted higher glucoamylase titres (22.7 U ml⁻¹) than those immobilized in other gel matrices and the freely growing mycelial pellets (18.5 U ml⁻¹). Loofah network provided a good support for mycelial growth, but the enzyme production was lower than that attained with alginate beads. Glucoamylase production increased with inoculum density and the optimum levels were achieved when 40 calcium alginate beads (∼5 × 10⁶ immobilized spores) were used to inoculate 50 ml production medium. The alginate bead inoculum displayed high storage stability at 4°C and produced comparable enzyme titres up to 120 days. The glucoamylase production by hyphae emerged from the immobilized sporangiospores was almost stable over eight batches of repeated fermentation. Scanning electron micrographs of alginate beads, after batch fermentation, revealed extensive mycelial growth inside and around the beads.     

Effect of calcium on immobilization of rice (<Emphasis Type="Italic">Oryza sativa</Emphasis> L.) peroxidase for bioassays in sodium alginate and Agarose gel

The direct immobilization of soluble peroxidase isolated and partially purified from shoots of rice seedlings in calcium alginate beads and in calcium agarose gel was carried out. Peroxidase was assayed for guaiacol oxidation products in presence of hydrogen peroxide. The maximum specific activity and immobilization yield of the calcium agarose immobilized peroxidase reached 2,200 U mg⁻¹ protein (540 mU cm⁻³ gel) and 82%, respectively. In calcium alginate the maximum activity of peroxidase upon immobilization was 210 mU g⁻¹ bead with 46% yield. The optimal pH for agarose immobilized peroxidase was 7.0 which differed from the pH 6.0 for soluble peroxidase. The optimum temperature for the agarose immobilized peroxidase however was 30°C, which was similar to that of soluble peroxidase. The thermal stability of calcium agarose immobilized peroxidase significantly enhanced over a temperature range of 30∼60°C upon immobilization. The operational stability of peroxidase was examined with repeated hydrogen peroxide oxidation at varying time intervals. Based on 50% conversion of hydrogen peroxide and four times reuse of immobilized gel, the specific degradation of guaiacol for the agarose immobilized peroxidase increased three folds compared to that of soluble peroxidase. Nearly 165% increase in the enzyme protein binding to agarose in presence of calcium was noted. The results suggest that the presence of calcium, ions help in the immobilization process of peroxidase from rice shoots and mediates the direct binding of the enzyme to the agarose gel and that agarose seems to be a better immobilization matrix for peroxidase compared to sodium alginate.     

Bioprocessing strategies for improving hen egg-white lysozyme (HEWL) production by recombinant Aspergillus niger HEWL WT-13-16

Hen egg-white lysozyme (HEWL) production by recombinant Aspergillus niger HEWL WT-13-16 from a cDNA under the control of the A. niger glucoamylase promoter was used as a model system. The fungal mycelium was either immobilized on porous Celite 560 micro-carrier or grown in suspension as pelleted and dispersed forms. The objective was to reduce the protease activity that adversely affects the expressed HEWL. Free suspension culture at uncontrolled pH served as the benchmark. The control of pH during growth at pH 4.0 gave rise to a greater than five-fold reduction of protease activity in suspension culture. An additional 38.5% decrease in protease activity was achieved in mycelial-pellet cultures in comparison to a 40.9% decrease in protease activity obtained with Celite 560 beads in an airlift vessel at controlled pH. The specific HEWL yields were 5.8, 5.0 and 4.1 mg/g dry wt. for the free suspension, mycelial-pellet, and Celite-560-immobilized cultures, respectively.     

Syringin production by <Emphasis Type="Italic">Saussurea medusa</Emphasis> cell cultures in a novel bioreactor

The culture of Saussurea medusa cell were cultured in an internal loop airlift bioreactor with sifter draft tube (ILABSDT) was investigated. Under the optimal culture conditions, which were inoculation size 1.5 g(d.m.) dm⁻³, aeration rate 0.3 dm³(air) dm⁻³(medium) min⁻¹, and 14 mesh sifter holes, the maximum biomass, syringin content and syringin production reached 11.7 g(d.m.) dm⁻³, 17.7 mg g⁻¹ and 206.6 mg dm⁻³, respectively. Among cell cultures in shake flask, bubble column bioreactor and ILABSDT, ILABSDT had the highest syringin productivity and reached 12.41 mg dm⁻³ d⁻¹.     

Optimization of lactic acid production by immobilized <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1

Production of lactic acid from glucose by immobilized cells of Lactococcus lactis IO-1 was investigated using cells that had been immobilized by either entrapment in beads of alginate or encapsulation in microcapsules of alginate membrane. The fermentation process was optimized in shake flasks using the Taguchi method and then further assessed in a production bioreactor. The bioreactor consisted of a packed bed of immobilized cells and its operation involved recycling of the broth through the bed. Both batch and continuous modes of operation of the reactor were investigated. Microencapsulation proved to be the better method of immobilization. For microencapsulated cells at immobilized cell concentration of 5.3 g l⁻¹, the optimal production medium had the following initial concentrations of nutrients (g l⁻¹): glucose 45, yeast extract 10, beef extract 10, peptone 7.5 and calcium chloride 10 at an initial pH of 6.85. Under these conditions, at 37 °C, the volumetric productivity of lactic acid in shake flasks was 1.8 g l⁻¹ h⁻¹. Use of a packed bed of encapsulated cells with recycle of the broth through the bed, increased the volumetric productivity to 4.5 g l⁻¹ h⁻¹. The packed bed could be used in repeated batch runs to produce lactic acid.     

Repeated-batch production of glucoamylase using recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> immobilized in a fibrous bed bioreactor

The recombinant Saccharomyces cerevisiae strain C468/pGAC9 has an unstable hybrid plasmid pGAC9, which directs production of glucoamylase. A fibrous cotton material with a good adsorption capability for recombinant S. cerevisiae cells was used as the immobilization matrix in an internal loop airlift-driven fibrous bed bioreactor (ILALFBB) system. With batch cultures in the ILALFBB, the fraction of plasmid-carrying cells was 72% after more than 2 days cultivation, which was two times higher than that in the conventional free-cell culture. Correspondingly, a high activity of glucoamylase (GA; 113 U/l) was achieved with a high productivity of 43 U/l/h. The ILALFBB system also maintained a high fraction of viable plasmid-carrying of 74% for glucoamylase production during repeated-batch cultures, achieving a high glucoamylase activity of 140 U/l with a productivity of 19–130 U/l/h in all 14 batches studied during 19.8 days. The stable and long-term glucoamylase production from the ILALFBB was attributed to the effect of cell immobilization on plasmid stability. Plasmid-carrying cells were preferentially retained in the fibrous matrix because of their ability to adhere to the fiber surface and to form cell aggregates higher than those of plasmid-free cells. The repeated batch using immobilized cell of recombinant S. cerevisiae in the ALALFBB system thus provides a feasible method for stable, long-term and high-level production of glucoamylase.     

Large-scale cultivation of adventitious roots of Echinacea purpurea in airlift bioreactors for the production of chichoric acid, chlorogenic acid and caftaric acid

Adventitious roots of Echinacea purpurea were cultured in airlift bioreactors (20 l, 500 l balloon-type, bubble bioreactors and 1,000 l drum-type bubble bioreactor) using Murashige and Skoog (MS) medium with 2 mg indole butyric acid l⁻¹ and 50 g sucrose l⁻¹ for the production of chichoric acid, chlorogenic acid and caftaric acid. In the 20 l bioreactor (containing 14 l MS medium) a maximum yield of 11 g dry biomass l⁻¹ was achieved after 60 days. However, the amount of total phenolics (57 mg g⁻¹ DW), flavonoids (34 mg g⁻¹ DW) and caffeic acid derivatives (38 mg g⁻¹ DW) were highest after 50 days. Based on these studies, pilot-scale cultures were established and 3.6 kg and 5.1 kg dry biomass were achieved in the 500 l and 1,000 l bioreactors, respectively. The accumulation of 5 mg chlorogenic acid g⁻¹ DW, 22 mg chichoric acid g⁻¹ DW and 4 mg caftaric acids g⁻¹ DW were achieved with adventitious roots grown in 1,000 l bioreactors.     

Immobilization of enzymes on crosslinked gelatin particles activated with various forms and complexes of titanium(IV) species

A number of methods of activating the surface of glutaraldehyde crosslinked gelatin beads with titanium(IV) compounds, for subsequent enzyme coupling, have been investigated. Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.1.3) was so immobilized using titanium(IV)-urea, -acrylamide, -citric acid and -lactose complexes; however, immobilized enzyme preparations with low activities were obtained (0.36–1.28 U g^?1). Activation with uncomplexed titanium(IV) chloride, however, of both moist and freeze-dried crosslinked gelatin particles resulted in highly active immobilized glucoamylase preparations (1.74–26.6 U g^?1). Dual immobilized enzyme conjugates of glucoamylase and invertase (β-d-fructofuranosidase, EC 3.2.1.26) were also prepared using this method. Invertase was served on the entrapped enzyme while glucoamylase was coupled on the surface of titanium(IV)-activated gelatin pre-entrapped invertase particles. A dual gelatin coupled glucoamylase/gelatin entrapped glucoamylase was prepared (3.8 U g^?1) and ～72.5% of the total combined activity was due to the surface bound enzyme.     

Production of xylanolytic enzymes by <Emphasis Type="Italic">Aspergillus terricola</Emphasis> in stirred tank and airlift tower loop bioreactors

Fungi producing high xylanase levels have attracted considerable attention because of their potential industrial applications. Batch cultivations of Aspergillus terricola fungus were evaluated in stirred tank and airlift bioreactors, by using wheat bran particles suspended in the cultivation medium as substrate for xylanase and β-xylosidase production. In the stirred tank bioreactor, in physical conditions of 30°C, 300 rpm, and aeration of 1 vvm (1 l min⁻¹), with direct inoculation of fungal spores, 7,475 U l⁻¹ xylanase was obtained after 36 h of operation, remaining constant after 24 h. In the absence of air injection in the stirred tank reactor, limited xylanase production was observed (final concentration 740 U l⁻¹). When the fermentation process was realized in the airlift bioreactor, xylanase production was higher than that observed in the stirred tank bioreactor, being 9,265 U l⁻¹ at 0.07 vvm (0.4 l min⁻¹) and 12,845 U l⁻¹ at 0.17 vvm (1 l min⁻¹) aeration rate.     

An airlift biofilm reactor for the biodegradation of phenol by Pseudomonas stutzeri OX1

Phenol bioconversion by Pseudomonas stutzeri OX1 using either free or immobilized cells was investigated with the aim of searching for optimal operating conditions of a continuous bioconversion process. The study was developed by analyzing: (a) free-cell growth and products of phenol bioconversion by batch cultures of P. stutzeri; (b) growth of P. stutzeri cells immobilized on carrier particles; (c) bioconversion of phenol-bearing liquid streams and the establishment and growth of an active bacterial biofilm during continuous operation of an internal-loop airlift bioreactor. We have confirmed that free Pseudomonas cultures are able to transform phenol through the classical meta pathway for the degradation of aromatic molecules. Data indicate that bacterial growth is substrate-inhibited, with a limiting phenol concentration of about 600 mg/L. Immobilization tests revealed that a stable bacterial biofilm can be formed on various types of solid carriers (silica sand, tuff, and activated carbon), but not on alumina. Entrapment in alginate beads also proved to be effective for P. stutzeri immobilization. Continuous bioconversion of phenol-bearing liquid streams was successfully obtained in a biofilm reactor operated in the internal-circulation airlift mode. Phenol conversion exceeded 95%. Biofilm formation and growth during continuous operation of the airlift bioreactor were quantitatively and qualitatively assessed.     

Immobilized growing cells of Gibberella fujikuroi P-3 for production of gibberellic acid and pigment in batch and semi-continuous cultures

Summary The performance of immobilized growing cells of Gibberella fujikuroi P-3 was affected by the immobilization agent used, nature and age of cells, mycelial cell density, size of beads and inclusion of linseed oil. The beads, prepared by using standardized procedures, could be used for 8 cycles without affecting productivity in semicontinuous culture. The rate of production of gibberellic acid was 0.58–0.66 mg/l/h. An inverted conical fluidized bioreactor, based on the design employed in continuous plant cell culture, was adopted. This bioreactor offers many advantages. The pigment produced by the fungus is not similar to bikaverin, norbikaverin and O-dimethylanhydrofusarubin, the known polyketides.     

Bioreactor application on adventitious root culture of <Emphasis Type="Italic">Astragalus membranaceus</Emphasis>

Astragalus membranaceus is one of the most widely used traditional medicinal herbs in China, but the time required to generate a useful product in the field production is long. The growth of adventitious root cultures was compared between cultures grown in solid, liquid, or a 5-L balloon-type bubble bioreactor. The maximum growth ratio (final dry weight/initial dry weight) was determined for adventitious roots grown in the bioreactor. Studies carried out to optimize biomass production of adventitious roots compared adventitious root growth from various inoculum root lengths, inoculum densities, and aeration volume in the bioreactors. The maximum growth ratio occurred in treatments with a 1.5-cm inoculum root length, with 30 g (fresh weight) of inoculum per bioreactor or with an aeration volume of 0.1 vvm (air volume/culture medium volume per min). The polysaccharide, saponin, and flavonoid content of roots from bioreactor-grown cultures were compared to roots from field-grown plants grown for 1 and 3 yr. Total polysaccharide content of adventitious roots in the bioreactor (30.0 mg g⁻¹ dry weight (DW)) was higher than the roots of 1-yr-old (13.8 mg g⁻¹ DW) and 3-yr-old (21.1 mg g⁻¹ DW) plants in the field. Total saponin (3.4 mg g⁻¹ DW) and flavonoid (6.4 mg g⁻¹ DW) contents were nearly identical to 3-yr-old roots and higher than that of 1-yr-old roots under field cultivation.     

Comparative profiles of α-amylase production in conventional tray reactor and GROWTEK bioreactor

GROWTEK bioreactor was used as modified solid-state fermentor to circumvent many of the problems associated with the conventional tray reactors for solid-state fermentation (SSF). Aspergillus oryzae IFO-30103 produced very high levels of α-amylase by modified solid-state fermentation (mSSF) compared to SSF carried out in enamel coated metallic trays utilizing wheat bran as substrate. High α-amylase yield of 15,833 U g⁻¹ dry solid in mSSF were obtained when the fungus were cultivated at an initial pH of 6.0 at 32°C for 54 h whereas α-amylase production in SSF reached its maxima (12,899 U g⁻¹ dry solid ) at 30°C after 66 h of incubation. With the supplementation of 1% NaNO₃, the maximum activity obtained was 19,665 U g⁻¹ dry solid (24% higher than control) in mSSF, whereas, in SSF maximum activity was 15,480 U g⁻¹ dry solid in presence of 0.1% Triton X-100 (20% higher than the control).     

产糖化酶黑曲霉固定化方法比较的研究

采用海藻酸钙凝胶电埋法、以沸石、多孔聚酯等材料为固定化载体的吸附法固定黑曲霉（Aspergillus niger AS3.4309)菌丝细胞,以游离菌丝体作为对照,进行发酵产糖化酶的比较,结果表明：以聚酯泡沫作为固定化载体吸附固定化菌丝细胞产糖化酶活力最高。在产糖化酶的发酵过程中,与游离菌丝体细胞相比,固定化黑曲霉持续产酶时间有一定程度的延长。     

Production of molecular hydrogen with immobilized cells ofRhodospirillum rubrum

Summary Cells ofRhodospirillum rubrum have been immobilized in various gels and tested for photobiological hydrogen production. Agar proved to be the best immobilizing agent with respect to production rates as well as stability. Agar immobilized cells were also superior compared to liquid suspension cultures. Growth conditions of the cells prior to immobilization, e.g. cell age, light intensity or nutrient composition, were of primary importance for the activity in the later immobilized state. A reactor with agar immobilized cells has been operated successfully over 3000 h with a loss of the activity of about 60%. Mean rates for hydrogen production for immobilized cells in this work during the first 60 to 70 hours after immobilization were in the range of 18 to 34 μl H₂ mg⁻¹ d.w. h⁻¹ and thus by a factor of up to 2 higher than liquid cultures under the same conditions. Maximal rates of hydrogen production (57 μl H₂ ml⁻¹ immobilized cell suspension) were reached in agar gel beads with cells immobilized after 70 h growth in liquid culture in the light and a cell density of 1.0 mg ml⁻¹, 70 h after immobilization.     

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.     

Efficient production of diltiazem chiral intermediate using immobilized lipase from <Emphasis Type="Italic">Serratia marcescens</Emphasis>

The lipase from Serratia marcescence ECU1010 (Sml) was capable of enantioselectively catalyzing the synthesis of many chiral drug precursors. This paper investigated the immobilization of Sml on appropriate supporting materials and its performance in bioreactor. Chitosan, Celite 545, and DEAE-cellulose were found to be the ideal supports among 8 carriers tested with respect to enzyme load and activity recovery of lipase. When Sml was immobilized, significant improvements of stability against pH, thermal, and operational deactivation were observed with all the 3 better supports, and the best stability was observed when the lipase was immobilized on glutaraldehyde activated chitosan. As for the effect of organic solvent in the biphasic reaction system, the hydrolytic activity of the immobilized lipase on trans-3-(4′-methoxyphenyl)glycidic acid methyl ester ((±)-MPGM) observed in isopropyl ether was 6 and 3 times higher than those in toluene and methyl tert-butyl ether. The lipasecatalyzed production of (−)-MPGM by enzymatic resolution of (±)-MPGM with chitosan-Sml in isopropyl etherwater biphasic system was carried out in a 2 L stirred-tank reactor. The batch operation was more efficient operation mode for the enantioselective hydrolysis of (±)-MPGM, affording enantiopure (−)-MPGM in 44.3% overall yield, in contrast to 29.3% in a continuous reactor.     

Dye decolorization by <Emphasis Type="Italic">Trametes hirsuta</Emphasis> immobilized into alginate beads

Summary The present paper studies the production of laccase by Trametes hirsuta immobilized into alginate beads in an airlift bioreactor. In order to enhance laccase production fresh ammonium chloride was added, which led to the production, of high laccase activities (around 1000 U l⁻¹). The bioreactor operated for 40 days without operational problems and the bioparticles maintained their shape throughout fermentation. Dye decolorization was performed at bioreactor scale operating in the batch mode. High decolorization percentages were obtained in a short time (96% for indigo carmine and 69% for phenol red in 24 h), indicating the suitability of this process for application to synthetic dye decolorization. On the other hand, in vitro decolorization of several industrial azo dyes by crude laccase produced in the above bioreactor was also performed. It was found that some of the dyes needed the addition of 1-hydroxybenzotriazole for their decolorization.