Characterization of <Emphasis Type="Italic">Mucor miehei</Emphasis> lipase immobilized on polysiloxane-polyvinyl alcohol magnetic particles

Mucor miehei lipase was immobilized on magnetic polysiloxane-polyvinyl alcohol particles by covalent binding. The resulting immobilized biocatalyst was recycled by seven assays, with a retained activity around 10% of its initial activity. K_m and V_max were respectively 228.3 M and 36.1 U mg of protein^–1 for immobilized enzyme. Whereas the optimum temperature remained the same for both soluble and immobilized lipase (45 °C), there was a shift in pH profiles after immobilization. Optimum pH for the immobilized lipase was 8.0. Immobilized enzyme showed to be more resistant than soluble lipase when assays were performed out of the optimum temperature or pH.     

A new method to determine the aw range in which immobilized lipases display optimum activity in organic media

Summary We describe a qualitative method to predict the pre-equilibration a_w, system value in which, covalent immobilized lipase B from Candida antarctica to sepharose and silica, displayed best synthetic activity. The methodology is based in the analysis of the water adsorption isotherms of the biocatalyst in air and in the organic solvent. The biocatalyst is active at pre-equilibration a_w values higher than the divergence point between both isotherms. In addition, native and immobilized lipase display highest activity if the biocatalyst is pre-equilibrated at a_w=P point. For preparative purposes, the validity of the method was proved in the esterification of racemic 2-(4-isobutyl phenyl) propionic acid with 1-propanol in isooctane at long reaction time.     

Integrated immobilized cell reactor-adsorption system for β-cyclodextrin production: a model study using PVA-cryogel entrapped Bacillus agaradhaerens cells

Production of cyclodextrins (CDs) by immobilized cells of the alkaliphilic Bacillus agaradhaerens LS-3C with integrated product recovery was studied. The microorganism was entrapped in polyvinyl alcohol-cryogel beads and used as a convenient source of immobilized cyclodextrin glycosyltransferase (CGTase). On activation by incubation in the cultivation medium containing 1% (w/v) starch, the entrapped cells multiplied and secreted CGTase with an activity of 2–3 mg -cyclodextrin h^–1 g^–1 beads. The immobilized biocatalyst exhibited maximum activity at pH 9 and 50 °C, and formed cyclodextrins comprising 92–94% -CD and remaining -CD. The cyclodextrin product from the immobilized cell bioreactor was continuously recovered by adsorption to Amberlite XAD-4 in a recycle batch mode. The product adsorption was facilitated at low temperature while hot water was used for elution.     

Microsomal Transformation of Organophosphorus Pesticides by White Rot Fungi

The enzymatic mechanism for the transformationof organophosphorus pesticides (OPPs) by differentwhite-rot fungi strains was studied. With theexception of Ganoderma applanatum 8168,all strains from a collection of 17 different fungicultures were able to deplete parathion. Threestrains showing the highest activities were selectedfor further studies: Bjerkandera adusta 8258,Pleurotus ostreatus 7989 and Phanerochaetechrysosporium 3641. These strains depleted 50 to96% of terbufos, azinphos-methyl, phosmet andtribufos after four-days exposure to the pesticides.In order to identify the cellular localization of thetransformation activity, the extracellular andmicrosomal fractions of Pleurotus ostreatus7989 were evaluated in vitro. While the activitiesof ligninolytic enzymes (lignin peroxidase,manganese peroxidase and laccase) weredetected in the extracellular fraction, noenzymatic modification of any of the fivepesticides tested could be found, suggestingthe intracellular origin of the transformationactivity. In accordance with this observation themicrosomal fraction was found able to transformthree OPPs with the following rates:10 mol mg prot^-1 h^-1 forphosmet, 5.7 mol mg prot^-1 h^-1 forterbufos, and 2.2 mol mg prot^-1 h^-1 forazinphos-methyl. The products from these reactions andfrom the transformation of trichlorfon and malathion,were identified by mass-spectrometry. These results,supported by specific inhibition experiments and thestringent requirement for NADPH during the in vitroassays suggest the involvement of a cytochrome P450.     

Improved conditions for protoplast formation and transformation of Pleurotus ostreatus

Conditions suitable for the production and regeneration of Pleurotus ostreatus protoplasts from dikaryotic mycelia were examined. Three commercially available muralytic enzymes, including Sigma lysing enzyme, Novozym 234 and Novozym 234 LP, were used for production of protoplasts. Over 2 × 10⁷ protoplasts per gram fresh weight mycelia were obtained within 1.5 h by using each of these three enzymes. The colony regeneration rate was up to 13% on potato-dextrose-agar medium containing 0.8 m mannitol. Genetic transformation was based on positive selection for resistance to hygromycin B (HmB) using the plasmid vector pAN7-1 and accomplished by either electroporation or a polyethylene glycol (PEG)-divalent cation method. P. ostreatus strains used in this study have innate sensitivity to HmB at a critical inhibitory concentration of between 40–50 g/ml. Selection for HmB resistance of this fungus, indicative of transformation, resulted in 3–48 HmB-resistant colonies per microgram of pAN7-1 per 10⁷ viable protoplasts. No significant differences were apparent when either transformation protocol or either P. ostreatus strain was used. The best electrical condition found for the electrotransformation of P. ostreatus is at a field strength of 2.6–2.8 kV/cm with a capacitance of 25F and a parallel resistance of 800 ohms, corresponding to a time constant range of 10–14 ms. Correspondence to: P. A. Lemke     

Sequential conversion of cortexolone to prednisolone by immobilized mycelia of Curvularia lunata and immobilized cells of Arthrobacter simplex

Summary Two-step bioconversion of cortexolone (Reichstein's Compound S) to its ¹-dehaydro-11-hydroxy derivative, prednisolone, was successfully performed by the combined use of immobilized Curvularia lunata mycelia and immobilized Arthrobacter simplex cells. Immobilized living mycelia of C. lunata having a high 11-hydroxylation activity were prepared by in situ germination of spores entrapped in photo-crosslinked resin gels of a suitable net-work structure. Acetone-dried cells of A. simplex having an induced steroid ¹-dehydrogenase activity were also entrapped with photo-crosslinkable resin prepolymers and used for - dehydrogenation of hydrocortisone to prednisolone. For the production of prednisolone from cortexolone, the combination of sequential steps, 11-hydroxylation and subsequent ¹-dehydrogenation, was found to be suitable. Each immobilized microbial cell system was stable and could be used for the sequential reactions repeatedly (operational period, 25 days).     

Bioconversion of apple pomace into a nutritionally enriched substrate by Candida utilis and Pleurotus ostreatus

Apple production in the world has increased significantly over the last 10 years. A considerable fraction of these fruits, mainly those not approved for fresh consumption, is industrially processed to produce juices, flavours and concentrates. During this processing, a large amount of solid residues is produced, comprised mainly of peels, seeds, and pulp, which are collectively known as apple pomace. This work aims to select biological treatments and conditions for the bioconversion of apple pomace by Candida utilis and Pleurotus ostreatus, either individually or sequentially, into an enriched substrate with increased digestibility for use as ruminant feed. After C. utilis fermentation, the protein level increased 100% and the mineral content 60%, accompanied by 8.2% of increase in the digestibility. The level of free sugars decreased 97% after substrate supplementation with ammonium sulphate (10 g l^–1). After optimization, sequential fermentation with C. utilis and P. ostreatus achieved a high protein level with 500% of crude protein enrichment after 60 days of fermentation as well as a considerable increase in the mineral level. The level of free sugars increased after the fermentation with P. ostreatus alone due to pectin and hemicellulose degradation. Considering the time required for fermentation, the C. utilis treatment was the most efficient treatment to convert apple pomace into a more nutritive substrate for ruminant feed.     

Production of high fructose syrup from <Emphasis Type="Italic">Asparagus</Emphasis> inulin using immobilized exoinulinase from <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> YS-1

Extracellular exoinulinase from Kluyveromyces marxianus YS-1, which hydrolyzes inulin into fructose, was immobilized on Duolite A568 after partial purification by ethanol precipitation and gel exclusion chromatography on Sephadex G-100. Optimum temperature of immobilized enzyme was 55 °C, which was 5 °C higher than the free enzyme and optimal pH was 5.5. Immobilized biocatalyst retained more than 90% of its original activity after incubation at 60 °C for 3 h, whereas in free form its activity was reduced to 10% under same conditions, showing a significant improvement in the thermal stability of the biocatalyst after immobilization. Apparent K _m values for inulin, raffinose and sucrose were found to be 3.75, 28.5 and 30.7 mM, respectively. Activation energy (E _a) of the immobilized biocatalyst was found to be 46.8 kJ/mol. Metal ions like Co²⁺ and Mn²⁺ enhanced the activity, whereas Hg²⁺ and Ag²⁺ were found to be potent inhibitors even at lower concentrations of 1 mM. Immobilized biocatalyst was effectively used in batch preparation of high fructose syrup from Asparagus racemosus raw inulin and pure inulin, which yielded 39.2 and 40.2 g/L of fructose in 4 h; it was 85.5 and 92.6% of total reducing sugars produced, respectively.     

Selection of a support for immobilization of a microbial lipase for the hydrolysis of triglycerides

Baterial lipase from Staphylococcus carnosus (pLipMut2) has been immobilized on various supports in order to determine a suitable immobilization technique in terms of activity and stability, when utilized for the hydrolysis of tributyrin. The hydrophobic materials PBA Eupergit and PBA Eupergit 250L prooved to be appropriate supports, when the enzyme was crosslinked with glutaraldehyde after adsorption. No desorption of the immobilized enzyme occured during operation. The pore size of the support has a strong effect on the activity but does not influence stability.The initial activity for immobilized and soluble lipase is found to follow the Arrhenius equation at low temperature, where mass transfer does not affect reaction kinetics. Activation energies for soluble and immobilized lipase were evaluated to be 21.7 kJ mol^–1 and 60.8 kJ mol^–1, respectively.Operational stability was studied in a packed bed recirculation reactor. Thermal desactivation followed first order kinetics with a half-life of 1340 h at 10°C. Model calculations for productivity showed, that optimal temperatures for high productivity are well below the temperature of maximal activity.List of Symbols E _a [kJ mol^–1] activation energy - E _d [kJ mol^–1] activation energy of desactivation - H [–] half-number - k _d [h^–1] desactivation constant - k _d, [h^–1] constant - k _N [–] desactivation constant (number) - N [–] number of runs - p [mol dm^–3] productivity - t [h] time - t _0.5 [h] half-life - T [K] absolute temperature - V [U ml^–1] activity - V(N) [Uml^–1] activity exhibited in the n-th run - V _s,O [U ml^–1] initial activity of supernatant - V _s, [U ml^–1] activity of supernatant after immobilization - V _O [U ml^–1] initial activity - V [U ml^–1] constant - _imm [–] activity yield - [ml ml^–1] ratio of volume of support to volume of supernatant Financial support of this work by the Deutsche Forschungsgemeinschaft (SFB 145, A15) is gratefully acknowledged.     

n-carbamoyl-d-p-hydroxyphenylglycine production using immobilized d-hydantoinase from recombinant E. coli

An immobilized d-hydantoinase was characterized and employed to produce n-carbamoyl-d-p-hydroxyphenylglycine (CpHPG) in a repeated batch process. The V_max and K_m of the immobilized d-hydantoinase at 50°C were 6.28 mm min⁻¹ g⁻¹ biocatalyst and 71.6 mm, respectively. The product CpHPG did not inhibit the activity of d-hydantoinase. Optimal reaction temperature was 60°C. A decrease in activity of immobilized d-hydantoinase due to thermal inactivation could be described as first-order decay; the deactivation energy was 23.97Kcal mol⁻¹. Under process conditions (50°C, 10% w/v substrate, and pH 8.5), the half-life of the immobilized d-hydantoinase was eight batches. The attrition of immobilized d-hydantoinase particles with a large amount of insoluble substrate particles during stirring resulted in fine biocatalyst particles. In addition to the thermal inactivation, the loss of fine biocatalyst particles during the recovery step contributed to the low operational stability.     

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     

Use of porous glass fiber as a support for biocatalyst immobilization

Summary Porous glass fiber has a very high surface area and good mechanical properties that make it an excellent support for biocatalyst immobilization. By packing aligned glass fibers in a tubular reactor such that the fibers are all parallel to the axis of the tube, the resulting pressure drop is considerably smaller than for a similar bed of packed beads. The utility of this support was demonstrated by immobilizing -glucoamylase by silane-glutaraldehyde coupling, and measuring its activity toward converting maltose to glucose. Using optimized immobilization conditions, an enzyme loading of 1.5 mg protein perm ² surface area was obtained, with an activity of 370 units/g glass at 50°C. The half-life of the immobilized glucoamylase was more than twice as long as that of the free enzyme.     

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.     

Continuous production of gibberellic acid in a fixed-bed reactor by immobilized mycelia of Gibberella fujikuroi in calcium alginate beads

Summary The continuous production of gibberellic acid with immobilized mycelia of Gibberella fujikuroi was maintained over a hundred days in a tubular fixed-bed reactor. Free mycelium at the beginning of the storage phase was harvested from G. fujikuroi shake-flask culture and was immobilized by ionotropic gelation in calcium alginate beads.The continuous recycle production system consisted of a fixed-bed reactor, a container in which the culture medium was heated, stirred and aerated, and valves for sample withdrawal or reactant addition during the first 1320 h (55 days). A two-phase continuous extractor was then added for the last 960 hours (40 days). Free and immobilized mycelium shake-flask cultures with the same strain used in the continuous culture system were also realized to compare growth, maintenance and production parameters. The results show about the same gibberellic acid productivity in both free and immobilized mycelium shakeflask cultures: 0.384 and 0.408 mgGA₃·gBiomass^-1 ·day^-1, respectively, whereas in the continuous system the gibberellic acid production is about twice as large for a similar biomass: 0.768 mgGA₃·gBiomass^-1·day^-1. Several factors affecting the overall productivity of the immobilized systems were found to be: the quality and the quantity of mycelia in the biocatalyst beads and the immobilization conditions.     

Production of l-glutamate by immobilized protoplasts

Summary Protoplasts of Brevibacterium flavum cultured in a medium containing 50 g·l^-1 of biotin were prepared with lysozyme and immobilized in matrices of agar-acetylcellulose filters. The immobilized protoplasts were applied to l-glutamate production from glucose and urea in a batch system. The productivity of l-glutamate by the immobilized protoplasts was 2.5 times higher than that by immobilized whole cells under optimal conditions. Maximal productivity initially reached 1.5 mg·ml^-1. The immobilized protoplasts of B. flavum could be used six times for l-glutamate production with retention of about 70% of the initial productivity.     

Transformation of microcrystalline hydrocortisone by free and immobilized cells of Arthrobacter simplex

Summary The transformation of microcrystalline hydrocortisone by free and immobilized cells of Arthrobacter simplex resulted in formation of prednisolone. The effect of medium composition, non-ionogenic surfactants and exogeneous electron acceptors on the ¹-dexydrogenase activity of free and immobilized cells is described. Offprint requests to: R. Vlahov     

Continuous sucrose hydrolysis by yeast cells immobilized to wool

A novel immobilized biocatalyst with invertase activity was prepared by adhesion of yeast cells to wool using glutaraldehyde. Yeast cells could be immobilized onto wool by treating either the yeast cells or wool or both with glutaraldehyde. Immobilized cells were not desorbed by washing with 1 M KCl or 0.1 M buffers, pH 3.5–7.5. The biocatalyst shows a maximum enzyme activity when immobilized at pH 4.2–4.6 and 7.5–8.0. The immobilized biocatalyst was tested in a tubular fixed-bed reactor to investigate its possible application for continuous full-scale sucrose hydrolysis. The influence of temperature, sugar concentration and flow rate on the productivity of the reactor and on the specific productivity of the biocatalyst was studied. The system demonstrates a very good productivity at a temperature of 70 °C and a sugar concentration of 2.0 M. The increase of the volume of the biocatalyst layer exponentially increases the productivity. The productivity of the immobilized biocatalyst decreases no more than 50% during 60 days of continuous work at 70 °C and 2.0 M sucrose, but during the first 30 days it remains constant. The cumulative biocatalyst productivity for 60 days was 4.8 × 10³kg inverted sucrose/kg biocatalyst. The biocatalyst was proved to be fully capable of continuous sucrose hydrolysis in fixed-bed reactors. Received: 8 November 1996 / Received revision: 31 January 1997 / Accepted: 31 January 1997     

Stability characterization and comparison of two fluidized-bed bioreactors

Fluidized-bed bioreactors (FBRs) with immobilized cells have been used successfully at Oak Ridge National Laboratory and at the Autonomous University of Barcelona for several applications, including high-productivity yields of ethanol. During the development of these processes, experimental results have revealed differences between three-phase fluidized biocatalyst systems and those systems typically used for hydrodynamic studies. These differences appear to be related to the physical properties (density, viscosity, surface tension) of the phases and, in particular, the low density of the solid particles. Parameters were calculated from these physical properties following the approach of Baker for two-phase flow. A map of these parameters was proposed previously and separated regions of satisfactory and unsatisfactory fluidization of a three-phase immobilized-yeast FBR fluidized with air. This same map was used for an FBR with immobilized Zymomonas mobilis that was liquid fluidized. The stability regions on the map corresponded to the two different experimental operating systems. This indicates the possible general applicability of this approach to biological FBRs.List of Symbols _L kg/s² liquid surface tension - _L kg/(ms) liquid viscosity - _L kg/m³ liquid density - _s kg/mm³ solid density - m_L kg/s mass liquid flow rate - _L kg/s mass flow rate of CO₂ generated by fermentation     

Production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans containing aminotransferase activity

Summary To establish an efficient production method for l-phenylalanine, the production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans pFPr-1 containing aminotransferase activity was investigated. By using intact cells, 0.74M l-phenylalanine was produced from 0.8M phenylpyruvate (conversion yield, 92.5%). Moreover, by using immobilized cells with -carrageenan, when the space velocity was 0.1 h^-1 at 30°C, 0.135 M l-phenylalanine was produced from 0.15 M phenylpyruvate (conversion yield, 90%). The half-life of the l-phenylalanine-forming activity of the column was estimated to be about 30 days at 30°C.     

Accumulation of cadmium by immobilizedZoogloea ramigera 115

Summary Zoogloea ramigera 115 was immobilized into beads of calcium-alginate and placed into batch air-bubbled column reactors. In the absence of any added nutrients the immobilized bacterium adsorbed Cd from solutions containing levels of 2 and 20 g ml^–1 per day, over a period of 21 and 20 days, respectively. Adsorption of Cd from solutions containing 20 g ml^–1 Cd was better than 90% for 16 days. Beads treated with Cd at 2 g ml^–1 never adsorbed less than 95% of the metal. Alginate adsorbed Cd as well, but inclusion of cells changed the effectiveness of adsorption. Of a 250 g ml^–1 Cd solution, alginate adsorbed 70.4% Cd in 60 min whereas alginate plus cells adsorbed 90.5% in the same time span. Temperature had no effect on adsorption by immobilized cells at levels of 2 and 10 g ml^–1 Cd. However at higher concentrations, binding was enhanced as temperature increased.Z. ramigera beads were stable during all treatments and for prolonged periods of time (21 days).