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Biochemical engineering of biocatalysts immobilized on cellulosic materials.

Complete design of the optimum immobilized biocatalyst seems to still be a matter of the future. To be successful, it would require numerical determination of all significant parameters at each enzyme engineering phase, that is at the design of the carriers, immobilized biocatalysts and immobilized reactors. Future research trends should follow this strategy. For processing, cellulosic materials have been considered carriers that fulfill requests to an example model: they represent a unique family of carriers that cover a broad variety of physical and chemical properties, immobilizing techniques, and immobilized reactors as well. The reason for writing this review article was to test the reliability of such a processing and subsequently, to confront theoretical considerations with practical applications of biocatalysts immobilized on cellulose materials.

Biotechnology↗

Steroid modifications with immobilized biocatalysts--use of immobilized enzyme-requiring cofactor regeneration and of immobilized mycelium.

Two biological approaches have been investigated for specific modifications of steroids. The first one uses the purified enzyme for the specific dehydrogenation of androsterone to androstanedione. The enzyme used is 3 alpha-hydroxysteroid dehydrogenase which requires a cofactor (NAD). A cofactor regeneration is needed so that the process could work continuously. The conjugation of two points (immobilization of the enzyme and optimization of the ratio methanol-water) allows a continuous work of the enzyme during 25 days. Moreover, we propose a chemical regeneration of the cofactor using methoxy derivative of phenazine methosulphate. Right now it is the limiting step of the process. The second approach of steroid modification uses a whole mycelium of Aspergillus phoenicis for the specific hydroxylation of progesterone to 11 alpha-hydroxy progesterone. The transformation of 90% of the progesterone is obtained with calcium alginate immobilization and the lowest number of products is obtained at pH lower than 2.5 with carrageenan and polyurethane immobilization. It seems promising to apply immobilized biocatalysts to the bioconversion of hydrophobic compounds in organic solvents system.

3-Hydroxysteroid Dehydrogenases↗

Characterization of an industrial biocatalyst: immobilized glutaryl-7-ACA acylase.

A batch of the immobilized industrial biocatalyst glutaryl-7-ACA acylase (GA), one of the two enzymes involved in the biotransformation of cephalosporin C (CefC) into 7-aminocephalosporanic acid (7-ACA), was characterized. K(m) value for glutaryl-7-ACA was 5 mM. Enzyme activity was found to be optimal at pH between 7 and 9.5 and to increase with temperature and in buffered solutions. To avoid product degradation, optimal reaction conditions were obtained working at 25 degrees C using a 50-mM phosphate buffer, pH 8.0. Immobilized GA showed good stability at pH value below 9 and at temperature up to 30 degrees C. The inactivation of immobilized GA in the presence of different amounts of H(2)O(2), a side product that might be present in the plant-scale industrial solutions of glutaryl-7-ACA, was also investigated, but the deactivation rates were negligible at H(2)O(2) concentration that might be reached under operative conditions. Finally, biocatalyst performance in the complete two-step enzymatic conversion process from CefC to 7-ACA was determined on a laboratory scale. Following the complete conversion of a 75 mM solution of CefC into glutaryl-7-ACA catalyzed by an immobilized D-amino acid oxidase (DAAO), immobilized GA was used for the transformation of this intermediate into the final product 7-ACA. This reaction was repeated for 42 cycles. An estimation of the residual activity of the biocatalyst showed that 50% inactivation of immobilized GA was reached after approximately 300 cycles, corresponding to an enzyme consumption of 0.4 kU per kg of isolated 7-ACA.

Amidohydrolases↗

Mechanical stability of immobilized biocatalysts (CLECs) in dilute agitated suspensions.

Cross-linked enzyme crystals (CLECs) are a novel form of immobilized biocatalyst designed for application in industrial biotransformation processes. In this work we have investigated the mechanical stability of agitated CLEC suspensions in relation to the design and scale-up of bioconversions carried out in stirred-tank reactors. By careful control of the crystallization conditions yeast alcohol dehydrogenase I (YADHI) microcrystals of different size were first prepared having either an hexagonal (approximately 12 microm) or rod-shaped (approximately 4.6 microm) morphology. These were then cross-linked with glutaraldehyde to form CLECs. The rate of breakage of the CLEC suspensions was subsequently measured in a rotating disk shear device (total volume, 11 mL) by monitoring the change in crystal size distribution with time. This device is designed to mimic the shear and energy dissipation rates found in a range of process scale equipment and may be used to study the mechanical stability of any immobilized biocatalyst preparation. Experiments were performed as a function of the speed and duration of disk rotation, CLEC concentration (0.26-2.5 mg.mL(-1)) and energy dissipation rate (2.2 x 10(3) to 6.8 x 10(5) W.kg(-1)). No breakage of the rod-shaped CLECs was observed over the entire range of experimental conditions investigated. Breakage of the larger hexagonal-shaped CLECs did occur, however, at energy dissipation rates, epsilon(max), above 1.0 x 10(5) W.kg(-1), where the calculated length scale of turbulence was around 2.0 microm. Based on visual observation of the sheared CLEC suspensions and models of crystal breakage, it was concluded that breakage of the hexagonal-shaped CLECs occurred due to shear induced attrition. Measurement of the catalytic activity of both the hexagonal and rod-shaped CLECs showed no significant change in activity before and after shearing.

Alcohol Dehydrogenase↗

[Immobilized biocatalysts in biotechnological processes].

In recent years, biotechnology has been stuck with the problem of choosing the most technologically convenient way of utilization of biocatalysts using bacterial cells or structural formations. Immobilization of bio-objects on solid carriers uses the advantages of heterogenic catalysis over homogenous like simple separation of byocatalyst from end product on completion of biotechnological process, and highly effective transformation or synthesis of organic compounds through biomass concentration in fermenter. In addition, immobilized biocatalysts exhibit better stability in case of exposure to aggressive temperatures, active environmental reactions, and "attack" of foreign microflora. Immobilized biocatalyzers can operate repeatedly and owing to the unique specificity show promise for wide application in aerospace and environmental medicine.

Biotechnology↗

Proteomic methods applied to the analysis of immobilized biocatalysts.

Methods adapted from proteomics can directly characterize proteins present in immobilized biocatalysts. Complete hydrolysis followed by HPLC analysis of Tyr and Phe estimates total protein bound, and is preferable to conventional difference methods, as tested with subtilisin Carlsberg on silica. This new method shows that various treatments give quantitative desorption of proteins immobilized by adsorption. Intact desorbed proteins may be analyzed by electrospray mass spectrometry. The Candida antarctica lipase B from Novozyme 435 was shown to be heavily glycosylated, while the lipase from Lipozyme RM IM was a mixture of four N-terminally truncated forms. Peptides from selective cleavage were analyzed by tandem mass spectrometry, leading to automatic identification of proteins present. A second major protein present in Lipozyme RM IM was thus found to be alpha-amylase from Aspergillus oryzae. These methods should be valuable complements to activity measurements in understanding immobilized enzyme activity and stability.

Adsorption↗

Continuous fabrication of biocatalyst immobilized microparticles using photopolymerization and immiscible liquids in microfluidic systems.

We report a novel technique for manufacturing polymeric microparticles containing biocatalysts by the behavior of immiscible liquids in microfluidic systems and in situ photopolymerization. The approach utilizes a UV-polymerizable hydrogel/enzyme solution and an immiscible oil solution. The oil and hydrogel solutions form emulsions in pressure-driven flow in microchannels at high values of the dimensionless capillary number (Ca). The resultant hydrogel droplets are then polymerized in situ via exposure to 365 nm UV light. This technique allows for the generation of monodisperse particles whose size can be controlled by the regulation of flow rates. In addition, both manufacturing microparticles and immobilizing biocatalysts can be performed simultaneously and continuously.

Biosensing Techniques↗

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.

Alcohol Dehydrogenase↗

Preparation of a very stable immobilized biocatalyst of glucose oxidase from Aspergillus niger.

Glucose oxidase (GOX) has been immobilized on different activated supports, including glyoxyl agarose, epoxy sepabeads and glutaraldehyde-activated supports. Immobilization onto supports pre-activated with glutaraldehyde rendered the most thermo-stable preparation of GOX. Therefore, as the glutaraldehyde chemistry gave a high stabilization of the enzyme, we proposed another technique for improving the multipoint attachment through glutaraldehyde: the enzyme was ionically adsorbed on cationic supports with primary amino groups and then the immobilized preparation was treated with a glutaraldehyde solution. The decrease on enzyme activity was <20%. Following this methodology, we achieved the highest stability of all the immobilization systems analyzed, showing a half-life 100 times higher than the soluble enzyme. Moreover, this derivative showed a higher stability in the presence of organic solvents (for instance methanol) or hydrogen epoxide than the ionically adsorbed enzyme or the soluble one. Therefore, the adsorption of GOX on aminated cationic support and subsequent treatment with glutaraldehyde was presented as a very successful methodology for achieving a very stable biocatalyst.

Aspergillus niger↗

Continuous itaconic acid production by immobilized biocatalysts.

The continuous itaconic acid production from sucrose with Aspergillus terreus TKK 200-5-3 mycelium immobilized on polyurethane foam cubes was optimized in column bioreactors using statistical experimental design and empirical modelling. The highest itaconic acid product concentration calculated on the basis of the obtained model was 15.8 g l-1 in the investigated experimental area, when sucrose concentration was 13.5%, aeration rate 150 ml min-1 and residence time 178 h. From sucrose with immobilized A. terreus TKK 200-5-3 mycelium itaconic acid production was stable for at least 4.5 months in continuous column bioreactors. In comparison, using glucose as substrate and immobilized A. terreus TKK 200-5-1 mycelium as biocatalyst similar stability was obtained with higher product concentration. The omission of copper sulphate from the production medium gave the highest itaconic acid product concentration (26 g l-1) from 9% glucose with 0.25% ammonium nitrate and 0.095% magnesium sulphate.

Aspergillus↗

Mechanical stability and diffusional resistance of a polymeric gel used for biocatalyst immobilization.

The mechanical strength of gelatin gels insolubilized by crosslinking with formaldehyde was measured at various gelatin percentages and formaldehyde-to-gelatin ratios. This property was shown to be related to the characteristic sponge-like structure of the insolubilized gelatin gel, a structure that unexpectedly is also responsible for the resistance to substrate and product diffusion. A comparison between immobilizates of invertase and invertase-active yeast cells prepared with different gelatin concentrations showed that the enzyme, in contrast to cells, is deeply involved in the gel insolubilization process. The catalytic behavior of agar, kappa-carrageenan, alginate, and gelatin immobilizates was compared under the same conditions of cell loading.

Catalysis↗

Ionic liquid-reconstituted cellulose composites as solid support matrices for biocatalyst immobilization.

Preparation of cellulose-polyamine composite films and beads, which provide high loading of primary amines on the surface allowing direct one-step bioconjugation of active species, is reported using an ionic liquid (IL) dissolution and regeneration process. Films and bead architectures were prepared and used as immobilization supports for laccase as a model system demonstrating the applicability of this approach. Performance of these materials, compared to commercially available products, has been assessed using millimeter-sized beads of the composites and the lipase-catalyzed transesterification of ethyl butyrate.

Biocompatible Materials↗

Detoxification of organophosphate nerve agents by immobilized dual functional biocatalysts in a cellulose hollow fiber bioreactor.

A whole-cell technology for detoxification of organophosphates based on genetically engineered Escherichia coli cell expressing both cellulose-binding domain (CBD) and organophosphorus hydrolase (OPH) onto cell surface was reported recently (Wang et al., 2002). This study reports the application of these biocatalysts when immobilized in a cellulose hollow fiber bioreactor (HFB) for the biodetoxification of a model organophosphate, paraoxon, in a continuous flow mode. In 24 h, 0.79 mg wet cell/cm2 fiber surface were immobilized onto cellulose fibers specifically and strongly through the cellulose binding domain, forming a monolayer demonstrated by Scanning Electronic Micrograph, and essentially no cell was washed away by washing buffer. The immobilized biocatalyst had a high performance of detoxifying paraoxon solution of 5,220 mumol/h x L reactor or 990 mumol/h x m2 reactor. The immobilized biocatalysts maintained a stable degradation capacity for 15 uses over a period of 48 days with only 10% decline in degradation efficiency under operating and storage conditions. In addition, the bioreactor was easily regenerated by washing with 1% sodium dodecyl sulfate (SDS), with 86.7% immobilization capacity and 93.9% degradation efficiency recovery. This is the first report using the HFB in a non-traditional way, immobilizing whole-cell biocatalysts by specific adhesion thus rendering the catalysis operation the advantages of low pressure drop, low shear force, and low energy requirement. The successful application of this genetically engineered dual functional E. coli strain in a model bioreactor shows its promise in large-scale detoxification of organophosphate nerve agents in bulk liquid phase.

Aryldialkylphosphatase↗