Response surface optimization for the continuous glucose isomerization process

Production of fructose via a continuous glucose isomerization process was optimized using response surface methodology. Glucose isomerization was performed using immobilized glucose isomerase in a flow-through tubular reactor. Process factors eg pH (7.0–7.8), temperature (50–60°C), flow rate (5–17 ml min^–1) and glucose content (30–50% w/w) of the feedstock solution were simultaneously tested according to a central composite experimental design. Measured responses such as % isomerization, and fructose yield (gh^–1) has an excellent correlation with tested factors. The highest desirability,D, (geometric mean of % isomerization and fructose yield) was obtained when the feedstock (56–60°C) had 34–36% glucose, a pH of 7.4–7.8 and was pumped at 15 ml min^–1.     

Improvement of oxidoreductase stability of cethyltrimethylammoniumbromide permeabilized cells ofZymomonas mobilis through glutaraldehyde crosslinking

Summary Permeabilization ofZymomonas mobilis with CTAB(Cetyltrimethylammoniumbromide) was investigated in order to obtain a stable process for sorbitol production in the immobilized system. The optimum conditions for sorbitol formation were treating cells with 0.2% CTAB at 4°C for 10 min. For the immobilized system permeabilized cells were treated with glutaraldehyde to improve the system with cross-linking of enzymes. In this way, no significant loss of enzyme activity was apparent during 30 day operation in a continuous process. The productivity of the continuous process at a dilution rate 0.2 h^–1 was 6.51g/L-h for sorbitol. The CTAB-permeabilized cells could be used to produce sorbitol and gluconic acid simultaneously in the long term continuous process.     

Production of l-lactic acid with immobilized Lactobacillus delbrueckii

Summary Living Lactobacillus delbrueckii cells were entrapped in calcium alginate gel beads and employed both in recycle batch and continuous column reactors to produce l-lactic acid from glucose. The substrate contained l% (w/v) yeast extract as nutrient and 4.8% (w/v) solid calcium carbonate as buffer. The maxiumum lactic acid yield obtained was 97%, of which more than 90% was l-lactic acid. The biocatalyst activity half-life in continuous operation was about 100 d, and only about 10% of the activity was lost during intermittent storage of the bioreactor at +7°C for about 5 months.     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

Investigation on macrokinetics of heterogeneous process of monosaccharide isomerization using non-growing cells of a glucoisomerase producer <Emphasis Type="Italic">Arthrobacter nicotianae</Emphasis> immobilized inside SiO<Subscript>2</Subscript>-xerogel

Macrokinetic peculiarites of heterogeneous process of monosaccharide (glucose/fructose) isomerization using biocatalysts prepared by incorporation of non-growing cells of a glucose isomerase-producing strain Arthobacter nicotianae inside SiO₂-xerogel have been investigated. It was shown that the process proceeds in kinetic regime without diffusion limitation and biocatalyst activities at 60 and 75°C were 19 and 32 U/g, respectively. Time of equilibrium in the reaction of monosaccharide isomerization was a function of starting (“triggering”) glucose isomerase activity in a unit of reaction volume. When the activity exceeds 10 U/ml, equilibrium equimolar mixture of glucose and fructose was produced within a few hours. It was established that a continuous process carried out in a plug-flow packed-bed reactor is more efficient than a batch process accompanied with recycling, first of all, to significant improvement of operation stability of the designed biocatalysts. Under model conditions of industrial heterogeneous process of producing glucose-fructose syrups, the half-life time of inactivation of the biocatalysts was more than 500 h at (65 ± 5)°C.     

The addition of Co2+ enhances the catalytic efficiency and thermostability of recombinant glucose isomerase from Thermobifida fusca

Glucose isomerase is an important industrial enzyme that catalyzes the reversible isomerization of glucose to fructose. In this study, the effect of cobalt ions (Co²⁺) on the catalytic efficiency and thermostability of recombinant glucose isomerase from Thermobifida fusca was analyzed. The activity of glucose isomerase from engineered Escherichia coli supplemented with 1 mM Co²⁺ (C-GI) reached 41 U/ml, 2.1-fold higher than enzyme prepared from E. coli without additive (GI). The purified C-GI also exhibited an increased specific activity (23.8 U/mg compared to 12.1 U/mg for GI) and a greater thermostability (half-life of 17 h at 75 °C, 11.3-fold higher than GI (1.5 h)). The optimal temperature for C-GI shifted from 80 °C to 85 °C and demonstrated higher activity over pH 7.0–9.0. The k_cat/K_m value of C-GI (89.3 M^?1 s^?1) for the isomerization of glucose to fructose was nearly 1.75-fold higher than that of GI. In addition, the engineered cells were immobilized with the method of flocculation-cross linking. The immobilized cells supplemented with 1 mM Co²⁺ (C-IGI) had a better operational performance than cells without additives (IGI); at the end of 6 cycles, the conversion rate of C-IGI was still 43.1%, meeting the conversion rate requirement.     

Optimization of biobleaching of paper pulp in an expanded bed bioreactor with immobilized alkali stable xylanase by using response surface methodology

Purified alkali stable xylanase from Aspergillus fischeri was immobilized on polystyrene beads using diazotization method. An expanded bed bioreactor was developed with these immobilized beads to biobleach the paper pulp in continuous mode. Response surface methodology was applied to optimize the biobleaching conditions. Temperature (degrees C), flow rate of pulp (ml/min) and concentration of the pulp (%) were selected as variables in this study. Optimal conditions for biobleaching process were reaction temperature 60 degrees C, flow rate of 2 ml/min and 5% (w/v) of pulp. The kappa number reduced from 66 in the unbleached pulp to 20 (reduction of 87%). This system proves to be a better option for the conventional chlorine based pulp bleaching.     

Co-immobilization of cellulase and glucose isomerase by molecular deposition technique

Cellulase was immobilized and co-immobilized with glucose isomerase within p-trimethylamine polystyrene beads using a molecular deposition technique. The co-immobilized enzyme system directly converted insoluble cellulose to glucose and fructose in 60:40 molar ratio. The co-immobilized enzyme still retained 50% of its initial activity at 50°C after 4 recycles of 5 hours for each time.     

Kinetics of invertase immobilised on poly(phe-lys) coated polystyrene beads

Summary Surface of polystyrene beads was modified by poly(phe-lys) for invertase immobilisation. The optimum immobilisation conditions of invertase were; 0.01% (w/v) poly(phe-lys), 2% (v/v) glutaraldehyde at 25 °C and pH 4.5. The kinetics of sucrose hydrolysis by free and immobilised invertase in a batch reactor at pH 4.5 and 55 °C gave K_m and V_max values for sucrose with free and immobilised invertase of 81, 114 mM and 10.1, 9.2 mol glucose/min.mg enzyme, respectively. The deactivation rate constants of free and immobilised invertase were 0.0347 and 0.0098 min^–1, respectively.     

H<Subscript>2</Subscript>-Producing bacterial communities from a heat-treated soil inoculum

Hydrogen gas (60% H₂) was produced in a continuous flow bioreactor inoculated with heat-treated soil, and fed synthetic wastewater containing glucose (9.5 g l^–1). The pH in the bioreactor was maintained at 5.5 to inhibit consumption of H₂ by methanogens. The objective of this study was to characterize bacterial communities in the reactor operated under two different hydraulic retention times (HRTs of 30-h and 10-h) and temperatures (30°C and 37°C). At 30-h HRT, the H₂ production rate was 80 ml h^–1 and yield was 0.91 mol H₂/mol glucose. At 10-h HRT, the H₂ production rate was more than 5 times higher at 436 ml h^–1, and yield was 1.61 mol H₂/mol glucose. Samples were removed from the reactor under steady-state conditions for PCR-based detection of bacterial populations by ribosomal intergenic spacer analysis (RISA). Populations detected at 30-h HRT were more diverse than at 10-h HRT and included representatives of Bacillaceae, Clostridiaceae, and Enterobacteriaceae. At 10-h HRT, only Clostridiaceae were detected. When the temperature of the 10-h HRT reactor was increased from 30°C to 37°C, the steady-state H₂ production rate increased slightly to 463 ml h^–1 and yield was 1.8 mol H₂/mol glucose. Compared to 30°C, RISA fingerprints at 37°C from the 10-h HRT bioreactor exhibited a clear shift from populations related to Clostridium acidisoli (subcluster Ic) to populations related to Clostridium acetobutylicum (subcluster Ib).     

Production of extracellular alkaline proteases by <Emphasis Type="Italic">Aspergillus clavatus</Emphasis>

Summary The production of extracellular alkaline proteases from Aspergillus clavatus was evaluated in a culture filtrate medium, with different carbon and nitrogen sources. The fungus was cultivated at three different temperatures during 10 days. The proteolytic activity was determined on casein pH 9.5 at 37 °C. The highest alkaline proteolytic activity (38 U/ml) was verified for culture medium containing glucose and casein at 1% (w/v) as substrates, obtained from cultures developed at 25 °C for 6 days. Cultures developed in Vogel medium with glucose at 2% (w/v) and 0.2% (w/v) NH₄NO₃ showed higher proteolytic activity (27 U/ml) when compared to the cultures with 1% of the same sugar. Optimum temperature was 40 °C and the half-lives at 40, 45 and 50 °C were 90, 25 and 18 min, respectively. Optimum pH of enzymatic activity was 9.5 and the enzyme was stable from pH 6.0 to 12.0.     

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.     

Gel beads composed of collagen reconstituted in alginate

Spherical gel beads of collagen/alginate were prepared by discharging droplets of a mixture containing collagen (1.07-1.9 mg/ml) and alginate (1.2-1.5% w/v) into 1.5% w/v CaCl2 solution at 4°C. Collagen in the gel beads was reconstituted by raising the temperature to 37°C after alginate was liquefied by citrate. Scanning electron microscopy of the beads revealed the characteristic fibrous structure of collagen. To demonstrate the application of this new technique in cell culture, GH3 rat pituitary tumor cells were entrapped and grown in the gel beads. The immobilized cells proliferated to a density of 1.95 x 106 cell/ml which is about an order of magnitude higher than that grown in the alginate beads.     

Thermal inducible expression of xylose isomerase and its performance in a hollow fiber bioreactor

Summary TheEscherichia coli xylose isomerase (EC 5.3.1.5) has been expressed under the control of a thermal inverting promotor system (att-nutL-p-att-N block) and its performance in a hollow fiber bioreactor measured. The conversion of xylose to xylulose was inversely proportional to the flow rate and the system operated up to 60°C. The maximum conversion efficiency observed was 19.05% at 55°C.     

Medium optimization for the production of glucose isomerase from thermophilic Streptomyces thermonitrificans

A thermophilic strain of Streptomyces thermonitrificans produced a high activity of intracellular glucose isomerase (12 U/ml) when grown in a medium containing 1% (w/v) xylose, supplemented with 2% (w/v) sorbitol as the second carbon source, at 50°C for 16 h. Addition of Mg²⁺ enhanced enzyme production but the organism could grow and produce the enzyme in the absence of Co²⁺.The authors are with the Division of Biochemical Sciences, National Chemical Laboratory, Pune 411 008, IndiaNCL Communication No. 5813     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

Increased yield of fructose from glucose employing thermophilic xylose isomerase in water-ethanol mixtures

Summary The isomerization of D-glucose in mixed ethanol-water was studied at various reaction temperatures (40–70 °C), employing glucose isomerase fromStreptomyces phaeochromogenes andClostridium thermohydrosulfuricum, respectively. The thermophilicClostridium enzyme was considerably, more stable towards the combination of organic cosolvent and increased temperature and with this enzyme a 55% yield of fructose from glucose was obtained at relatively low concentration of ethanol (40 %).     

Production of recombinant h-AT III with mammalian cell cultures using capillary electrophoresis for product monitoring

The importance of mammalian cell cultures for biotechnological production processes is steadily increasing, despite the high demands of these organisms on their culture conditions. Efforts towards a more efficient bioprocess generally concentrate on maximizing the culture's life time, the cell number, and the product concentration. Here recombinant BHK 21 c13 cells are used to produce rh-AT III, an anticoagulant of high therapeutic value. The influence of the process mode (batch, repeated batch, continuous perfusion) and the process temperature (30°C vs. 37°C) on the above mentioned parameters is investigated. It is possible to increase the length of the culture from 140 h (batch) to more than 500 h (continuous perfusion culture), while concomitantly increasing the cell density from 0.72 10⁶/ml (batch) to 2.27 10⁶/ml (repeated batch) and 2.87 10⁶/ml (continuous perfusion culture). The accumulation of toxic metabolites, such as lactate, can be curtailed by reducing the bioreactor temperature from 37°C to 30°C during the later part of the exponential growth phase. Fast and reliable product monitoring became essential during process optimization. Capillary zone electrophoresis (CZE) in uncoated fused silica capillaries was studied for that purpose and compared to the standard ELISA. Under optimized conditions an AT III quantification could be done within 2 min with CZE. The detection limit was 5 g/ml. A relative standard deviation of less than 0.9% was calculated. The detection limit could be lowered by one order of magnitude by using a two dimensional system, where an liquid chromatographic (LC) system is coupled to the CZE. Concomitantly the resolution is improved. The two-dimensional analysis required 5 min. Membrane adsorbers (MA) were used as stationary phase in the LC-system, to allow the application of high flow rates (5–10 ml/min). The correlation between the LC-CZE analysis and the standard AT III-ELISA was excellent, with r²: 0.965. Using the assay for at line product monitoring, it is shown, that the process temperature is of no consequence for the productivity whereas the process mode strongly influences this parameter.     

Catalytical properties of <Emphasis Type="Italic">Arthrobacter nicotianae</Emphasis> cells,a producer of glucose isomerase,immobilized inside xerogel of silicium dioxide

Arthrobacter nicotianae cells, producers of glucose isomerase, were immobilized inside xerogel of silicium dioxide, and properties of the resulted heterogeneous biocatalysts were investigated in the process of isomerization of monosaccharide (glucose and fructose). The glucose isomerase activity of the resulted biocatalysts was shown to be 10 U/g, on average, taking into account the loss of the activity upon the immobilization, which amounted to 50% of the cell activity in suspension. The rate of the fructose isomerization increased linearly in the range of 55–80°C with the temperature coefficient 1.3. The biocatalysts were stable in this range; they were rapidly inactivated, however, at increasing temperature. The half-pife time of inactivation was six to seven h and five min or less at 80 and 85°C, respectively. The half-pife time of inactivation of heterogeneous biocatalysts was 50–90 h in the periodic process of isomerization of 2 M monosaccharides at 60°C in the presence of the immobilized Arthrobacter nicotianae cells.     

Optimal covalent immobilization of glucose oxidase-containing liposomes for highly stable biocatalyst in bioreactor

The glucose oxidase-containing liposomes (GOL) were prepared by entrapping glucose oxidase (GO) in the liposomes composed of phosphatidylcholine (PC), dimyristoyl L-alpha-phosphatidylethanolamine (DMPE), and cholesterol (Chol) and then covalently immobilized in the glutaraldehyde-activated chitosan gel beads. The immobilized GOL gel beads (IGOL) were characterized to obtain a highly stable biocatalyst applicable to bioreactor. At first, the glutaraldehyde concentration used in the gel beads activation as well as the immobilizing temperature and time were optimized to enhance the immobilization yield of the GOL to the highest extent. The liposome membrane composition and liposome size were then optimized to obtain the greatest possible immobilization yield of the GOL, the highest possible activity efficiency of the IGOL, and the lowest possible leakage of the entrapped GO during the GOL immobilization. As a result, the optimal immobilization conditions were found to be as follows: the liposome composition, PC/DMPE/Chol = 65/5/30 (molar percentage); the liposome size, 100 nm; the glutaraldehyde concentration, 2% (w/v); the immobilizing temperature, 4 degrees C; and the immobilizing time, 10 h. Furthermore, the optimal IGOL prepared were characterized by its rapidly increasing effective GO activity to the externally added substrate (glucose) with increasing temperature from 20 to 40 degrees C, and also by its high stability at 40 degrees C against not only the thermal denaturation in a long-term (7 days) incubation but also the bubbling stress in a bubble column. Finally, compared to the conventionally immobilized glucose oxidase (IGO), the higher operational stability of the optimal IGOL was verified by using it either repeatedly (4 times) or for a long time (7 days) to catalyze the glucose oxidation in a small-scale airlift bioreactor.