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.     

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.     

Immobilization of <Emphasis Type="Italic">Aspergillus oryzae</Emphasis> α-galactosidase in gelatin and its application in removal of flatulence-inducing sugars in soymilk

Raffinose oligosaccharides (RO) are the major factors responsible for flatulence following ingestion of soybean-derived products. Removal of RO from seeds or soymilk would then have a positive impact on the acceptance of soy-based foods. In this study, α-galactosidase from Aspergillus oryzae was entrapped in gelatin using formaldehyde as the hardener. The immobilization yield was 64.3% under the optimum conditions of immobilization. The immobilized α-galactosidase showed a shift in optimum pH from 4.8 to 5.4 in acetate buffer. The optimum temperature also shifted from 50°C to 57°C compared with soluble enzyme. Immobilized α-galactosidase was used in batch, repeated batch and continuous mode to degrade RO present in soymilk. In the repeated batch, 45% reduction of RO was obtained in the fourth cycle. The performance of immobilized α-galactosidase was tested in a fluidized bed reactor at different flow rates and 86% reduction of RO in soymilk was obtained at 25 ml h⁻¹ flow rate. The study revealed that immobilized α-galactosidase in continuous mode is efficient in reduction of RO present in soymilk.     

Immobilization of cyclodextrin glucanotransferase on capillary membrane

A bioreactor system with the enzyme immobilized on a capillary membrane is a promising tool for the mass production of valuable substances, because of the good productive efficiency. To investigate the kinetics of immobilized cyclodextrin glucanotransferase ([EC 2.4.1.19]; CGTase) on a capillary membrane in a bioreactor system, the amount of immobilized CGTase and the operating conditions, such as pressure and the reaction temperature, were examined under a constant substrate concentration (1.0%) and a constant flow rate (0.12 m/s). When the CGTase was immobilized at a concentration of 0.04 to 0.62 mg per membrane area (cm²), the decrease in the immobilized amount of CGTase resulted in an increase in the cyclodextrin production rate (g of CD/h·m²; CPR) and the CPR correlated well with the flux of the CGTase-immobilized membrane. Although a higher reaction temperature caused an increase in the CPR within a short operating time of the bioreactor, repeated operation at 60°C led to a reduction in the CPR due to the denaturation of the immobilized CGTase. The percentage of cyclodextrin (CD) to total sugar obtained in the permeate was slightly more than 60% under most operating conditions, but immobilization of the excess amount of CGTase (0.42–0.62 mg/cm²) reduced the CD yield as well as the ratio of α-CD to β-CD, suggesting that it led to a CGTase side-reaction such as intermolecular transglycosylation. These data suggest that the conditions under which the bioreactor with 0.04–0.40 mg/cm² was operated; a reaction temperature of 50°C, a residence time of 1–2 min and adjustable pressure, could be employed to obtain a high CPR using a large scale CGTase-immobilized membrane bioreactor.     

Immobilization of chitosan-modified invertase on alginate-coated chitin support via polyelectrolyte complex formation

Saccharomyces cerevisiae invertase was chemically modified with chitosan and further immobilized on sodium alginate-coated chitin support. The yield of immobilized protein was determined as 85% and the enzyme retained 97% of the initial chitosan-invertase activity. The optimum temperature for invertase was increased by 10 °C and its thermostability was enhanced by about 9 °C after immobilization. The immobilized enzyme was stable against incubation in high ionic strength solutions and was four-fold more resistant to thermal treatment at 65 °C than the native counterpart. The biocatalyst prepared retained 80% of the original catalytic activity after 50 h under continuous operational regime in a packed bed reactor.     

Immobilization of invertase on a new type of macroporous glycidyl methacrylate

Invertase was immobilized via its carbohydrate moiety. The immobilized enzyme has a specific activity of 5500 IU g^–1, with 45% activity yield on immobilization. In a packed bed reactor, 90% 2.5 M sucrose was converted at a flow rate of 4 bed volumes h^–1. The obtained specific productivity at 40 °C of 3 kg l^–1 h^–1 is the best one so far. Long-term stability was 290 days in 2.5 M sucrose at 40 °C and at a flow rate of 3 bed volumes h^–1.     

Hydrolysis of Galacto-oligosaccharides in Soymilk by κ-carrageenan-entrapped α-galactosidase from Aspergillus Oryzae

Summary α-Galactosidase was immobilized in κ-carrageenan. The optimum pH of the soluble enzyme and immobilized enzyme was 4.8. The optimum temperature of the soluble enzyme was 50 °C and that of the immobilized enzyme was increased to 53 °C. The immobilized enzyme was used in batch, repeated batch, and in the continuous mode to degrade the raffinose family sugars present in soymilk. Two hours incubation with free and immobilized α-galactosidase resulted in 88 and 75% reduction in raffinose family oligosaccharides in soymilk respectively. In the repeated batch, 61% reduction was obtained in the fourth cycle. A fluidized bed reactor was designed to treat soymilk continuously. The performance of immobilized α-galactosidase was also tested in a fluidized bed reactor at different flow rates and 92% reduction of raffinose family oligosaccharides in soymilk was obtained at 25 ml h⁻¹ flow rate. The study revealed that immobilized α-galactosidase in continuous mode is efficient in reducing the oligosaccharides present in the soymilk.     

Biosynthesis of γ-aminobutyric acid (GABA) using immobilized whole cells of <Emphasis Type="Italic">Lactobacillus brevis</Emphasis>

On an industrial scale, the production of γ-aminobutyric acid (GABA) from the cheaper sodium L-glutamate (L-MSG) is a valuable process. By entrapping Lactobacillus brevis cells with higher glutamate decarboxylase (GAD) activity into Ca-alginate gel beads, the biotransformation conditions of L-MSG to GABA were optimized with the immobilized cells. The cells obtained from a 60-h culture broth showed the highest biotransformation efficiency from L-MSG to GABA. The optimal cell density in gel beads, reaction pH and temperature were 11.2 g dry cell weight (DCW) l⁻¹, 4.4 and 40°C respectively. The thermal stability of immobilized cells was significantly higher than free cells. Under the optimized reaction conditions, the yield of GABA reached above 90% during the initial five batches and the yield still remained 56% in the tenth batch. Continuous production of GABA was realized with a higher yield by incorporating cell re-cultivation using the packed bed reactor.     

Immobilization on Eupergit C of cyclodextrin glucosyltransferase (CGTase) and properties of the immobilized biocatalyst

The extreme thermophilic cyclodextrin glucanotransferase (CGTase) from Thermoanaerobacter sp. was covalently attached to Eupergit C. Different immobilization parameters (incubation time, ionic strength, pH, ratio enzyme/support, etc.) were optimized. The maximum yield of bound protein was around 80% (8.1 mg/g support), although the recovery of β-cyclodextrin cyclization activity was not higher than 11%. The catalytic efficiency was lower than 15%. Results were compared with previous studies on covalent immobilization of CGTase.

The enzymatic properties of immobilized CGTase were investigated and compared with those of the soluble enzyme. Soluble and immobilized CGTases showed similar optimum temperature (80–85 °C) and pH (5.5) values, but the pH profile of the immobilized CGTase was broader at higher pH values. The thermoinactivation of the CGTase coupled to Eupergit C was slower than the observed with the native enzyme. The half-life of the immobilized enzyme at 95 °C was five times higher than that of the soluble enzyme. The immobilized CGTase maintained 40% of its initial activity after 10 cycles of 24 h each. After immobilization, the selectivity of CGTase (determined by the ratio CDs/oligosaccharides) was notably shifted towards oligosaccharide production.     

聚氨酯固定化热带假丝酵母发酵木糖醇

固定在多孔聚氨酯载体中的热带假丝酵母(Candida tropicalis), 可有效地利用玉米芯半纤维素水解液生产木糖醇。在摇瓶条件下, 采用分批发酵方式, 确立了适宜的发酵工艺参数为: 接种量7%, 聚氨酯加入量1.0 g/100 mL, 温度30°C, 初始pH值6.0, 分段改变摇床转速进行溶氧调节, 其中0~24 h 为200 r/min; 24 h~46 h为140 r/min。聚氨酯固定化提高了菌体对发酵抑制物的耐受力, 固定化细胞密度高, 发酵性能稳定, 发酵产率和体积生产速率都有所提高。水解液未经脱色与离子交换便可转化成木糖醇, 大幅降低了成本, 显示了良好的应用前景。固定化细胞连续重复进行12批次21 d的发酵, 木糖醇得率平均为67.6%, 体积生产速率平均为1.92 g/(L·h)。     

Synthesis of Cyclodextrin glycosyl transferase by immobilized cells of Bacillus circulans

The cells of Bacillus circulans (ATCC 21783) immobilized in sodium alginate gel matrix were able to synthesize the extracellular enzyme, Cyclodextrin glycosyl transferase (CGTase, E.C. 2.4.1.19) which is industrially employed for the preparation of cyclodextrins. Optimization for the maximum production of enzyme was carried out by varying the cell density (3.3–53.5 kg/m³) in the gel and the incubation temperature (30°–42°C). The CGTase activity was found to be the highest (45 units/cm³) with maximum cell loading at 37°C. The reusability of immobilized cells was ascertained by repeated batch experiments. The enzyme activity exhibited was in the range of 50 to 55 units/cm³ in each batch. The continuous synthesis of CGTase by immobilized cells has been demonstrated by operating a fluidized bed reactor at a dilution rate 1.1 · 10^–4 sec^–1 for a period of 15 days. The enzyme activity has decreased to 42.5 units/cm³ from an initial value of 61 units/cm³ during continuous operation.The authors are grateful to Dr. A.D. Damodaran, Director, Regional Research Laboratory, Trivandrum for his keen interest and encouragement and to Department of Biotechnology, Government of India, New Delhi for financial support.     

Enhancing operational stability and exhibition of enzyme activity by removing water in the immobilized lipase‐catalyzed production of erythorbyl laurate

Erythorbyl laurate was continuously synthesized by esterification in a packed‐bed enzyme reactor with immobilized lipase from Candida antarctica. Response surface methodology based on a five‐level three‐factor central composite design was adopted to optimize conditions for the enzymatic esterification. The reaction variables, such as reaction temperature (10–70°C), substrate molar ratio ([lauric acid]/[erythorbic acid], 5–15), and residence time (8–40 min) were evaluated and their optimum conditions were found to be 56.2°C, 14.3, and 24.2 min, respectively. Under the optimum conditions, the molar conversion yield was 83.4%, which was not significantly different (P < 0.05) from the value predicted (84.4%). Especially, continuous water removal by adsorption on an ion‐exchange resin in a packed‐bed enzyme reactor improved operational stability, resulting in prolongation of half‐life (2.02 times longer compared to the control without water‐removal system). Furthermore, in the case of batch‐type reactor, it exhibited significant increase in initial velocity of molar conversion from 1.58% to 2.04%/min. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:882–889, 2013     

Enhanced bioconversion of colchicine to regiospecific 3-demethylated colchicine (3-DMC) by whole cell immobilization of recombinant E. coli harboring P450 BM-3 gene

Biotransformation of colchicine into regiospecific 3-demethylated colchicine (3-DMC) which is pharmacologically active and a potent anti-cancer drug, mediated by immobilization of recombinant microbial monooxygenases is a novel and promising strategy for its production. In the present study, recombinant Escherichia coli expressing P450 BM-3 was immobilized in calcium-alginate beads and its ability to catalyze colchicine into 3-DMC was investigated. Characteristics of immobilized system showed that optimum conditions for activity of microbial cells were not affected due to immobilization. The optimum pH and temperature for both free and immobilized cells were found to be 7.5 and 37.5 °C, respectively. Experimental variables under consideration such as Ca²⁺ concentration, alginate concentration, P450 BM-3 enzyme activity and colchicine concentration were optimized using response surface methodology. The immobilized cells exhibited a markedly improved thermal stability as compared to free cells. The yield of 3-DMC with immobilized microbial cells was found to be an average of 69%, with 82, 73 and 52% across three independent batches in succession as against bioconversion by free cells, which indicated improved operational stability and reusability of immobilized cells in batch processes. Additionally, a packed bed reactor has been proposed for the immobilized biocatalytic system for bioconversion of colchicine and other biochemicals.     

Cu2+ Removal and recovery by Spi SORB: batch stirred and up-flow packed bed columnar reactor systems

The biosorption of Cu²⁺ by free and poly acrylamide gel (PAG) immobilized Spirulina platensis (SpiSORB) was characterized under batch and continuous packed bed columnar reaction systems. The biosorption of Cu²⁺ was shown to be highest at pH of 6.0 for both types of biomass. The PAG immobilization process did not interfere with the Cu²⁺ binding sites present on biomass leading to cent percent (ca. 250 mg g⁻¹ of dry biomass) retention of biosorption as compared to free cells. Transmission electron microscopy on Cu²⁺ localization revealed that majority of metal is being sequestered by the cell wall only. The infrared spectrum of metal treated S. platensis biomass indicated the possible involvement of amide, amino, and carboxyl groups in metal binding. Up-flow packed bed columnar reactor containing 2.0 g of PAG immobilized S. platensis shown a maximum of 143-fold volume reduction factor at the residence time of 4.6 min for Cu²⁺ alone and found to decrease dramatically when Zn²⁺ is present in a bimetallic solution.     

Bio catalytic oxidation of sulphide laden wastewater from leather industry using sulfide: Quinone oxidoreductase immobilized bio reactor

Abstract

Anaerobic treatment of sulphate rich wastewater results in high amount of sulphide in liquid phase and gaseous phase. Sulphide is malodorous in gaseous phase and toxic even at very low concentrations in liquid phase and causes objectionable environmental issues. In the present investigation the sulphide present in the UASB treated post tanning wastewater was oxidised into elemental sulphur using Sulfide: Quinone oxidoreductase (SQR) immobilized Functionalized Carbon-silica matrix (FCSM) packed bed reactor. The variables employed for the production of Bacillus clausii biomass for the extraction of SQR were optimized using RSM. The purified SQR showed the maximum activity and stability at pH 6.0 to 8.0 and the percentage oxidation of sulphide at HRT of 24?h were 99.2%?±?0.2 at pH 6.0; 99.6%?±?0.2 at pH 7.0 and 99.6%?±?2.12 at pH 8.0. The effect of temperature on SQR activity was optimized and it established the maximum activity and stability at 40?°C with sulphide oxidation of 99.6%?±?0.8%. The optimum conditions for immobilization of SQR onto FCSM were time, 240?min; pH, 7.0; temperature, 40?°C and SQR concentration, 10?mg/g. The immobilization of SQR onto FCSM obeyed the Langmuir isotherm model. The immobilization of SQR onto FCSM was confirmed by SEM, FT-IR, XRD, TGA and DSC analyses. The SQR-FCSM packed bed reactor was operated separately for the oxidation of sulfide in UASB treated post-tanning wastewater under continuous mode at different HRTs and it recorded the maximum sulphide oxidation by 99?±?0.1% at HRT of 15?h with residual sulphide of 2.4?±?1.1?mg/L. The formation of elemental Sulphur was confirmed by XRD studies. The present investigation provides the scope for the removal of sulphide and thereby substantial reduction in Total Dissolved Solids from post tanning wastewater without addition of chemicals.     

Development of Bed Reactor Using Brick Dust Immobilized CIVI-Cellulase from Seeds of Cowpea (Vigna sinensis L)

Cellulase extracted from seeds of Cowpea (Vigna sinensis L var VITA-4) was partially purified and immobilized on brick dust as solid support via glutaraldehyde. The percentage retention of the enzyme activity on brick dust was nearly 85%. After immobilization specific activity of the enzyme increased from 0.275 to 0.557 U mg^?1 protein with about 2 fold enrichment. The optimum pH and temperature of soluble enzyme were determined as pH 4.6 and WC, respectively whereas immobilized enzyme showed at pH 5.0 and 37°C, respectively. The V_max values for soluble and immobilized enzyme were determined as 6.67 and 1.25 mg min^?1, respectively whereas K_m values were 4.35 and 4.76 mg ml^?1, respectively. The immobilized enzyme displayed higher thermal stability than soluble enzyme and retained about 50% of its initial activity after 12 reuses. Immobilized enzyme was packed in an indigenously designed double walled glass bed reactor for continuous production of reducing sugars.     

Studies on microbial glucose isomerase: 4. Characteristics of immobilized whole-cell glucose isomerase from Streptomyces spp.

Whole-cell glucose isomerase from a Streptomyces spp. was immobilized by entrapment in gelatin matrices crosslinked with glutaraldehyde. The resultant immobilized enzyme preparation had up to 40% recovery yield of the activity and showed relatively long stabilities during storage and the isomerizing reaction. The storage half-life of the preparation was 19 months at 5°C and the half-life of the enzyme during operation was 260 days in the presence of 1 mM Co²⁺ and 80 days in the absence of the metal ion. Optimum pH and temperature were 7.5 and 70–75°C, respectively. The K_m values for glucose and fructose were 0.29 and 0.46 m, respectively, with a maximum theoretical conversion yield of 56%. The simulation results based on the reversible one-substrate enzyme kinetic model agreed well with the experimental data obtained from a batch reactor. The continuous operation of packed bed reactors demonstrated that some effects of the external film diffusion resistance were apparent at low flow rates of the substrate feed solution, whereas the internal pore diffusion resistance was negligible up to the pellet size used in this work.     

Immobilization ofSaccharomyces diastaticus on wood chips for ethanol production

Saccharomyces diastaticus cells were immobilized onto beech wood chips of different particle size and three pH values. pH values in the range 5.0–6.0, and 1.84–1.92 mm particle size had a positive effect on the immobilization process. The chosen carrier—1.84 mm-sized wood chips adsorbed 150 mg dry cell mass per g dry carrier mass. The Gibbs free energy and the activation energy for the first (monolayer) and second (multilayer) immobilization stages was 4581, 19090 and 8590 J g mol⁻¹, respectively. The kinetics of immobilized cell systems in ethanol production have been studied in a packed bed-reactor. Ethanol production and the respiration quotient (RQ) were at a maximum at a dilution rate of 0.16/h. The reactor was operated under steady-state conditions for 30 d at the dilution rate 0.16/h.     

Enzymatic preparation of fatty acid esters of sugar alcohols by condensation in acetone using a packed-bed reactor with immobilized Candida antarctica lipase

Mono- and dilauroyl arabitols, ribitols, xylitols and sorbitols were synthesized batchwise or continuously at 50°C or 60°C by condensation catalyzed by an immobilized Candida antarctica lipase in acetone. Continuous production was realized using a system where a column packed with sugar alcohol and a packed-bed reactor with the immobilized lipase were connected in series. The concentrations of the mono- and dilauroyl esters of each sugar alcohol became almost constant at mean residence times of 15 min or longer in the packed-bed reactor. The monolauroyl, monomyristoyl and monopalmytoyl arabitols, ribitols, xylitols and sorbitols were continuously produced using the reactor system at 60°C, and the productivity was in the range of 1.3–2.0 kg L^?1-reactor·day except for the fatty acid esters of sorbitol, the productivity of which was 0.6–0.8 kg L^?1-reactor·day.     

Production of ethanol by adsorbed yeast cells

Summary Various ion exchange resins were tested for their ability to adsorb cells of Saccharomyces cerivisiae with the ultimate intention of developing a packed bed immobilized cell reactor for the continuous production of ethanol. The resins varied greatly in their ability to adsorb cells - the least effective resins retained less than 1 mg S. cerivisiae cells (dry weight)/g of resin (dry weight), and the most effective, 130–140 mg cells/g of resin. A column reactor packed with adsorbed yeast cells was operated continuously for over 200 hours using a 12% (w/v) glucose medium at dilution rates of 1.1 h^-1 and 1.44 h^-1 (based on void volume). High ethanol productivities of 53.1 and 62.0 g ethanol/l-h were obtained.