A comparative study on the production of amidase using immobilized and dehydrated immobilized cells of Pseudomonas putida MTCC 6809

Pseudomonas putida MTCC 6809, a plant growth promoting rhizobacteria producing amidase was isolated from the rhizosphere of Pisum sativum. The cells were immobilized in sodium alginate for the production of amidase and the effect of dehydration on immobilized beads were studied. Optimization of process parameters for amidase production was carried out to enhance enzyme production using immobilized cells. From the results it is clear that 2% and 3% (w/v) of alginate were suitable for amidase production with 12.8 and 13 U/ml activity, respectively after 36 h of incubation. Among the various substrates studied acetamide (2% w/v) was a good inducer of amidase. It was observed that immobilized catalysts could be recycled up to five batches. Amidase production was observed in both free and immobilized cells, nevertheless immobilization is much favored in comparison to free cells, as it leads to reusability of beads, lesser contamination, consistent amidase production and adaptability to wide range of culture conditions. The relative enzyme activity with the dehydrated beads was only 27% in comparison to hydrated beads, it is possible to pack considerably more into a fixed volume as the relative volume of dehydrated beads is 20%. Even though consistent amidase production was difficult to achieve using dehydrated beads, which may have certain advantages like less chances for microbial contamination and easy to transport.     

Preparation of active corn peptides from zein through double enzymes immobilized with calcium alginate–chitosan beads

Double enzymes (alcalase and trypsin) were effectively immobilized in a composite carrier (calcium alginate–chitosan) to produce immobilized enzyme beads referred to as ATCC. The immobilization conditions for ATCC were optimized, and the immobilized enzyme beads were characterized. The optimal immobilization conditions were 2.5% of sodium alginate, 10:4 sodium alginate to the double enzymes, 3:7 chitosan solution to CaCl₂ and 2.5 h immobilization time. The ATCC beads had greatly enhanced stability and good usability compared with the free form. The ATCC residual activity was retained at 88.9% of DH (degree of hydrolysis) after 35 days of storage, and 36.0% of residual activity was retained after three cycles of use. The beads showed a higher zein DH (65.8%) compared with a single enzyme immobilized in the calcium alginate beads (45.5%) or free enzyme (49.3%). The ATCC kinetic parameters V_max and apparent K_m were 32.3 mL/min and 456.62 g⁻¹, respectively. Active corn peptides (CPs) with good antioxidant activity were obtained from zein in the ethanol phase. The ATCC might be valuable for preparing CPs and industrial applications.     

Dried alginate-entrapped enzymes (DALGEEs) and their application to the production of fructooligosaccharides

A modification of the classical calcium alginate enzyme entrapment technique is described aiming to overcome some of the limitations of the former gel-based biocatalysts. Dried alginate entrapped enzymes (DALGEEs) were obtained dehydrating calcium alginate gel beads containing entrapped enzymes. A fructosyltransferase from Aspergillus aculeatus, present in Pectinex Ultra SP-L, was entrapped using this technique. The resulting DALGEEs were successfully tested both operating batchwise and in a continuous fixed-bed reactor for fructooligosaccharides (FOS) synthesis from sucrose. Interestingly, DALGEEs did not re-swell upon incubation in concentrated (600 g/L) sucrose solutions, probably due to the lowered water activity (a_w) of such media. Confocal laser scanning microscopy of DALGEEs revealed that the enzyme molecules accumulated preferably in the shell of the particles. DALGEEs showed an approximately 30-fold higher volumetric activity (300 U/mL) compared with the calcium alginate gel beads. Moreover, a significant enhancement (40-fold) of the space-time-yield of fixed-bed bioreactors was observed when using DALGEEs as biocatalyst compared with gel beads (4030 g/day L of FOS vs. 103 g/day L). The operational stability of fixed-bed reactors packed with DALGEEs was extraordinary, providing a nearly constant FOS composition of the outlet during at least 700 h. It was also noticeable their resistance against microbial attack, even after long periods of storage at room temperature. The DALGEEs immobilisation strategy may also be useful for other biotransformations, in particular when they take place in low a_w media.     

Influence of whole microalgal cell immobilization and organic solvent on the bioconversion of androst-4-en-3,17-dione to testosterone by Nostoc muscorum

The use of free, immobilized and reused immobilized cells of the microalga Nostoc muscorum was studied for bioconversion of androst-4-en-3,17-dione (AD) to testosterone in hexadecane. Among polymers such as agar, agarose, κ-carrageenan, polyacrylamide, polyvinyl alcohol, and sodium alginate that were examined for cell entrapment, sodium alginate with a concentration of 2% (w/v) proved to be the proper matrix for N. muscorum cells immobilization. The bioconversion characteristics of immobilized whole algal cells at ranges of temperatures, substrate concentrations, and shaking speeds were studied followed by a comparison with those of free cells. The conditions were 30 °C, 0.5 g/L, and 100 rpm, respectively. The immobilized N. muscorum showed higher yield (72 ± 2.3%) than the free form (24 ± 1.3%) at the mentioned conditions. The bioconversion yield did not decrease during reuse of immobilized cells and remained high even after 5 batches of bioreactions while Na-alginate 3% was used; however, reuse of alginate 2% beads did not give a satisfactory result.     

Surfactant-mediated permeabilization of Pseudomonas putida KT2440 and use of the immobilized permeabilized cells in biotransformation

Surfactants were used to permeabilize cells of Pseudomonas putida KT2440 so as to maximize retention of the arginine deiminase (ADI) activity within the treated cells. The surfactants cetyltrimethylammoniumbromide (CTAB), sodium dodecyl sulfate (SDS) and Triton X100 were tested separately. Statistical models were developed for the effects on the ADI activity of the following factors: the concentration of the surfactant, the length of the treatment period and the concentration of the cells. For all surfactants, the concentration of cells was the most significant factor in influencing permeabilization. All permeabilization treatments used mild conditions (pH 7, 37 °C). The permeabilized cells were immobilized in alginate beads for the biotransformation of arginine to citrulline. The optimal conditions for immobilization and biotransformation were as follows: 2% (w/v, g/100 mL) sodium alginate, 100 g/L of treated cells, 40 mM arginine, pH 6.0, a temperature of 35 °C and an agitation speed of 150 rpm. The immobilized biocatalyst retained nearly 90% of its initial activity after nine cycles of repeated use in batch operations. In contrast, the freely suspended cells were barely active after the second use cycle.     

Encapsulation of lactate dehydrogenase in carbon nanotube doped alginate–chitosan capsules

Alginate–chitosan shell–core (AC) capsules doped with carbon nanotubes (CNTs) were prepared for lactate dehydrogenase (LDH, EC 1.1.1.27) encapsulation to convert pyruvic acid to lactic acid coupling with the oxidation of NADH to NAD⁺. LDH was entrapped within the liquid core of the capsules and the CNTs were incorporated in the alginate or chitosan matrices or both. The physical properties of the capsules and the immobilized LDH activity were investigated. The AC capsules doped with CNTs showed better mechanical strength than that without CNTs. The LDH loading efficiency of the AC capsules with CNTs (10 mg/mL) doped in both the shell and the core was 30.7% higher than that without CNTs. The optimal pH value for the bioconversion catalyzed by immobilized LDH was 7.0, lower than that by free LDH (7.5). The optimal temperature was 35 °C for both immobilized and free LDH. Operational stability of the immobilized LDH was greatly improved by doping CNTs in AC capsules. The results showed that this method was efficient for enzyme encapsulation in the biotechnology applications.     

Enzymatic transformation of 2-O-α-d-glucopyranosyl-l-ascorbic acid (AA-2G) by immobilized α-cyclodextrin glucanotransferase from recombinant Escherichia coli

This work aims to produce 2-O-α-d-glucopyranosyl-l-ascorbic acid (AA-2G) from ascorbic acid and β-cyclodextrin with immobilized α-cyclodextrin glucanotransferase (α-CGTase) from recombinant Escherichia coli. Molecular sieve (SBA-15) was used as an adsorbent, and sodium alginate was used as a carrier, and glutaraldehyde (GA) was used as a cross-linker. The effects of several key variables on α-CGTase immobilization were examined, and optimal immobilization conditions were determined as the following: glutaraldehyde (GA, cross-linker) 0.01% (v/v), SBA-15 (adsorbent) 2 g/L, CaCl₂ 3 g/L, sodium alginate 20 g/L, adsorption time 3 h, and immobilization time 1 h. In comparison with free α-CGTase, immobilized α-CGTase had a similar optimal pH (5.5) and a higher optimal temperature (45 °C). The continuous production of AA-2G from ascorbic acid and β-cyclodextrin in the presence of immobilized α-CGTase was carried out, and the highest AA-2G production reached 21 g/L, which was 2-fold of that with free α-CGTase. The immobilization procedure developed here was efficient for α-CGTase immobilization, which was proved to be a prospective approach for the enzymatic production of AA-2G.     

Application of chitosan beads immobilized Rhodococcus sp. NCIM 2891 cholesterol oxidase for cholestenone production

The cell-bound cholesterol oxidase from the Rhodococcus sp. NCIM 2891 was purified three fold by diethylaminoethyl–sepharose chromatography. The estimated molecular mass (SDS-PAGE) and K_m of the enzyme were ∼55.0 kDa and 151 μM, respectively. The purified cholesterol oxidase was immobilized on chitosan beads by glutaraldehyde cross-linking reaction and immobilization was confirmed by Fourier transform infrared spectroscopy, scanning electron microscopy and energy dispersive X-ray analysis. The optimum temperature (45 °C, 5 min) for activity of the enzyme was increased by 5 °C after immobilization. Both the free and immobilized cholesterol oxidases were found to be stable in many organic solvents except for acetone. Fe²⁺ and Pb²⁺ at 0.1 mM of each acted as inhibitors, while Ag⁺, Ca²⁺, Ni²⁺ and Zn²⁺ activated the enzyme at similar concentration. The biotransformation of cholesterol (3.75 mM) with the cholesterol oxidase immobilized beads (3.50 U) leads to ∼88% millimolar yield of cholestenone in a reaction time of 9 h at 25 °C. The immobilized enzyme retains ∼67% activity even after 12 successive batches of operation. The biotransformation method thus, shows a great promise for the production of pharmaceutically important cholestenone.     

Covalent immobilization of ω-transaminase from Vibrio fluvialis JS17 on chitosan beads

Chitosan beads were prepared by emulsion method and used for the immobilization of ω-transaminase of Vibrio fluvialis. The yield of enzyme immobilization (54.3%) and its residual activity (17.8%) were higher than those obtained with other commercial beads. ω-Transaminase was effectively immobilized on the chitosan beads at pH 6.0. The optimal pH of the immobilized enzyme was pH 9.0, which is the same as that of the free enzyme. The immobilized enzyme on chitosan beads retained ca. 77% of its conversion after five consecutive reactions with the 25 mM substrate, while the immobilized enzyme on Eupergit^® C retained 12%. Also, the immobilized ω-transaminase on chitosan bead retained 70% of initial activity when it's stored at 4 °C for 3.5 weeks. Addition of the co-factor, pyridoxal 5-phosphate (PLP), was needed to maintain the stability of the immobilized ω-transaminase.     

Inulinase production by the marine yeast Cryptococcus aureus G7a and inulin hydrolysis by the crude inulinase

The marine yeast strain G7a isolated from sediment of China South Sea was found to secrete a large amount of inulinase into the medium. This marine yeast strain was identified to be a strain of Cryptococcus aureus according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast showed the highest activity at pH 5.0 and 50 °C. The optimal medium for inulinase production was artificial seawater containing inulin 4.0% (w/v), K₂HPO₄ 0.3% (w/v), yeast extract 0.5% (w/v), KCl 0.5% (w/v), CaCl₂ 0.12% (w/v), NaCl 4.0% (w/v) and MgCl₂·6H₂O 0.6% (w/v), while the optimal cultivation conditions for inulinase production were pH 5.0, a temperature of 28 °C and a shaking speed of 170 rpm. Under the optimal conditions, over 85.0 U/ml of inulinase activity was produced within 42 h of fermentation at shake flask level. This is very high level of inulinase activity produced by yeasts. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.     

Optimization of date syrup for enhancement of the production of citric acid using immobilized cells of Aspergillus niger

Date syrup as an economical source of carbohydrates and immobilized Aspergillus niger J4, which was entrapped in calcium alginate pellets, were employed for enhancing the production of citric acid. Maximum production was achieved by pre-treating date syrup with 1.5% tricalcium phosphate to remove heavy metals. The production of citric acid using a pretreated medium was 38.87% higher than an untreated one that consumed sugar. The appropriate presence of nitrogen, phosphate and magnesium appeared to be important in order for citric acid to accumulate. The production of citric acid and the consumed sugar was higher when using 0.1% ammonium nitrate as the best source of nitrogen. The production of citric acid increased significantly when 0.1 g/l of KH₂PO₄ was added to the medium of date syrup. The addition of magnesium sulfate at the rate of 0.20 g/l had a stimulating effect on the production of citric acid. Maximum production of citric acid was obtained when calcium chloride was absent. One of the most important benefits of immobilized cells is their ability and stability to produce citric acid under a repeated batch culture. Over four repeated batches, the production of citric acid production was maintained for 24 days when each cycle continued for 144 h. The results obtained in the repeated batch cultivation using date syrup confirmed that date syrup could be used as a medium for the industrial production of citric acid.     

Immobilization of tomato (Lycopersicon esculentum) pectinmethylesterase in calcium alginate beads and its application in fruit juice clarification

Clarity of fruit juices is desirable to maintain an aesthetically pleasing quality and international standards. The most commonly used enzymes in juice industries are pectinases. A partially-purified pectinmethylesterase from tomato was entrapped in calcium alginate beads and used for juice clarification. The activity yield was maximum at 1 % (w/v) CaCl₂ and 2.5 % (w/v) alginate. The immobilized enzyme retained ~55 % of its initial activity (5.7 × 10^?2 units) after more than ten successive batch reactions. The K_m, pH and temperature optima were increased after immobilization. The most effective clarification of fruit juice (%T₆₂₀ ~60 %) by the immobilized enzyme was at 4 °C with a holding time of 20 min. The viscosity dropped by 56 % and the filterability increased by 260 %. The juice remains clear after 2 months of storage at 4 °C.     

Immobilizing cholesterol oxidase in chitosan–alginic acid network

Proton conducting biopolymer networks have potential use for bio-sensors. The cost-effective, non-hazardous and environmentally safe biopolymer, such as chitosan, is an attractive feature for bio-sensors. Cholesterol oxidase was immobilized in conducting network via complexation of chitosan with alginic acid. A method for the preparation of the complex along with characterization by elemental analysis, FTIR spectroscopy, TGA and DSC were reported. The proton conductivity chitosan–alginic acid network was studied via impedance spectroscopy under humidified condition. The complex polymer electrolyte with x = 1 exhibited maximum proton conductivity of 1.4 × 10^?3 S/cm at RT, RH ～ 50%. The potential use of this network in enzyme immobilization was studied by manufacturing cholesterol oxidase entrapped polymer networks. Additionally, the maximum reaction rate (V_max) and Michaelis–Menten constant (K_m) were investigated for the immobilized cholesterol oxidase. Also, temperature and pH optimization studies were performed, and operational stability and shelf life of the polymer network were examined.     

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.     

Optimized endodextranase-epoxy CIM® disk reactor for the continuous production of molecular weight-controlled prebiotic isomalto-oligosaccharides

An epoxy-activated monolithic Convective Interaction Media (CIM^®) disk was used for the immobilization of endodextranase D8144 from Penicillium sp. (EC 3.2.1.11) in order to produce on-line isomalto-oligosaccharides (IMOs) from Dextran T40. Enzymatic parameters, molecular weight of IMOs and performance of the IMmobilized Enzymes Reactor (IMER) were investigated. The immobilization yield of enzymes was about 45.3% (w/w), and the real specific activity close to 3.26 U mg⁻¹. The K_m values did not significantly change between free (12.8 g L⁻¹) and immobilized enzymes (14.2 g L⁻¹), due to the absence of diffusional limitation. The IMER system presented more than 80% of its residual activity after 5000 column volumes, highlighting the high stability of the immobilized endodextranases. Response surface methodology was used to enhance the performance of the IMER. Depending on dextran concentrations and flow rates, specific patterns of IMOs distributions were observed during the enzymatic hydrolysis. Finally, prebiotic activity was also investigated on IMOs produced by medium conditions (flow rate 0.3 mL min⁻¹ and dextran concentrations 4% w/w) against Lactobacillus rhamnosus GG (ATCC 53103). Their scores were at least as good as two commercialized fructo-oligosaccharides (FOS), Fibrulose^® F97 and Orafti^® P95.     

Decolorization of azo dye by immobilized Pseudomonas luteola entrapped in alginate–silicate sol–gel beads

Pseudomonas luteola was immobilized by entrapment in alginate–silicate sol–gel beads for decolorization of the azo dye, Reactive Red 22. The influences of biomass loading and operating conditions on specific decolorization rate and dye removal efficiency were studied in details. The immobilized cells were found to be less sensitive to changes in agitation rates (dissolved oxygen levels) and pH values. Michaelis–Menten kinetics could be used to describe the decolorization kinetics with the kinetic parameters being 36.5 mg g⁻¹ h⁻¹, 300.1 mg l⁻¹ and 18.2 mg g⁻¹ h⁻¹, 449.8 mg l⁻¹ for free and immobilized cells, respectively. After five repeated batch cycles, the decolorization rate of the free cells decreased by nearly 54%, while immobilized cells still retained 82% of their original activity. The immobilized cells exhibited better thermal stability during storage and reaction when compared with free cells. From SEM observation, a dense silicate gel layer was found to surround the macroporous alginate–silicate core, which resulted in much improved mechanical stability over that of alginate beads when tested under shaking conditions. Alginate–silicate matrices appeared to be the best matrix for immobilization of P. luteola in decolorization of Reactive Red 22 when compared with previous results using synthetic or natural polymer matrices.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

Industrial application of α-galactosidase requires efficient methods to immobilize the enzyme, yielding a biocatalyst with high activity and stability compared to free enzyme. An α-galactosidase from tomato fruit was immobilized on galactose-containing polymeric beads. The immobilized enzyme exhibited an activity of 0.62 U/g of support and activity yield of 46%. The optimum pH and temperature for the activity of both free and immobilized enzymes were found as pH 4.0 and 37 °C, respectively. Immobilized α-galactosidase was more stable than free enzyme in the range of pH 4.0–6.0 and more than 85% of the initial activity was recovered. The decrease in reaction rate of the immobilized enzyme at temperatures above 37 °C was much slower than that of the free counterpart. The immobilized enzyme shows 53% activity at 60 °C while free enzyme decreases 33% at the same temperature. The immobilized enzyme retained 50% of its initial activity after 17 cycles of reuse at 37 °C. Under same storage conditions, the free enzyme lost about 71% of its initial activity over a period of 7 months, whereas the immobilized enzyme lost about only 47% of its initial activity over the same period. Operational stability of the immobilized enzyme was also studied and the operational half-life (t_1/2 was determined as 6.72 h for p-nitrophenyl α-d-galactopyranoside (PNPG) as substrate. The kinetic parameters were determined by using PNPG as substrate. The K_m and V_max values were measured as 1.07 mM and 0.01 U/mg for free enzyme and 0.89 mM and 0.1 U/mg for immobilized enzyme, respectively. The synthesis of the galactose-containing polymeric beads and the enzyme immobilization procedure are very simple and also easy to carry out.     

A comparison of the kinetic properties of free and immobilized Aspergillus oryzae β-galactosidase

The objective of this work was to compare the properties of free and immobilized β-galactosidase (Aspergillus oryzae), entrapped in alginate–gelatin beads and cross-linked with glutaraldehyde. The free and immobilized forms of the enzyme showed no decrease in enzyme activity when incubated in buffer solutions in pH ranges of 4.5–7.0. The kinetics of lactose hydrolysis by the free and immobilized enzymes were studied at maximum substrate concentrations of 90 g/L and 140 g/L, respectively, a temperature of 35 °C and a pH of 4.5. The Michaelis–Menten model with competitive inhibition by galactose fit the experimental results for both forms. The K_m and V_m values of the free enzyme were 52.13 ± 2.8 mM and 2.56 ± 0.3 g_glucose/L min mg_enzyme, respectively, and were 60.30 ± 3.3 mM and 1032.07 ± 51.6 g_lactose/min m³_catalyst, respectively, for the immobilized form. The maximum enzymatic activity of the soluble form of β-galactosidase was obtained at pH 4.5 and 55 °C. Alternatively, the immobilized form was most active at pH 5.0 at 60 °C. The free and immobilized enzymes presented activation energies of 6.90 ± 0.5 kcal/mol and 7.7 ± 0.7 kcal/mol, respectively, which suggested that the immobilized enzyme possessed a lower resistance to substrate transfer.     

Immobilization of the marine microalga Phaeodactylum tricornutum in alginate for in situ experiments: Bead stability and suitability

Microalgae immobilization in alginate matrixes has been recently used to perform in situ experiments. However, the susceptibility of alginate matrixes to cation chelating agents and to antigelling cations, which can cause bead disruption or dissolution, is a major limitation for in situ exposures in estuarine and marine systems. The ultimate goal of this study was to produce alginate beads stable in seawater and suited for Phaeodactylum tricornutum growth. For this, different concentrations of alginate isolated from Macrocystis pyrifera (1.5, 1.9 and 2.3% [w/v]) and Laminaria hyperborea (4.0, 4.9 and 5.8% [w/v]), two concentrations of the hardening cations calcium and strontium (2.0 and 4.0% [w/v]), and the use of the polycation chitosan were investigated. Only beads found to be more stable after 16 days of exposure in seawater were inoculated with the microalga. P. tricornutum immobilized in beads prepared from 5.8% L. hyperborea alginate and in all beads in which a chitosan hardening treatment was applied showed a weak microalgal growth. Beads prepared using 4.9% of L. hyperborea alginate and a 4% (w/v) strontium solution were found to be the most stable and the most suitable for microalgal growth, and were exposed in the field, under natural fluctuating conditions of light and temperature. In situ growth rates of immobilized P. tricornutum cells demonstrated the potential of these beads for future use in in situ experiments in estuarine and marine systems.     

Lipase in biphasic alginate beads as a biocatalyst for esterification of butyric acid and butanol in aqueous media

Esterification of organic acids and alcohols in aqueous media is very inefficient due to thermodynamic constraints. However, fermentation processes used to produce organic acids and alcohols are often conducted in aqueous media. To produce esters in aqueous media, biphasic alginate beads with immobilized lipase are developed for in situ esterification of butanol and butyric acid. The biphasic beads contain a solid matrix of calcium alginate and hexadecane together with 5 mg/mL of lipase as the biocatalyst. Hexadecane in the biphasic beads serves as an organic phase to facilitate the esterification reaction. Under optimized conditions, the beads are able to catalyze the production of 0.16 mmol of butyl butyrate from 0.5 mmol of butyric acid and 1.5 mmol of butanol. In contrast, when monophasic beads (without hexadecane) are used, only trace amount of butyl butyrate is produced. One main application of biphasic beads is in simultaneous fermentation and esterification (SFE) because the organic phase inside the beads is very stable and does not leach out into the culture medium. SFE is successfully conducted with an esterification yield of 6.32% using biphasic beads containing iso-octane even though the solvent is proven toxic to the butanol-producing Clostridium spp.