Selective and stable production of physiologically active chitosan oligosaccharides using an enzymatic membrane bioreactor

We investigated the production of chitosan oligosaccharides by continuous hydrolysis of chitosan in an enzyme membrane bioreactor, with the goal of improving the yield of physiologically active oligosaccharides (pentamers and hexamers) and achieving operational stability. The bioreactor was a continuous-flow stirred-tank reactor equipped with an ultrafiltration membrane with a molecular weight cut-off of 2000 Da, and the hydrolysis was accomplished with chitosanase from Bacillus pumilus. After optimization of the reaction parameters, such as the amount of enzyme, the yield of the target oligosaccharides produced in the membrane bioreactor with free chitosanase reached 52% on the basis of the fed concentration of chitosan. An immobilized chitosanase prepared by the multipoint attachment method was used to improve the operational stability of the membrane bioreactor. Under the optimized conditions, pentameric and hexameric chitosan oligosaccharides were steadily produced at 2.3 g/L (46% yield) for a month. The half-life of the productivity of the reactor was estimated to be 50 d under the conditions examined.     

Production of chitosan oligosaccharides by chitosanase directly immobilized on an agar gel-coated multidisk impeller

An immobilized enzyme bioreactor consisting of an agar gel-coated multidisk impeller was developed for the hydrolysis of highly viscous chitosan solutions, and the operating conditions for the production of physiologically active chitosan oligosaccharides (pentamers and hexamers) were investigated. Chitosanase was directly immobilized on the agar gel-coated multidisk impeller by a multipoint attachment method. The high stability of the immobilized enzyme was confirmed by means of five repetitions of a batch hydrolysis reaction. When the enzyme activity at the support surface was relatively high, the yield of the target products was higher at an impeller speed of 2 s⁻¹ than at a speed of 1 s⁻¹. However, no significant increase in yield was observed at impeller speeds higher than 2 s⁻¹ in reactions at either of the two substrate concentrations tested (5 and 20 kg/m³). When the surface enzyme activity was low, the impeller speed did not affect the yield of the target products. The maximum yield of pentamers and hexamers increased as the surface enzyme activity decreased, and high yields (>30%) were obtained at activities below 160 U/m². From the viewpoint of productivity, the optimal surface-enzyme activity was about 340 U/m², and at that activity, the yield of target products was 22%. This yield was higher than that reported for conventional acid hydrolysis. To maximize both the productivity and the yield of the target products, the surface area for the immobilized enzyme should be increased. Our results suggest that it may be possible to obtain high yields of pentamers and hexamers of chitosan oligosaccharides from highly viscous chitosan solutions with this reactor.     

Factors affecting the composition of oligosaccharides produced in chitosan hydrolysis using immobilized chitosanases

The hydrolysis reaction of chitosan using immobilized chitosanases with regard to the composition of its products and the yield of the intermediate target products, pentamer and hexamer of chitosan oligosaccharides, was investigated. Chitosanase was immobilized onto agar or agarose gel particles by the multipoint attachment method. In batch experiments, surface enzyme density, support particle size, temperature, agitator speed, and initial substrate concentration significantly affected the composition of the oligosaccharides produced. It was believed that these factors all related to the reaction rate and mass transfer rate at the surface of the support materials immobilizing the enzymes. These effects were summarized as a correlation with Damk?hler number (Da), defined as the ratio of the maximum reaction rate to the maximum mass transfer rate. The result showed that the reaction conditions that give a low value of Da provide a high yield of pentamer and hexamer oligosaccharides.     

Chitooligosaccharides enzymatic production by Metarhizium anisopliae

The products of chitosan hydrolysis are chitooligosaccharides and are used mainly for medical applications due to their specific biological activities. The objective of this study was to detect and identify the products of enzymatic hydrolysis of chitosan (dimers to hexamers) using a crude extract of chitosanolytic enzymes produced by the fungus Metarhizium anisopliae. These fungus was able to produce, during 48 h cultivation in a medium containing chitosan, chitooligosaccharides ranging from dimers, trimers, tetramers and pentamers at concentrations 0.2, 0.19, 0.06, 0.04 mg/mL, respectively, and the enzymatic activity was 2.5 U/L. Using the crude enzyme extract for chitosan hydrolysis, we detected the presence of dimers to hexamers at hydrolysis times of 10, 20, 30, 40, 50 and 60 min of enzymatic reaction, but the yields were higher at 10 min (54%). The hexamers was obtained only with 30 min of reaction with concentration of 0.004 mg/mL.     

Optimum conditions for the precipitation of chitosan oligomers with DP 5–7 in concentrated hydrochloric acid at low temperature

Chitosan was partially hydrolysed with 35% hydrochloric acid for 2 h at 80°C and the hydrolysate stored at −20°C after dilution with water to precipitate higher molecular weight (MW) chitosan oligomers. When the hydrolysate was not diluted with water, no precipitate was formed but 7.3% chitosan oligomers were precipitated at a dilution ratio of 1.0 (ml water/ml hydrolysate). The time for precipitation was not significantly changed after storing the hydrolysate at −20°C for 1 day. In addition, the precipitation yield was not significantly influenced by the concentration of HCl used for the hydrolysis except at less than 5.0 (ml HCl/g chitosan). However, the yield of precipitated oligomers changed with partial hydrolysis time. For 0.5 and 2 h hydrolysis, 10.1 and 7.3% of the oligomers were precipitated, respectively, but only 3.1% of the oligomers were obtained after a 4 h reaction. When methanol was added to the hydrolysate, the precipitation yield increased up to 70% but the amounts of lower MW chitosan oligomers in the precipitated oligomers also increased with the increase of higher MW. The precipitated oligomers were mainly composed of pentamers and hexamers.     

Control of virus assembly: HK97 "Whiffleball" mutant capsids without pentons

The capsid of Escherichia coli bacteriophage HK97 assembles as a 420 subunit icosahedral shell called Prohead I which undergoes a series of maturation steps, including proteolytic cleavage, conformational rearrangements, and covalent cross-linking among all the subunits to yield the highly stable mature Head II shell. Prohead I have been shown to assemble from pre-formed hexamers and pentamers of the capsid protein subunit. We report here the properties of a mutant of the capsid protein, E219K, which illuminate the assembly of Prohead I. The mutant capsid protein is capable of going through all of the biochemically and morphologically defined steps of capsid maturation, and when it is expressed by itself from a plasmid it assembles efficiently into a Prohead I that is morphologically indistinguishable from the wild-type Prohead I, with a full complement of both hexamers and pentamers. Unlike the wild-type Prohead I, when the mutant structure is dissociated into capsomers in vitro, only hexamers are found. When such preparations are put under assembly conditions, these mutant hexamers assemble into "Whiffleballs", particles that are identical with Prohead I except that they are missing the 12 pentamers. These Whiffleballs can even be converted to Prohead I by specifically binding wild-type pentamers. We argue that the ability of the mutant hexamers to assemble in the absence of pentamers implies that they retain a memory of their earlier assembled state, most likely as a conformational difference relative to assembly-naive hexamers. The data therefore favor a model in which Prohead I assembly is regulated by conformational switching of the hexamer.     

固定化嗜热脂肪芽孢杆菌合成低聚半乳糖

利用海藻酸钙、明胶和壳聚糖为固定化载体包埋嗜热脂肪芽孢杆菌细胞合成低聚半乳糖 (GOS)。通过比较三种方法的酶活力回收、最适反应条件、GOS的得率和和载体机械强度 ,选择明胶作为固定化细胞的载体。反应体系的温度、pH、乳糖浓度、乳糖的转化率和载体的传质阻力对GOS合成有明显影响。在CSTR反应器中水解 60 %乳糖 ,GOS最大得率为31 2 % ,经过 96h( 8批反应 ) ,产物得率为原来的 88%。在空速 0 0 9h- 1条件下 ,利用填充床反应器连续水解乳糖 ,GOS的得率和反应器生产能力分别为 31 5%和 1 7 4g (L·h) ,连续反应1 40h,GOS得率下降 2 0 %。产物经过活性炭柱层柱分离纯化 ,通过13C NMR鉴定四糖的化学结构为 β D Gal ( 1→ 3) D Gal ( 1→ 6) D G ( 1→ 4) D Glu。     

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable beta-glycosidases and optimization of a packed-bed reactor for lactose conversion.

Recombinant hyperthermostable beta-glycosidases from the archaea Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) were covalently attached onto the insoluble carriers chitosan, controlled pore glass (CPG), and Eupergit C. For each enzyme/carrier pair, the protein-binding capacity, the immobilization yield, the pH profiles for activity and stability, the activity/temperature profile, and the kinetic constants for lactose hydrolysis at 70 degrees C were determined. Eupergit C was best among the carriers in regard to retention of native-like activity and stability of Ss beta Gly and CelB over the pH range 3.0-7.5. Its protein binding capacity of approximately 0.003 (on a mass basis) was one-third times that of CPG, while immobilization yields were typically 80% in each case. Activation energies for lactose conversion by the immobilized enzymes at pH 5.5 were in the range 50-60 kJ/mol. This is compared to values of approximately 75 kJ/mol for the free enzymes. Immobilization expands the useful pH range for CelB and Ss beta Gly by approximately 1.5 pH units toward pH 3.5 and pH 4.5, respectively. A packed-bed enzyme reactor was developed for the continuous conversion of lactose in different media, including whey and milk, and operated over extended reaction times of up to 14 days. The productivities of the Eupergit C-immobilized enzyme reactor were determined at dilution rates between 1 and 12 h(-1), and using 45 and 170 g/L initial lactose. Results of kinetic modeling for the same reactor, assuming plug flow and steady state, suggest the presence of mass-transfer limitation of the reaction rate under the conditions used. Formation of galacto-oligosaccharides in the continuous packed-bed reactor and in the batch reactor using free enzyme was closely similar in regard to yield and individual saccharide components produced.     

Formation of Oligosaccharides during Enzymic Hydrolysis of Milk Whey Permeates

Lactose present in whey UF-permeates was hydrolysed by an immobilised enzyme reactor and the formation of monosaccharides (glucose + galactose) and oligosaccharides was monitored. The enzyme used was β-galactosidase from A. oryzaeimmobilised in a porous film. The reactor, run in the flow-through mode, allowed large conversions at short residence times (60% conversion in 1 min). The conversion to oligosaccharides as a function of the reaction time (or degree of conversion) reaches a maximum and then declined as oligosaccharides were converted back to mono- and disaccharides. The higher the initial lactose concentration the higher the conversion to oligosaccharides and these maxima appear at higher degrees of conversion. Some trials were carried out on the concentration of the oligosaccharides present in the hydrolysates by means of membrane filtration (nanofiltration) .     

Purification and characterization of chitosanase from Bacillus sp. strain KCTC 0377BP and its application for the production of chitosan oligosaccharides

For the enzymatic production of chitosan oligosaccharides from chitosan, a chitosanase-producing bacterium, Bacillus sp. strain KCTC 0377BP, was isolated from soil. The bacterium constitutively produced chitosanase in a culture medium without chitosan as an inducer. The production of chitosanase was increased from 1.2 U/ml in a minimal chitosan medium to 100 U/ml by optimizing the culture conditions. The chitosanase was purified from a culture supernatant by using CM-Toyopearl column chromatography and a Superose 12HR column for fast-performance liquid chromatography and was characterized according to its enzyme properties. The molecular mass of the enzyme was estimated to be 45 kDa by means of sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The enzyme demonstrated bifunctional chitosanase-glucanase activities, although it showed very low glucanase activity, with less than 3% of the chitosanase activity. Activity of the enzyme increased with an increase of the degrees of deacetylation (DDA) of the chitosan substrate. However, the enzyme still retained 72% of its relative activity toward the 39% DDA of chitosan, compared with the activity of the 94% DDA of chitosan. The enzyme produced chitosan oligosaccharides from chitosan, ranging mainly from chitotriose to chitooctaose. By controlling the reaction time and by monitoring the reaction products with gel filtration high-performance liquid chromatography, chitosan oligosaccharides with a desired oligosaccharide content and composition were obtained. In addition, the enzyme was efficiently used for the production of low-molecular-weight chitosan and highly acetylated chitosan oligosaccharides. A gene (csn45) encoding chitosanase was cloned, sequenced, and compared with other functionally related genes. The deduced amino acid sequence of csn45 was dissimilar to those of the classical chitosanase belonging to glycoside hydrolase family 46 but was similar to glucanases classified with glycoside hydrolase family 8.     

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.     

Overexpression and characterization of a novel chitinase gene from a marine bacterium Pseudomonas sp. BK1

The chitinase A (ChiA)-coding gene of Pseudomonas sp. BK1, which was isolated from a marine red alga Porphyra dentata, was cloned and expressed in Escherichia coli. The structural gene consists of 1602 bp encoding a protein of 534 amino acids, with a predicted molecular weight of 55,370 Da. The deduced amino acid sequence of ChiA showed low identity (less than 32%) with other bacterial chitinases. The ChiA was composed of multiple domains, unlike the arrangement of domains in other bacterial chitinases. Recombinant ChiA overproduced as inclusion bodies was solubilized in the presence of 8 M urea, purified in a urea-denatured form and re-folded by removing urea. The purified enzyme showed maximum activity at pH 5.0 and 40 degrees C. It exhibited high activity towards glycol chitosan and glycol chitin, and lower activity towards colloidal chitin. The enzyme hydrolyzed the oligosaccharides from (GlcNAc)4 to (GlcNAc)6, but not GlcNAc to (GlcNAc)3. The results suggest that the ChiA is a novel enzyme, with different domain structure and action mode from bacterial family 18 chitinases.     

螺旋藻批式与连续培养及其生长动力学

在内循环气升式光生物反应器中,分别研究了螺旋藻细胞在批式和连续培养条件下的生长特性,结果表明：Richards模型和指数衰减模型可较好地描述批式培养时细胞和碳源底物浓度与培养时间的关系;批式培养时最大细胞生长速率为0371g/d/L,细胞对碳的得率系数为3.439g/gC;连续培养时随着稀释率的增大,细胞和底物浓度分别呈下降和上升趋势;连续培养时最大细胞产率为0.362g/L/d,最佳稀释率为0.45/d,细胞对碳的得率系数为2.050g/gC;所提出的连续培养动力学模型可较好地拟合实验数据。     

High yield production of monomer-free chitosan oligosaccharides by pepsin catalyzed hydrolysis of a high deacetylation degree chitosan

The high molecular weight of chitosan, which results in a poor solubility at neutral pH values and high viscosity aqueous solutions, limits its potential uses in the fields of food, health and agriculture. However, most of these limitations are overcome by chitosan oligosaccharides obtained by enzymatic hydrolysis of the polymer. Several commercial enzymes with different original specificities were assayed for their ability to hydrolyze a 93% deacetylation degree chitosan and compared with a chitosanase. According to the patterns of viscosity decrease and reducing end formation, three enzymes--cellulase, pepsin and lipase A--were found to be particularly suitable for hydrolyzing chitosan at a level comparable to that achieved by chitosanase. Unlike the appreciable levels of both 2-amino-2-deoxy-D-glucose and 2-acetamido-2-deoxy-D-glucose monomers released from chitosan by the other enzymes after a 20h-hydrolysis (4.6-9.1% of the total product weight), no monomer could be detected following pepsin cleavage. As a result, pepsin produced a higher yield of chitosan oligosaccharides than the other enzymes: 52% versus as much as 46%, respectively. Low molecular weight chitosans accounted for the remaining 48% of hydrolysis products. The calculated average polymerization degree of the products released by pepsin was around 16 units after 20h of hydrolysis. This product pattern and yield are proposed to be related to the bond cleavage specificity of pepsin and the high deacetylation degree of chitosan used as substrate. The optimal reaction conditions for hydrolysis of chitosan by pepsin were 40 degrees C and pH 4.5, and an enzyme/substrate ratio of 1:100 (w/w) for reactions longer than 1h.     

Cloning,expression, and characterization of a glycoside hydrolase family 86 β-agarase from a deep-sea <Emphasis Type="Italic">Microbulbifer</Emphasis>-like isolate

The gene for a novel -agarase from a deep-sea Microbulbifer-like isolate was cloned and sequenced. It encoded a mature protein of 126,921 Da (1,146 amino acids), which was a modular protein including two tandem carbohydrate-binding module (CBM)-like sequences and a catalytic module. The catalytic module resembled a glycoside hydrolase family 86 -agarase, AgrA, from Pseudoalteromonas atlantica T6c with 31% amino acid identity. Its recombinant agarase was hyper-produced extracellularly using Bacillus subtilis as the host and purified to homogeneity. The activity and stability were strongly enhanced by CaCl₂. The maximal enzyme activity was observed at 45°C and pH 7.5 in the presence of 10 mM CaCl₂. The enzyme was an endo-type -agarase and degraded agarose and agarose oligosaccharides more polymerized than hexamers to yield neoagarohexaose as the main product. This is the first glycoside hydrolase family 86 enzyme to be homogeneously purified and characterized.     

Degradation of raffinose oligosaccharides in soymilk by immobilized alpha-galactosidase of Aspergillus oryzae

Alpha-galactosidase was immobilized in a mixture of k-carrageenan and locust bean gum. The properties of the free and immobilized enzyme were then determined. The optimum pH for both the soluble and immobilized enzyme was 4.8. The optimum temperature for the soluble enzymes was 50 degrees C, whereas that for the immobilized enzyme was 55 degrees C. The immobilized enzyme was used in batch, repeated batch, and continuous modes to degrade the raffinose-family sugars present in soymilk. Two hours of incubation with the free and immobilized alpha-galactosidases resulted in an 80% and 68% reduction in the raffinose oligosaccharides in the soymilk, respectively. In the repeated batch, a 73% reduction was obtained in the fourth cycle. A fluidized bed reactor was also designed to treat soymilk continuously and the performance of the immobilized alpha-galactosidase tested at different flow rates, resulting in a 90% reduction of raffinose-family oligosaccharides in the soymilk at a flow rate 40 ml/h. Therefore, the present study demonstrated that immobilized alpha-galactosidase in a continuous mode is efficient for reducing the oligosaccharides present in soymilk, which may be of considerable interest for industrial application.     

Molecular cloning of the gene encoding a novel beta-N-acetylhexosaminidase from a marine bacterium, Alteromonas sp. strain O-7, and characterization of the cloned enzyme

We have reported that the chitinolytic system of Alteromonas sp. strain O-7 consists of chitinases (ChiA, ChiB, and ChiC), a chitinase-like enzyme (ChiD), beta-N-acetylglucosaminidases (GlcNAcasesA, GlcNAcaseB, and GlcNAcaseC), and a novel transglycosylative enzyme (Hex99). The gene encoding a beta-hexosaminidase with an unusual substrate specificity (hex86), located upstream of the hex99 gene, was cloned and sequenced. The gene encoded a protein of 761 amino acids with a calculated molecular mass of 86,758 Da. The deduced amino acid sequence of Hex86 showed sequence similarity with beta-hexosaminidases belonging to family 20. The hex86 gene was expressed in Escherichia coli, and the recombinant enzyme was purified to homogeneity. The enzyme rapidly cleaved p-nitrophenyl-beta-N-acetyl-D-glucosaminide and slowly cleaved p-nitrophenyl-beta-N-acetyl-D-galactosaminide. Unexpectedly, the enzyme did not hydrolyzed chitin oligosaccharides under the assay conditions for synthetic glycosides. However, after prolonged incubation with excessive quantities of the enzyme, Hex86 hydrolyzed chitin oligosaccharides. These results indicate that Hex86 is a novel enzyme that prefers p-nitrophenyl-beta-N-acetyl-D-glucosaminide to chitin oligosaccharides as a substrate.     

Immobilization of beta-galactosidase on fibrous matrix by polyethyleneimine for production of galacto-oligosaccharides from lactose

The production of galacto-oligosaccharides (GOS) from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth was studied. A novel method of enzyme immobilization involving PEI-enzyme aggregate formation and growth of aggregates on individual fibrils of cotton cloth leading to multilayer immobilization of the enzyme was developed. A large amount of enzyme was immobilized (250 mg/g support) with about 90-95% efficiency. A maximum GOS production of 25-26% (w/w) was achieved at near 50% lactose conversion from 400 g/L of lactose at pH 4.5 and 40 degrees C. Tri- and tetrasaccharides were the major types of GOS formed, accounting for about 70% and 25% of the total GOS produced in the reactions, respectively. Temperature and pH affected not only the reaction rate but also GOS yield to some extend. A reaction pH of 6.0 increased GOS yield by as much as 10% compared with that of pH 4.5 while decreased the reaction rate of immobilized enzyme. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme under the same reaction conditions, suggesting diffusion limitation was negligible in the packed bed reactor and the enzyme carrier. Increase in the thermal stability of PEI-immobilized enzyme was also observed. The half-life for the immobilized enzyme on cotton cloth was close to 1 year at 40 degrees C and 21 days at 50 degrees C. Stable, continuous operation in a plug-flow reactor was demonstrated for about 3 days without any apparent problem. A maximum GOS production of 26% (w/w) of total sugars was attained at 50% lactose conversion with a feed containing 400 g/L of lactose at pH 4.5 and 40 degrees C. The corresponding reactor productivity was 6 kg/L/h, which is several-hundred-fold higher than those previously reported.     

Enzymatic production of biodiesel from cotton seed oil using t-butanol as a solvent

The enzymatic production of biodiesel by methanolysis of cottonseed oil was studied using immobilized Candida antarctica lipase as catalyst in t-butanol solvent. Methyl ester production and triacylglycerol disappearance were followed by HPLC chromatography. It was found, using a batch system, that enzyme inhibition caused by undissolved methanol was eliminated by adding t-butanol to the reaction medium, which also gave a noticeable increase of reaction rate and ester yield. The effect of t-butanol, methanol concentration and temperature on this system was determined. A methanolysis yield of 97% was observed after 24h at 50 degrees C with a reaction mixture containing 32.5% t-butanol, 13.5% methanol, 54% oil and 0.017 g enzyme (g oil)(-1). With the same mixture, a 95% ester yield was obtained using a one step fixed bed continuous reactor with a flow rate of 9.6 mlh(-1) (g enzyme)(-1). Experiments with the continuous reactor over 500 h did not show any appreciable decrease in ester yields.     

Activity and operational stability of immobilized mandelonitrile lyase in methanol/water mixtures

Summary The enzyme mandelonitrile lyase was covalently immobilized on solid support materials using different methods. Immobilization on porous silica using coupling with glutaraldehyde afforded preparations with high enzyme loading (up to 9% (w/w)). The immobilized enzyme was used in a packed bed reactor for the continuous production of d-mandelonitrile from benzaldehyde and cyanide. The influence of the flow rate, pH, substrate concentrations and enzyme loading on the reaction yield and the enantiomeric purity of the product was investigated. In order to suppress the competing spontaneous reaction, the enzymatic reaction must be rapid. A flow rate of 9.5 ml/min (0.1 M benzaldehyde and 0.3 M HCN) through a 3 ml reactor afforded a 86% yield of mandelonitrile with 92% enantiomeric excess. No leakage of enzyme occurred under continuous operation. One column was used continuously for 200 h without any decrease in yield or enantiomeric purity of the product. High concentrations of benzoic acid were shown to decrease the operational stability of the system.