A群脑膜炎球菌荚膜多糖纯化工艺的优化

目的对A群脑膜炎球菌荚膜多糖纯化工艺的关键步骤进行分步研究,优化每一步工艺参数。方法优化十六烷基三甲基溴化铵的加入浓度、复合多糖的解离浓度和解离时间、不同厂家的苯酚、超滤和透析等工艺过程对荚膜多糖的影响。结果十六烷基三甲基溴化铵质量体积终浓度0.10%(w/v)沉淀效果更好,纯化获得的荚膜多糖产量更高相对分子质量更大。复合多糖解离浓度越高,纯化获得的荚膜多糖相对分子质量越小。延长复合多糖解离时间有利于提高荚膜多糖产量。不同厂家的苯酚、超滤和透析等工艺对荚膜多糖的产量和分子大小没有影响。结论现行A群脑膜炎球菌荚膜多糖纯化工艺复杂,优化后的工艺提高了荚膜多糖产量,缩短了工艺用时,增加了工艺稳定性。     

14型肺炎链球菌荚膜多糖纯化工艺中两种去除蛋白方法的比较

目的苯酚抽提法和脱氧胆酸钠沉淀法去除14型肺炎链球菌荚膜多糖中蛋白质的效果比较。方法将3批次14型肺炎链球菌发酵培养液经超滤、乙醇沉淀等方法初步纯化后,平分成两份,分别采用苯酚抽提法和脱氧胆酸钠沉淀法去除蛋白,通过比较多糖收获量、多糖组分检定结果、多糖分子质量、多糖抗原活性、多糖核磁共振图谱,以此评价这两种蛋白去除方法的效果。结果与苯酚抽提法相比,脱氧胆酸钠沉淀法制备的14型肺炎链球菌纯化荚膜多糖除收获量较高,蛋白和核酸杂质含量较低外,氨基己糖含量、多糖分子质量、抗原活性和多糖核磁共振图谱的检定分析结果无显著性差异(P>0.1)。结论作为14型肺炎链球菌荚膜多糖纯化工艺中的除蛋白方法,脱氧胆酸钠沉淀法优于苯酚抽提法。     

Purification of a conjugated polysaccharide vaccine using tangential flow diafiltration

Conjugated vaccines prepared from the capsular polysaccharide of Streptococcus pneumoniae can provide immunization against invasive pneumococcal disease, meningitis, and otitis media. One of the critical steps in the production of these vaccines is the removal of free (unreacted) polysaccharides from the protein-polysaccharide conjugate. Experimental studies were performed to evaluate the effects of membrane pore size, filtrate flux, and solution conditions on the transmission of both the conjugate and free polysaccharide through different ultrafiltration membranes. Conjugate purification was done using diafiltration performed in a linearly-scalable tangential flow filtration cassette. More than 98% of the free polysaccharide was removed within a 5-diavolume diafiltration process, which is a significant improvement over previously reported results for purification of similar conjugated vaccines. These results clearly demonstrate the opportunities for using ultrafiltration/diafiltration for the final purification of conjugated vaccine products.     

An overview of purification methods of glycoside hydrolase family 70 dextransucrase

The enzyme dextransucrase (sucrose:1, 6-α-D-glucan 6-α-glucosyltransferase, EC 2.4.1.5) catalyses the synthesis of exopolysaccharide, dextran from sucrose. This class of polysaccharide has been extensively exploited in pharmaceutical industry as blood volume expander, as stabiliser in food industry and as a chromatographic medium in fine chemical industry because of their nonionic nature and stability. Majority of the dextrans are synthesized from sucrose by dextransucrase secreted mainly by bacteria belonging to genera Leuconostoc, Streptococcus and Lactobacillus. Bulk of the information on purification of extracellular dextransucrase has been generated from Leuconostoc species. Various methods such as precipitation by ammonium sulphate, ethanol or polyethylene glycol, phase partitioning, ultrafiltration and chromatography have been used to purify the enzyme. Purification of dextransucrase is rendered difficult by the presence of viscous dextran in the medium. However, processes like ultra-filtration, salt and PEG precipitation, chromatography and phase partitioning have been standardized and successfully used for higher scale purification of the enzyme. A recombinant dextransucrase from Leuconostoc mesenteroides B-512F with a histidine tag has been expressed in E. coli cells and purifi ed by immobilized metal ion chromatography. This review reports the available information on purifi cation methods of dextransucrase from Leuconostoc mesenteroides strains.     

Isolation and antioxidant property of the extracellular polysaccharide from <Emphasis Type="Italic">Rhodella reticulata</Emphasis>

The extracellular polysaccharide from Rhodella reticulata was separated from the culture medium followed by concentration and ethanol precipitation, and purified by anion exchange chromatography on DEAE-Sepharose Fast Flow. This study compared the free radical-scavenging property and antioxidant activity with various treatments of crude extracellular polysaccharides of R. reticulata. The results showed that both the crude extracellular polysaccharide and deproteinized crude extracellular polysaccharide gave evidence of the free radical scavenging and antioxidant activity in a dose-dependent manner. The crude extracellular polysaccharide exhibited higher free radical scavenging capacity and better antioxidant activity than the various treatments of crude extracellular polysaccharide samples. The superoxide anion radical scavenging ability of various samples was significantly higher compared to standard antioxidant (α-tocopherol). These results indicate that the extracellular polysaccharide of R. reticulata is a potent natural antioxidant.     

Application of a 22L scale membrane bioreactor and cross-flow ultrafiltration to obtain purified chondroitin

Recently, the possibility of producing fructosylated chondroitin from the capsular polysaccharide of Escherichia coli O5:K4:H4, in fed‐batch and microfiltration experiments was assessed on a 2 L bioreactor. In this work, a first scale‐up step was set on a 22 L membrane reactor with modified baffles to insert ad hoc designed microfiltration modules permanently inside the bioreactor vessel. Moreover, the downstream polysaccharide purification process, recently established on the A¨?KTA cross‐flow instrument, was translated to a UNIFLUX‐10, a tangential flow filtration system suitable for prepilot scale. In particular, the microfiltered permeates obtained throughout the fermentation, and the supernatant recovered from the centrifuged broth at the end of the process, were treated as two separate samples in the following ultrafiltration procedure, and the differences in the two streams and how these affected the ultrafiltration/diafiltration process performance were analysed. The total amount of K4 capsular polysaccharide was about 85% in the broth and 15% in the microfiltered permeates. However, the downstream treatment was more efficient when applied to the latter. The major contaminant, the lipopolysaccharide, could easily be separated by a mild hydrolysis that also results in the elimination of the unwanted fructosyl residue, which is linked to the C‐3 of glucuronic acid residues. The tangential ultrafiltration/diafiltration protocols developed in a previous work were effectively scaled‐up, and therefore in this research proof of principle was established for the biotechnological production of chondroitin from the wild‐type strain E. coli O5:K4:H4. The complete downstream procedure yielded about 80% chondroitin with 90% purity. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 28: 1012–1018, 2012     

C群脑膜炎球菌多糖纯化方法的改进

将C群脑膜炎球菌粗多糖的纯化改进为用1:1容量冷酚提取的生产工艺。结果表明,改进后的方法去除蛋白质效果同样能够达到《中国药典》2005版(三部)的要求,总体结果优于改进前。同时能扩大处理量而降低了生产成本,适合规模化生产。     

Polysaccharides from mycelium of the fungus <Emphasis Type="Italic">Cunninghamella japonica</Emphasis>

Preliminary data on the polysaccharide composition of mycelium of the fungus Cunninghamella japonica (synonymous with C. echinulata) grown by the method of submerged cultivation were obtained. Mild acidic hydrolysis of mycelium resulted in the formation of glucose, mannose, and galactose; while the treatment with acid under drastic conditions afforded glucosamine as a product of hydrolysis of chitin and chitosan, their total content was about 35%. Several polysaccharide fractions were isolated from mycelium by successive extraction with hot water, 2% aqueous NaOH, and 10% AcOH; their monosaccharide composition was characterized. The yield of chitosan extracted with AcOH was insignificant. Additional purification of the fraction obtained after extraction with alkali afforded polysaccharide which was a linear (1 → 3)-α-D-glucopyranan according to the data of NMR spectroscopy and the chemical methods of structural analysis. The presence of this polysaccharide, as well as a low content of chitosan and polyuronides, distinguishes the studied strain C. japonica from most of the known Mucorales.     

Quantitative determination of starch, amylose, and amylopectin in plant tissues using glass fiber paper

Methods for accurate and rapid determination of starch, amylose, and amylopectin in plant tissues are described. They are based on simplified extraction of starch with 32% perchloric acid and selective retention of the starch-iodine complex on a glass fiber disk (Whatman GF/A). The starch on the disk is dissolved in 0.75 M sulfuric acid and estimated with phenol. For amylose and amylopectin determination the starch on the disk is dissolved in perchloric acid, precipitated with ethanol, and retained on a 10-cm glass fiber strip. Both polysaccharides are separated by a chromatographic procedure involving development of the strip in a mixture of ethanol and dimethyl sulfoxide and in dimethyl sulfoxide. The strip is washed in ethanol and stained with iodine or used for polysaccharide quantitation. As little as 5 micrograms of starch or its components present in different amounts of plant material can be estimated.     

Expression,purification, and characterization of pro‐phenoloxidase‐activating serine protease from Spodoptera litura

One of the important trigger molecules for innate immunity is a serine protease that activates zymogen phenol oxidase (PPO). Central to wound healing response is the activation of phenol oxidase zymogen. Molecular characterization of phenol oxidase has been recently reported by us. Here, we report isolation, cloning, expression, and purification of prophenol oxidase activating enzyme 1 (slppae1) from polyphagous pest, Spodoptera litura. SLPPAE1 is induced within 6 h of physical injury. The structural features of the mature polypeptide are reminiscent of other lepidopteran PPAE in having a signal peptide, propeptide, and catalytically active polypeptide. The cDNA has been expressed in Sf21 cells using baculovirus expression vector. Fractionation of expressing Sf21 cells revealed its expression in the membranes. The recombinant protein was solubilized from membranes and purified by Ni‐NTA affinity chromatography. The purified enzyme is catalytically active on chromogenic substrate, activates recombinantly expressed prophenol oxidase (PPO) of S. litura, and is sensitive to inhibition by aprotenin. N‐terminal sequencing of processed phenol oxidase revealed 11 kDa propeptide instead of in‐silico predicted 6 kDa polypeptide. © 2009 Wiley Periodicals, Inc.     

Optimization of extraction process by response surface methodology and preliminary structural analysis of polysaccharides from defatted peanut (Arachis hypogaea) cakes

In this work, response surface methodology was used to determine optimum conditions for extraction of polysaccharides from defatted peanut cake. A central composite design including independent variables, such as extraction temperature (x₁), extraction time (x₂), and ethanol concentration (x₃) was used. Selected response which evaluates the extraction process was polysaccharide yield, and the second-order model obtained for polysaccharide yield revealed coefficient of determination of 97.81%. The independent variable with the largest effect on response was ethanol concentration (x₃). The optimum extraction conditions were found to be extraction temperature 48.7 °C, extraction time 1.52 h, and ethanol concentration of 61.9% (v/v), respectively. Under these conditions, the extraction efficiency of polysaccharide can increase to 25.89%. The results of structural analysis showed that the main composition of defatted peanut cake polysaccharide was α-galactose.     

Effect of electrostatic interactions on the ultrafiltration behavior of charged bacterial capsular polysaccharides

Charged polysaccharides are used in the food industry, as cosmetics, and as vaccines. The viscosity, thermodynamics, and hydrodynamic properties of these charged polysaccharides are known to be strongly dependent on the solution ionic strength because of both inter‐ and intramolecular electrostatic interactions. The goal of this work was to quantitatively describe the effect of these electrostatic interactions on the ultrafiltration behavior of several charged capsular polysaccharides obtained from Streptococcus pneumoniae and used in the production of Pneumococcus vaccines. Ultrafiltration data were obtained using various Biomax? polyethersulfone membranes with different nominal molecular weight cutoffs. Polysaccharide transmission decreased with decreasing ionic strength primarily because of the expansion of the charged polysaccharide associated with intramolecular electrostatic repulsion. Data were in good agreement with a simple theoretical model based on solute partitioning in porous membranes, with the effective size of the different polysaccharide serotypes evaluated using size exclusion chromatography at the same ionic conditions. These results provide fundamental insights and practical guidelines for exploiting the effects of electrostatic interactions during the ultrafiltration of charged polysaccharides. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1531–1538, 2016     

Reconstitution of emulsifying activity of Acinetobacter calcoaceticus BD4 emulsan by using pure polysaccharide and protein

Acinetobacter calcoaceticus BD4 and BD413 produce extracellular emulsifying agents when grown on 2% ethanol medium. For emulsifying activity, both polysaccharide and protein fractions were required, as demonstrated by selective digestion of the polysaccharide with a specific bacteriophage-borne polysaccharide depolymerase, deproteinization of the extracellular emulsifying complex with hot phenol, and reconstitution of emulsifier activity with pure polysaccharide and a polysaccharide-free protein fraction. Chemical modification of the carboxyl groups in the polysaccharide resulted in a loss of activity. The protein required for reconstitution of emulsifying activity was purified sevenfold. The BD4 emulsan apparently derives its amphipathic properties from the association of an anionic hydrophilic polysaccharide with proteins.     

Reconstitution of emulsifying activity of Acinetobacter calcoaceticus BD4 emulsan by using pure polysaccharide and protein.

Acinetobacter calcoaceticus BD4 and BD413 produce extracellular emulsifying agents when grown on 2% ethanol medium. For emulsifying activity, both polysaccharide and protein fractions were required, as demonstrated by selective digestion of the polysaccharide with a specific bacteriophage-borne polysaccharide depolymerase, deproteinization of the extracellular emulsifying complex with hot phenol, and reconstitution of emulsifier activity with pure polysaccharide and a polysaccharide-free protein fraction. Chemical modification of the carboxyl groups in the polysaccharide resulted in a loss of activity. The protein required for reconstitution of emulsifying activity was purified sevenfold. The BD4 emulsan apparently derives its amphipathic properties from the association of an anionic hydrophilic polysaccharide with proteins.     

Inhibition of ethanol-producing yeast and bacteria by degradation products produced during pre-treatment of biomass

An overview of the different inhibitors formed by pre-treatment of lignocellulosic materials and their inhibition of ethanol production in yeast and bacteria is given. Different high temperature physical pre-treatment methods are available to render the carbohydrates in lignocellulose accessible for ethanol fermentation. The resulting hydrolyzsates contain substances inhibitory to fermentation—depending on both the raw material (biomass) and the pre-treatment applied. An overview of the inhibitory effect on ethanol production by yeast and bacteria is presented. Apart from furans formed by sugar degradation, phenol monomers from lignin degradation are important co-factors in hydrolysate inhibition, and inhibitory effects of these aromatic compounds on different ethanol producing microorganisms is reviewed. The furans and phenols generally inhibited growth and ethanol production rate (Q_EtOH) but not the ethanol yields (Y_EtOH) in Saccharomyces cerevisiae. Within the same phenol functional group (aldehyde, ketone, and acid) the inhibition of volumetric ethanol productivity was found to depend on the amount of methoxyl substituents and hence hydrophobicity (log P). Many pentose-utilizing strains Escherichia coli, Pichia stipititis, and Zymomonas mobilis produce ethanol in concentrated hemicellulose liquors but detoxification by overliming is needed. Thermoanaerobacter mathranii A3M3 can grow on pentoses and produce ethanol in hydrolysate without any need for detoxification.     

伤寒Vi多糖疫苗大规模生产中的工艺改进

对伤寒Ｖｉ多糖疫苗大规模生产进行了三项工艺改进：１．将液体菌种由静止期接种大罐改为对数生长期接种大罐,大罐培养时间可缩短３－４小时。２．２％（Ｖ／Ｖ）甲醛溶液杀菌时间由５℃６小时改为２０－２５℃２小时,能保证杀菌完全。３．用冷酚精制Ｖｉ多糖由常规法改为乳化法,可减少精制次数及冷酚用量,提高多糖收率     

Antiviral Effects of Sulfated Exopolysaccharide from the Marine Microalga <Emphasis Type="Italic">Gyrodinium impudicum</Emphasis> Strain KG03

The sulfated exopolysaccharide p-KG03, which is produced by the marine microalga Gyrodinium impudicum strain KG03, exhibited impressive antiviral activity in vitro (EC₅₀ = 26.9 µg/ml) against the encephalomyocarditis virus (EMCV). Depending on the p-KG03 concentration, the development of cytopathic effects in EMCV-infected HeLa cells was either inhibited completely or slowed. Moreover, p-KG03 did not show any cytotoxic effects on HeLa cells, even at concentrations up to 1000 µg/ml. The polysaccharide was purified by repeated precipitation in ethanol, followed by gel filtration. The p-KG03 polysaccharide had a molecular weight of 1.87 × 10⁷, and was characterized as a homopolysaccharide of galactose with uronic acid (2.96% wt/wt) and sulfate groups (10.32% wt/wt). The biological activities of p-KG03 suggest that sulfated metabolites from marine organisms are a rich source of antiviral agents. This is the first reported marine source of antiviral sulfated polysaccharides against EMCV. The p-KG03 polysaccharide may be useful in the development of marine bioactive exopolysaccharide for biotechnological and pharmaceutical products.     

Intracellular polysaccharide of an anaerobic psychrophile <Emphasis Type="Italic">Clostridium algoriphilum</Emphasis>

Polysaccharide was revealed in the cytoplasm of spore-forming Clostridium algoriphilum 14D1 = VKM B-2271 = DSM 16153 grown on glucose at 5°C. This polymer was isolated, purified, and identified as a glycogen-like compound based on analysis of its hydrolysis products. The ratio of the polysaccharide to the dry biomass weight did not change in the course of culture growth. Limitation of C. algoriphilum 14D1 growth by nitrogen resulted in a doubling of the polysaccharide/dry biomass ratio. The transition of C. algoriphilum 14D1 cells from optimal conditions into carbon-free medium resulted in utilization of intracellular polysaccharide. The amount of polysaccharide was shown to depend on glucose concentration, type of the carbon substrate, and growth temperature. Future investigations of polysaccharide functions in C. algoriphilum 14D1 cells are discussed.     

Ethanol production from paper sludge by simultaneous saccharification and co‐fermentation using recombinant xylose‐fermenting microorganisms

Simultaneous saccharification and co‐fermentation (SSCF) of waste paper sludge to ethanol was investigated using two recombinant xylose‐fermenting microbes: Zymomonas mobilis 8b and Saccharomyces cerevisiae RWB222. S. cerevisiae RWB222 produced over 40 g/L ethanol with a yield of 0.39 g ethanol/g carbohydrate on paper sludge at 37°C, while similar titers and yields were achieved by Z. mobilis 8b at 30°C. Both S. cerevisiae RWB222 and Z. mobilis 8b exhibited decreasing cell viability at 37°C when producing over 40 g/L ethanol. A high ethanol concentration can account for S. cerevisiae RWB222 viability loss, but ethanol concentration was not the only factor influencing Z. mobilis 8b viability loss at 37°C. Over 3 g/L residual glucose was observed at the end of paper sludge SSCF by Z. mobilis 8b, and a statistical analysis revealed that a high calcium concentration originating from paper sludge, a high ethanol concentration, and a high temperature were the key interactive factors resulting in glucose accumulation. The highest ethanol yields were achieved by SSCF of paper sludge with S. cerevisiae RWB222 at 37°C and Z. mobilis 8b at 30°C. With good sugar consumption at 37°C, S. cerevisiae RWB222 was able to gain an improvement in the polysaccharide to sugar yield compared to that at 30°C, whereas Z. mobilis 8b at 30°C had a lower polysaccharide to sugar yield, but a higher sugar to ethanol yield than S. cerevisiae. Both organisms under optimal conditions achieved a 19% higher overall conversion of paper sludge to ethanol than the non‐xylose utilizing S. cerevisiae D5A at its optimal process temperature of 37°C. Biotechnol. Bioeng. 2010;107: 235–244. © 2010 Wiley Periodicals, Inc.     

Pectin substances of the callus culture of <Emphasis Type="Italic">Silene vulgaris</Emphasis> (M.) G.

Pectin-protein fraction SVC was isolated from the callus culture of the bladder campion (Silene vulgaris). The main components in it were residues of D-galacturonic acid, galactose, arabinose, rhamnose, and protein. Using ion-exchange chromatography, ultrafiltration, and acid and enzymatic hydrolysis, it was shown that SVC contained a mixture of molecules of linear pectin, branched pectin polysaccharide, and pectin-protein polymer. A fragment of the linear chain of galacturonan amounted to more than half of the entire carbohydrate silenan chain. The branched area of the macromolecule is represented by rhamnogalacturonan I. The pectin-protein polymer consisted mainly of protein and weakly branched pectin fragments with molecular mass of more than 300 kDa.