Detection of Staphylococcal Enterotoxin in Foods

A short procedure for the extraction of staphylococcal enterotoxins from food materials has been developed. The procedure involves extraction of the food at pH 4.5, centrifugation, extraction of the supernatant with CHCl(3) (pH 7.5), extraction of the enterotoxin from the water layer with CG-50 ion exchange resin (pH 5.4 to 5.9), and treatment of the eluate with agar and concentration with Carbowax 20-M. The concentrate was extracted with CHCl(3), and the water layer was lyophilized. The dried material was dissolved in a 1% trypsin solution and placed on microslides, which were incubated 24 h at 37 C. The time required for enterotoxin analysis was 3 days with microslides and 1 day with the reversed passive hemagglutination technique.     

Systematic interpolation method predicts protein chromatographic elution with salt gradients,pH gradients and combined salt/pH gradients

A methodology is presented to predict protein elution behavior from an ion exchange column using both individual or combined pH and salt gradients based on high‐throughput batch isotherm data. The buffer compositions are first optimized to generate linear pH gradients from pH 5.5 to 7 with defined concentrations of sodium chloride. Next, high‐throughput batch isotherm data are collected for a monoclonal antibody on the cation exchange resin POROS XS over a range of protein concentrations, salt concentrations, and solution pH. Finally, a previously developed empirical interpolation (EI) method is extended to describe protein binding as a function of the protein and salt concentration and solution pH without using an explicit isotherm model. The interpolated isotherm data are then used with a lumped kinetic model to predict the protein elution behavior. Experimental results obtained for laboratory scale columns show excellent agreement with the predicted elution curves for both individual or combined pH and salt gradients at protein loads up to 45 mg/mL of column. Numerical studies show that the model predictions are robust as long as the isotherm data cover the range of mobile phase compositions where the protein actually elutes from the column.     

Purification and some physicochemical properties of staphylococcal enterotoxin D.

A method was developed for the isolation of staphylococcal enterotoxin D in highly purified form from cultures of Staphylococcus aureus strain 1151m. The method involves removal of the toxin from the culture supernatant fluid with the ion-exchange resin CG-50 followed by chromatography on carboxymethylcellulose (twice) and by gel filtration on Sephadex G-75 (twice). The purified toxin is homogeneous by polyacrylamide gel and sodium dodecyl sulfate-polyacrylamide gel electrophoresis and double gel diffusion tests. It is a simple, colorless, antigenic protein with an isoelectric point of 7.4 as determined by isoelectric focusing. Its molecular weight was determined to be 27 300 +/- 700 by molecular sieve chromatography on Sephadex G-100 and sodium dodecyl sulfate-polyacrylamide gel electrophoresis. Its serological activity is stable over a wide range of pH values (1.2--10.7). The enterotoxin consists of 236 amino acid residues and contains no free sulfhydryl groups. End-group analysis showed serine to be the NH2-terminal amino acid and lysine to be the COOH-terminal amino acid.     

Separation of phycocyanin from <Emphasis Type="Italic">Spirulina platensis</Emphasis> using ion exchange chromatography

This paper presents the evaluation of some important parameters for the purification of phycocyanin using ion exchange chromatography. The influences of pH and temperature on the equilibrium partition coefficient were investigated to establish the best conditions for phycocyanin adsorption. The equilibrium isotherm for the phycocyanin-resin system was also determined. The separation of phycocyanin using the Q-Sepharose ion exchange resin was evaluated in terms of the pH and elution volume that improved the increase in purity and recovery. The highest partition coefficients were obtained in the pH range from 7.5 to 8.0 at 25 degrees C. Under these conditions the equilibrium isotherm for phycocyanin adsorption was well described by the Langmuir model, attaining a Q (m) of 22.7 mg/mL and K (d) of 3.1 x 10(-2) mg/mL. The best conditions for phycocyanin purification using the ion exchange column were at pH 7.5 with an elution volume of 36 mL, obtaining 77.3% recovery and a 3.4-fold increase in purity.     

离子交换法分离D-天冬氨酸和L-丙氨酸

对离子交换法分离D-天冬氨酸和L-丙氨酸的工艺条件进行了研究。综合考虑树脂对D-天冬氨酸和L-丙氨酸的吸附容量及相对选择系数,选择了一种适合该体系分离的树脂—XH-1,并对吸附条件及洗脱条件进行了研究,确定了最佳工艺条件,为今后工业应用提供一定的依据。     

Fluidized bed ion exchange for improving purification of lactic acid from fermentation

A strong anionic exchange resin was used to recover lactic acid directly from fermentation in an upflow fluidized bed column, resulting in 0.18 g lactic acid/g resin bound with a subsequent elution of 94%. When the culture broth was heated and adjusted pH to 8.0, 0.4 g lactic acid was bound per g resin, with a subsequent elution of 90%. L(+) and D(–) lactic acid isomers distribution was analyzed in the elution product resulting in an increase of L(+) isomer concentration. The resin did not alter its binding capacity after 23 cycles.     

Adsorption of BSA on QAE-dextran: equilibria

Equilibrium isotherms for adsorption of bovine serum albumin (BSA) on a strong-base (QAE) dextran-type ion exchanger have been determined experimentally. They were not affected by the initial concentration of BSA but were affected by pH considerably. They were correlated by the Langmuir equation when pH >/= 5.05 and by the Freundlich equation of pH 4.8, which is close to pl approximately 4.8 of BSA. The contribution of ion exchange to adsorption of BSA on the ion exchanger was determined experimentally. The maximum amounts of inorganic anion exchanged for BSA were 1% and 0.4% of the exchange capacity of the ion exchanger at pH 6.9, respectively. Since the effect of the ion exchange on the adsorption appeared small, BSA may be adsorbed mainly by electrostatic attraction when pH >/= 5.05 and by hydrophobic interaction or hydrogen bonding at pH 4.8. When NaCl coexisted in the solution, the shape of the isotherm was similar to the Langmuir isotherm, but it is shifted to the right. When the concentration of NaCl was 0.2 mol/dm(3), BsA was not adsorbed on the resin. When BSA was dissolved in pure water, the saturation capacity of BSA on HPO(4) (2-),-orm resin was about 2 times larger than that for adsorption from the solution with buffer (pH 6.9 and 8.79). The saturation capacity for adsorption of BSA in pure water on HPO(4) (2-) + H(2)O(4) (-)-from resin was much smaller than that from the solution with buffer. The isotherms for univalent Cl(-)-and H(2)PO(4) (-)-form resin was peculiar; that is, the amount of BSA adsorbed decreased with increasing the liquid-phase equilibrium concentration of BSA. (c) 1993 John Wiley & Sons, Inc.     

Biosorption of mercury by the inactivated cells of pseudomonas aeruginosa PU21 (Rip64)

Biomass of a mercury-resistant strain Pseudomonas aeruginosa PU21 (Rip64) and hydrogen-form cation exchange resin (AG 50W-X8) were investigated for their ability to adsorb mercury. The maximum adsorption capacity was approximately 180 mg Hg/g dry cell in deionized water and 400 mg Hg/g dry cell in sodium phosphate solution at pH 7.4, higher than the maximum mercury uptake capacity in the cation exchange resin (100 mg Hg/g dry resin in deionized water). The mercury selectivity of the biomass over sodium ions was evaluated when 50 mM and 150 mM of Na(+) were present. Biosorption of mercury was also examined in sodium phosphate solution andphosphate-buffered saline solution (pH 7.0), containing 50mM and 150 mM of Na(+), respectively. It was found that the presence of Na(+) did not severely affect the biosorption of Hg(2+), indicating a high mercury selectivity ofthe biomass over sodium ions. In contrast, the mercury uptake by the ion exchange resin was strongly inhibited by high sodium concentrations. The mercury biosorption was most favorable in sodium phosphate solution (pH 7.4), with a more than twofold increase in the maximum mercury uptake capacity. The pH was found to affect the adsorption of Hg(2+)bythe biomass and the optimal pH value was approximately 7.4. The adsorption of mercury on the biomass and the ion exchange resin appeared to follow theLangmuir or Freundlich adsorption isotherms. (c) 1994 John Wiley & Sons, Inc.     

Simplified Method for Purification of Clostridium perfringens Type A Enterotoxin

Purification of Clostridium perfringens type A enterotoxin from sporulated cells was simplified. The method consisted of precipitation of the enterotoxin from the extract of sonically treated cells at 40% saturation of ammonium sulfate at pH 7, differential solubilization in 0.02 M phosphate buffer, pH 6.7, and repeated gel filtration on Sephadex G-200. The purified enterotoxin was at least 98% pure in ultracentrifugation, polyacrylamide gel electrophoresis, and agar gel double diffusion. Recovery was over 74% from the sporulated cell extract. The toxin had biological activities of at least 4,700 mouse intravenous minimal lethal doses/mg of N, 3,900 capillary permeability-increasing U/mg of N in the guinea pig skin, and 210 rabbit intestinal loop distension U/mg of N. The toxin, containing no hexose, lipid, or nucleic acid, appeared to be identical in sedimentation constant, isoelectric point, and ultraviolet absorption spectrum to the toxin purified previously by different procedures.     

肝素纯化工艺中离子交换树脂的选择与应用研究

研究比较了5种树脂对肝素的吸附能力,从中选出S5428阴离子交换树脂来纯化肝素。通过对各因素的研究,确定了树脂对肝素的静态、动态吸附以及解吸的最佳条件。结果表明:静态吸附的温度45℃,pH 8.0的条件下吸附2 h,肝素的吸附率为90.5%;层析柱的动态吸附温度45℃,肝素溶液进样浓度1.0 mg/mL,进样速度1.5 mL/min,树脂柱能处理1.5 BV肝素液而不发生泄露,吸附量为3.05 mg/mL,达到饱和吸附时可处理4BV的料液,吸附量为9.18 mg/mL;采用2.0 mol/L NaCl洗脱,洗脱流速1.5 mL/min,肝素解吸率可达95.8%,肝素效价可达150 U/mg,效价回收率98%。     

Control of Nutrient Solution pH with an Ion Exchange System: Effect on Soybean Nodulation

Growth and nodulation response of soybean (Glycine max (L.) Merr.) to various single nitrogen sources in solution culture is confounded by unequal shifts in solution pH. A recirculating ion exchange system was designed in which a cation exchange resin (Amberlite IRC 50) was used to control the pH of solutions in which soybeans were grown. Nutrient solution pH levels were established at range extremes of 9.0 to 3.7 with 100% Ca²⁺ or H⁺ forms of resin, respectively. Intermediate pH levels were established by varying the ratio of Ca²⁺ to H⁺ forms of resin. The system is capable of maintaining pH within 0.5 to 0.9 units of the initial pH over a two-week growth period of soybeans with either nitrate- or urea-N sources. In the absence of the resin column, pH of the urea nutrient solution rapidly declined to less than pH 4 which resulted in depressed plant nodule development. The optimum pH range for nodule mass and N₂ fixation (measured by acetylene reduction) was between 5.2 and 7.0 with urea nutrition. Both nitrate- and ammonium-N sources were inhibitory to acetylene reduction in comparison with urea which allowed extensive nodule development and activity.     

Recovery of potassium clavulanate from fermentation broth by ion exchange chromatography and desalting electrodialysis

Ion exchange chromatography (IEC) and desalting electrodialysis (DSED) processes were developed for the recovery and purification of potassium clavulanate (KCA) from fermentation broth. A strong anion exchanger, Amberlite IRA 400 resin, a potassium acetate solution as equilibrium buffer, and a potassium chloride (KCl) solution as elution buffer were used for the recovery of KCA in IEC. In order to determine optimal operating conditions, the effects of various operating parameters such as equilibrium buffer pH and concentration, elution buffer concentration, gradient length, and volumetric flow rate on KCA recovery and by-product removal were investigated using a simulated fermentation broth. In the subsequent step of DSED, employing cation (Neocepta CMS, Tokuyama, Japan) and anion (Neocepta ACS, Tokuyama, Japan) exchange membranes were carried out to remove KCl that existed in a large amount in the ion exchanged solution. The effects of operation voltage and feed composition on the performance of DSED were investigated. Based on the operating conditions determined above, IEC and DSED were applied in sequence to an ultrafiltered fermentation broth. Almost complete removal of KCl was possible with no significant loss of KCA, although the KCA recovery was slightly lower than that with the simulated fermentation broth. Based on this observation, it was concluded that IEC and DESD could be an effective process combination for the recovery of KCA from fermentation broth.     

Rapid fractionation of bovine transferrin using immobilized gangliosides.

Bovine transferrin (BTF) was fractionated from bovine whey using ganglioside affinity chromatography. After loading the immobilized matrix with a 2% whey solution, the matrix was washed with sodium acetate buffer at pH 4 containing 1 M NaCl before elution of BTF with sodium phosphate buffers at pH 7. Concanavalin-A affinity and ion exchange chromatography were used for further purification. The ganglioside column showed a 74.2% BTF recovery from whey and BTF was enriched to 61% purity with ion exchange chromatography. Bovine transferrin was identified by SDS-PAGE and western analysis. The Concanavalin-A affinity and ion exchange chromatography steps enriched BTF in the samples and removed other whey proteins from ganglioside purified fractions. These results indicate that immobilized ganglioside can be used to fractionate BTF from bovine whey. Our novel ganglioside affinity chromatography is rapid and efficient for the fractionation of BTF from whey.     

Application of ion exchange to purify acarbose from fermentation broths

Acarbose is conventionally used to reduce the insuline consumption of the diabetic patients. This compound is an oligosaccharide with the general formulae C25H43NO18 and obtained from fermentation processes by certain strains of Actinoplanes Utahensis. After the fermentation process, the acarbose has to be isolated from the fermentation broth where is accompanied of a large amount of substances, such as substrates, intermediate metabolites, proteins and different salts.

Four strong acid resins considering geliform and macroporous matrix types in aqueous and organic media have been tested in order to reach an easy and selective separation process. According to the experimental data, the Finex CS10GC (a gel strong cationic ion exchanger) presented the maximum acarbosa uptake and also the highest rate of ion exchange in water. The best behavior in non-aqueous media was observed with the Purolite CT151 (macroporous ion exchanger) but its maximum capacity of ion exchange was really lower than that exhibited by the Finex CS10GC resin in aqueous media. These results suggest that the acarbose removal from fermentation broths must be carried out in aqueous media to ensure the maximum usage of the resin uptake capacity. The results obtained provide a significant insight into the main equilibrium phenomena that takes place depending on the characteristics of the liquid phase. Finally, the elution of acarbose from the resin can be accomplished of a selectivity way by using a solution of 2.25N of HCl. The proposed separation method seems to be technically and economically feasible.     

Kinetics and mass transfer for lactic acid recovered with anion exchange method in fermentation solution

An anion exchange method for lactic acid recovered from lactic acid-glucose solution in an ion-exchange membrane-based extractive fermentation system was examined. The exchange isotherms of anion exchange resins for lactic acid recovered were measured batchwise, and the exchange-desorption kinetics of lactic acid passing through the exchange column was investigated. The determined typical breakthrough and elution curves were measured and simulated by conventional mode. The mass transfer coefficients were identified by numberical method. The effects of the velocity of the fluid on the dynamics were studied. Aqueous NaOH solution was found to be the best solvent for elution. An experiment on anioun exchange from clarified lactic acid fermentation broth was carried out to obtain knowledge of the performance of the ion exchange system from a borth. The ion-exchange mass-transfer coefficient and efficiency from the fermentation broth is found to be lower when compared with aqueous solutions of pure lactic acid. The results show that the separation method with anion exchange resins may be used in the production of lactic acid by fermentation.(c) 1995 John Wiley & Sons, Inc.     

The application of QAE-Sephadex for the purification of two staphylococcal enterotoxins. I. Purification of enterotoxin C2.

A new method developed for purification of enterotoxin C2 from Staphylococcus aureus strain 361 consisted of four steps: batchwise adsorption from culture supernatant on QAE-Sephadex; gel filtration on Sephadex G-100; chromatography on QAE-Sephadex using a buffer of constant pH and molarity; and gel filtration using a volatile buffer of constant pH and molarity; and gel filtration using a volatile buffer as the eluting solvent. The purified enterotoxin appeared homogeneous by gel immunodiffusion, gel chromatography and in the analytical ultracentrifuge, although an apparent heterogeneity was noted on QAE-Sephadex chromatography and polyacrylamide disc electrophoresis at pH 4.5. The emetic dose, ED50, by intravenous route in cynomolgus monkeys was 0.04 mug/kg of animal weight. Upon treatment with sodium dodecylsulfate, beta-mercaptoethanol and urea, enterotoxin C2 separated into 3 bands in sodium dodecylsulfate-electrophoresis. One band mol. wt 29000, and two bands of lower molecular weight were so close that they moved as a single zone. After elution from gels, the zone of lower molecular weight were so close that they moved as a single zone. After elution from gels, the zone of lower molecular weight oligopeptides emerged as a single peak at the same position as untreated enterotoxin C2 during gel filtration with buffer lacking thiol and denaturant, and gave a reaction of complete identify to enterotoxin C2 in Ouchterlony immunodiffusion. The results suggest that enterotoxin C2 is a mixture composed of intact polypeptide chains, mol. wt 29000, and two fragments cleaved in the disulfide region of molecular weight of approx. 15400 and 12800 linked by the single disulfide bond in the toxin molecule. Amino acid analysis indicates that enterotoxin C2 consists of 255 amino acid residues.     

High performance anion exchange chromatography of reduced oligosaccharides from sialomucins

High performance anion exchange chromatography on pellicular ion exchange resins under high pH conditions with detection of sugars using a pulsed amperometric detector has been developed as a method for the separation and analysis of reduced oligosaccharides liberated from mucins by alkaline borohydride treatment. Ovine, bovine and porcine submaxillary mucins were used as models to develop the method. Although neutral reduced di-to tetraoligosaccharides were poorly retained on the column, a variety of sialylated reduced oligosaccharides could be separated efficiently. Treatment of the samples with sialidase and rechromatography identified the sialylated compounds in the elution profile. A striking finding was the greatly delayed elution times given byN-glycolylneuraminic acid containing compounds in comparison with the correspondingN-acetylneuraminic acid containing analogues. The elution profiles for the product from the mucins closely corresponded to those expected for the major oligosaccharides from these mucins. The procedures described will be useful for analysing sialomucins on a microscale without resorting to radiolabelling procedures.     

Evaluation of differences between dual salt‐pH gradient elution and mono gradient elution using a thermodynamic model: Simultaneous separation of six monoclonal antibody charge and size variants on preparative‐scale ion exchange chromatographic resin

The efficiencies of mono gradient elution and dual salt‐pH gradient elution for separation of six mAb charge and size variants on a preparative‐scale ion exchange chromatographic resin are compared in this study. Results showed that opposite dual salt‐pH gradient elution with increasing pH gradient and simultaneously decreasing salt gradient is best suited for the separation of these mAb charge and size variants on Eshmuno^® CPX. Besides giving high binding capacity, this type of opposite dual salt‐pH gradient also provides better resolved mAb variant peaks and lower conductivity in the elution pools compared to single pH or salt gradients. To have a mechanistic understanding of the differences in mAb variants retention behaviors of mono pH gradient, parallel dual salt‐pH gradient, and opposite dual salt‐pH gradient, a linear gradient elution model was used. After determining the model parameters using the linear gradient elution model, 2D plots were used to show the pH and salt dependencies of the reciprocals of distribution coefficient, equilibrium constant, and effective ionic capacity of the mAb variants in these gradient elution systems. Comparison of the 2D plots indicated that the advantage of opposite dual salt‐pH gradient system with increasing pH gradient and simultaneously decreasing salt gradient is the noncontinuous increased acceleration of protein migration. Furthermore, the fitted model parameters can be used for the prediction and optimization of mAb variants separation in dual salt‐pH gradient and step elution. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:973–986, 2018     

Modified method for production and purification of Staphylococcus aureus enterotoxin B.

A medium containing 4% bio-trypcase and 1% yeast extract was used for the production of Staphylococcus aureus enterotoxin B. The yield obtained was estimated at 200 micrograms of enterotoxin per ml of S. aureus S-6 culture supernatant. The purification method involves chromatography on Biorex 70 resin, isoelectric focusing, and gel filtration on Sephadex G-100. The purified enterotoxin (isoionic point, pH 8.55) was shown to be homogenous protein with a molecular weight of 29,000 when tested by gel electrophoresis.     

Analysis, Production, and Isolation of an Extracellular Laccase from Polyporus anceps

Methods are described for the analysis, production, and isolation of laccase produced by a strain of Polyporus anceps. A simple quantitative colorimetric assay based on the oxidation of syringaldazine to syringaldazine quinone is described. Using a defined medium supplemented with the amino acids cysteine and histidine and with elevated phosphate, consistently high titers of laccase were obtained. The enzyme was isolated directly from fermentation medium by binding to diethylaminoethyl cellulose, and, once bound to the ion exchanger, it could be stored for 6 months at -70°C with minimal loss of activity. The enzyme was quantitatively recovered from the resin by elution with 0.2 M phosphate buffer (pH 5.0).