Bovine plasma protein fractionation by ion exchange chromatography

An ion exchange chromatography process was developed to separate the main protein fractions of bovine blood plasma using a composite material, Q-HyperD resin, and a gel material, DEAE-Sepharose. The experiments were carried out at semipreparative scale. It was necessary to establish analytical methods of electrophoresis and HPLC to identify the fractionated proteins. Results show that these materials are able to adequately fractionate different protein groups from the raw blood plasma. This method may be used to avoid chemical fractionation using agents such as ethanol or PEG and, thus, decrease protein denaturation of the different fractions to be used for research or pharmaceutical purposes. The Q-HyperD resin presents a better retention capacity for plasma protein than DEAE-Sepharose under the experimental conditions employed.     

L-谷氨酰胺在强酸性离子交换树脂上的稳定性

研究了谷氨酰胺在强酸性阳离子交换树脂「氢型」上离子交换时的化学稳定性,结果显示,在典型的及所述其他实验条件下,谷氨酰胺相当稳定。典型离交过程：１００ｍｌ去菌体谷氨酰胺发酵液含主要成份谷氨酰胺、谷氨酸和硫酸铵分别为３１２ｍｍｏｌ／Ｌ、６７．０ｍｍｏｌ／Ｌ和０．７５ｍｏｌ／Ｌ,离子交换柱床层体积２００ｍｌ,离交流速１．０ＢＶ／ｈ,０．５ｍｏｌ／Ｌ氨水洗脱流速０．５ＢＶ／ｈ。     

Interfacial thermodynamics of protein adsorption, ion co-adsorption and ion binding in solution. II. Model interpretation of ion exchange in lysozyme chromatography

In this paper we present a model for the ion exchange effects in protein adsorption. The model is applied to chromatography of lysozyme on strong cation exchanger ‘mono S’. The experimental and general thermodynamic aspects have been discussed in Part 1, the preceding paper. The main modelling assumptions are (i) the charge regulation is confined to the small layer of contact between adsorbed protein and exchanger surface, (ii) the contact layer as a whole is electroneutral and (iii) the number of protein acid/base groups and exchanger surface acid groups which participate in the ion exchange is proportional to the area of the contact layer. The model is fitted to the experimental data by adjustment of only two or three parameters. The experimental co-adsorption numbers are very well reproduced. A few conspicuous features emerge: (i) the number of protein acid/base groups and exchanger surface acid groups in the contact layer varies with the medium conditions, such that the number is higher when the interaction between protein and exchanger surface is stronger. (ii) There is indirect evidence for structural alterations in the upper layers of the exchanger surface: the adsorbed protein is probably partly ‘buried’ in the surface.     

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.     

The impact of protein exclusion on the purity performance of ion exchange resins

Dynamic binding capacity (DBC) decreases with increasing conductivity in the equilibrium regime for ion exchange chromatography. An exclusion regime has been demonstrated in ion exchange resins where DBC increases with increasing conductivity and decreasing protein charge. The purpose of this work was to examine the impact of the exclusion regime on impurity removal. Resin performance was evaluated based on dynamic binding capacities and purity within the exclusion and equilibrium regimes. The results revealed that Chinese hamster ovary proteins (CHOP), a major impurity, exhibit similar exclusion trends as the MAb proteins. The results further the understanding of the exclusion regime and its impact on product purity, a critical area for IEX development and optimization.     

Obtaining highly purified intrinsically disordered protein by boiling lysis and single step ion exchange

Intrinsically disordered proteins (IDPs) is a term used to describe proteins that do not have a well-defined tertiary structure. IDPs have many roles such as in cell cycle control (p53), neuronal signal transmission (myelin basic protein), and protein stability (dehydrins). Producing recombinant IDPs in bacteria for nuclear magnetic resonance (NMR) studies is problematic because the lack of stable tertiary structure makes them excellent substrates for bacterial proteases, which will cause loss in yield. We have developed a two-step method to produce the grape dehydrin K₂ and YSK₂ using Escherichia coli. Dehydrins are expressed by certain plants in response to dehydration, increased salinity, or low temperatures. Purification of 10 mg/L (K₂) and 15 mg/L (YSK₂) was performed by boiling bacterial pellets to lyse the cells, remove most of the contaminating proteins, and denature bacterial proteases. This resulted in protein purity comparable to that produced by sonication and nickel affinity chromatography. Boiling was followed by cation exchange chromatography to remove the remaining trace contaminants. The sample was shown to be more than 95% pure by reversed-phase high-performance liquid chromatography. The method presented here can easily be adapted to the purification of other IDPs and heat-stable proteins without requiring multiple chromatography steps or the use of protease inhibitors.     

Interfacial thermodynamics of protein adsorption, ion co-adsorption and ion binding in solution. I. Phenomenological linkage relations for ion exchange in lysozyme chromatography and titration in solution

In this paper we discuss the thermodynamics of ion binding in solution, protein adsorption and ion co-adsorption. The emphasis is on charge regulation effects. To this end, we introduce phenomenological linkage relations from which the ion binding can be calculated from the electrolyte dependency of proton titration curves and the co-adsorption from the electrolyte dependency of protein adsorption isotherms. The linkage relations are derived from classical interfacial thermodynamics, and thus offer an alternative approach as compared to the mass balance equations which are currently used in biotechnology, and Record et al.'s 1978 analysis of Wyman's Binding Polynomial for protein interactions. The co-adsorption theory is an extension of our previous analysis of ion binding in solution, which we include here for comparison of the ion co-adsorption with the ion binding in solution. The theory is applied to the chromatography of lysozyme on the strong cation exchanger ‘mono S’ and to the proton titration of lysozyme in solution. In the accompanying Part 2 of this paper the results are interpreted with a simple model.     

离子交换层析纯化透明质酸

考察6种离子交换树脂的静态吸附解析效果,选出201＊7阴离子交换树脂填柱,确定洗脱流速为0.6mL/min,40mL0.3mol/LNaCl和50mL0.5mol/L NaCl双浓度洗脱,实现透明质酸和杂蛋白的分离。制得透明质酸产品蛋白含量为0.057%,葡萄糖醛酸含量为43%,平均相对分子质量大于1.1×10^6,收率为54%,符合医用级透明质酸行业标准的要求。     

Separation of D- and L-amino acids by ion exchange column chromatography in the form of alanyl dipeptides

Summary A method of ion exchange column chromatography was developed for the determination of D- and L-amino acids in the form of diastereomeric dipeptide. First the protein containing samples were hydrolyzed with 6 molar hydrochloric acid, then the single amino acids were separated in an LKB automated amino acid analyzer with the LKB fraction collector. Following lyophilization, the single amino acids were transformed into alanyl dipeptides with tertiary-butyloxycarbonil-L-alanine-N-hydroxy-succinimide (t-BOC-L-Ala-ONSu) active ester. The alanyl dipeptides were easily separated from one another and the initial amino acids. Determination of the D- and L-amino acids in this form is relatively accurate and reproducible but takes some time (33–38 min). Accuracy of the determination is satisfactory. The coefficient of variation amounts to 3–5%. The use of the method is suggested to laboratories having an amino acid analyzer and wish to determine D-and L-amino acids in synthetic-amino acids complements, peptides or natural materials.     

A rapid ion exchange procedure that facilitates spectrophotometric assays of phosphorylated metabolites in potato extracts

A variety of metabolites are routinely assayed after perchloric acid extraction of plant tissues. A common technique uses coupled enzyme assays that produce or consume pyridine nucleotides together with spectrophotometric detection at 340 nm. Because of the presence of pigments in plant tissues, the high absorbance of such extracts usually limits the amount of extract that can be assayed spectrophotometrically. Here, we show that after batch adsorption with AG50WX8 (H⁺ form), the absorbance of potato root perchloric acid extracts at 340 nm is significantly reduced. This clean up procedure does not interfere with the assay or the recovery of anionic metabolites such as hexose phosphates. It therefore facilitates spectrophotometric assays of metabolites in plant extracts with high absorbance.     

Densonucleosis virus purification by ion exchange membranes

Preparative chromatography is widely used in the downstream purification of biopharmaceutical products. Replacement of resins by membranes as chromatographic supports, overcomes many of the limitations associated with resin-based chromatography such as high-pressure drops, slow processing rates due to pore diffusion and channeling of the feed through the bed. In particular, adsorptive membranes may be ideally suited for virus capture. Virus capture is critical in a number of applications. In gene therapy and vaccine production, large-scale purification of virus vectors is often essential. In the manufacture of biopharmaceuticals, validation of virus clearance is critical.Here results for purification of Aedes aegypti densonucleosis virus (AeDNV) using anion and cation exchange membranes are presented. AeDNV is a non-enveloped, single-stranded mosquito-specific parvovirus. Virus particles are around 20 nm in size. AeDNV could find potential applications in integrated vector-borne disease control programs. In addition, capture of parvovirus for validation of virus clearance in the manufacture of biopharmaceuticals is of commercial importance.By adjusting the pH of the feed stream, AeDNV particles may be adsorbed by both anion and cation exchange membranes. However, strongly basic anion exchange membranes were the most effective in adsorbing AeDNV particles. Adsorption and subsequent elution of AeDNV by anion exchange membranes leads to significant virus concentration. Dynamic and static capacities for anion exchange membranes were similar. Further, a sharp elution curve was obtained suggesting that pore diffusional resistances are insignificant. The adsorption of AeDNV particles by anion exchange membranes may be described by a linear isotherm.     

Effect of fouling on the capacity and breakthrough characteristics of a packed bed ion exchange chromatography column

This study examined the impact of fouling with yeast homogenate on capacity and breakthrough performance of an ion exchange packed bed column. Column performance was assessed by analysis of breakthrough curves obtained with BSA as a test protein. The overall impact of fouling on breakthrough performance depended heavily on the level of clarification of the feed stream. Challenging the column with particulate-free homogenate caused no change in column performance. Loading successive small volumes of poorly clarified homogenate, interspersed with frequent column salt washes, did not alter significantly the column capacity. By contrast, when the column was challenged with an equivalent cumulative volume of poorly clarified homogenate, dynamic binding capacity decreased significantly and changes in breakthrough curves suggested increased intraparticle and external mass transfer limitations. These changes were ascribed to deposition of solid particulates in void spaces in the bed and colloidal contaminants in the bead pores.     

Arginine metabolism by pumpkin seedlings. Separation of plant extracts by ion exchange resins

Arginine-U-¹⁴C was injected into the cotyledons of 7-day oldpumpkin seedlings. At most, 24% of the administered ¹⁴C wastransported to the axis tissue. The amounts of arginine incorporatedinto cotyledonary protein suggests that turnover was occurringat a rapid rate. Arginine was extensively metabolized, and after96 hr 50% of the administered ¹⁴C had been released as ¹⁴CO₂.The remaining label was primarily in unmetabolized arginine,protein or transported to the axis tissue with little labelin other amino acids. The results suggest that the carbon fromarginine is incorporated into protein or catabolized to CO₂while the carbon for new amino acid skeletons is derived fromsugar. A simple, reproducible method for the quantitative fractionationof plant extracts or hydrolysates of insoluble plant materialinto basic amino acids, acidic amino acids, neutral amino acids,organic acids and sugars was reported. (Received September 10, 1968; )     

High-throughput protein purification under denaturating conditions by the use of cation exchange chromatography

A high-throughput protein purification strategy using the polycationic Z(basic) tag has been developed. In order for the strategy to be useful both for soluble and less soluble proteins, a denaturating agent, urea, was used in all purification steps. First, four target proteins were genetically fused to the purification tag, Z(basic). These protein constructs were purified by cation exchange chromatography and eluted using a salt gradient. From the data achieved, a purification strategy was planned including stepwise elution to enable parallel protein purification using a laboratory robot. A protocol that includes all steps, equilibration of the chromatography resin, load of sample, wash, and elution, all without any manual handling steps, was handled by the laboratory robot. The program allows automated purification giving milligram amounts of pure recombinant protein of up to 60 cell lysates. In this study 22 different protein constructs, with different characteristics regarding pI and solubility, were successfully purified by the laboratory robot. The data show that Z(basic) can be used as a general purification tag also under denaturating conditions. Moreover, the strategy enables purification of proteins with different pI and solubility using ion exchange chromatography (IEXC). The procedure is highly reproducible and allows for high protein yield and purity and is therefore a good complement to the commonly used His(6)-tag.     

Remediation of contaminated soils by biotechnology with nanomaterials: bio-behavior,applications, and perspectives

Soil contamination caused by heavy metals and organic pollutants has drawn world-wide concern. Biotechnology has been applied for many years to the decontamination of soils polluted with organic and inorganic contaminants, and novel nanomaterials (NMs) has attracted much concern due to their high capacity for the removal/stabilization/degradation of pollutants. Recently, developing advanced biotechnology with NMs for the remediation of contaminated soils has become a hot research topic. Some researchers found that bioremediation efficiency of contaminated soils was enhanced by the addition of NMs, while others demonstrated that the toxicity of NMs to the organism negatively influenced the repair capacity of polluted soils. This paper reviews the application of biotechnology and NMs in soil remediation, and further provides a critical view of the effects of NMs on the phytoremediation and micro-remediation of contaminated soils. This review also discusses the future research needs for the combined application of biotechnology and NMs in soil remediation.     

Purification of recombinant aprotinin from transgenic corn germ fraction using ion exchange and hydrophobic interaction chromatography

Plants have attracted interest as hosts for protein expression because of the promise of a large production capacity and a low production cost. However, recovery costs remain a challenge as illustrated for recovery of recombinant aprotinin, a trypsin inhibitor, with removal of native corn trypsin inhibitor from transgenic corn (Azzoni et al. in Biotechnol Bioeng 80:268–276, 2002). When expression is targeted to corn grain fractions, dry milling can separate germ and endosperm fractions. Hence, only the product-containing fraction needs to be extracted, reducing the cost of extraction and the impurity level of the extract. Selective extraction conditions can reduce impurity levels to the point that low-cost adsorbents can result in relatively high purity levels. In this work, we attempted to achieve comparable purity with these lower cost methods. We replaced whole grain extraction and purification of recombinant aprotinin with sequential trypsin affinity and IMAC steps with an alternative of germ fraction extraction and purification with ion exchange and hydrophobic interaction chromatography (HIC). Using germ extraction at acidic pH supplemented with heat precipitation to remove additional host proteins resulted in a higher specific activity feed to the chromatographic steps. The cation exchange step provided 7.6× purification with 76.4% yield and no sodium dodecyl sulfate–polyacrylamide gel electrophoresis detectable native corn trypsin inhibitor. After the HIC step (2.7× step purification with 44.0% yield), the final product had a specific activity that was 75.3% of that of the affinity-purified aprotinin.