Chromatographic separation of proteins on metal immobilized iminodiacetic acid-bound molded monolithic rods of macroporous poly(glycidyl methacrylate-co-ethylene dimethacrylate)

Continuous rod of macroporous poly(glycidyl methacrylate-co-ethylene dimethacrylate) was prepared by a free radical polymerization within the confines of a stainless-steel column. The epoxide groups of the rod were modified by a reaction with iminodiacetic acid (IDA) that affords the active site to form metal IDA chelates used for immobilized metal affinity chromatography (IMAC). The efficiency of coupling of IDA to the epoxide-contained matrix was studied as a function of reaction time and temperature. High-performance separation of proteins, based on immobilized different metals on the column, were described. The influence of pH on the adsorption capacity of bovine serum albumin on the Cu2+-IDA continuous rod column was investigated in the range from 5.0 to 9.0. Purification of lysozyme from egg white and human serum albumin (HSA) on the commercially available HSA solution were performed on the naked IDA and Cu2+-IDA continuous rod columns, respectively; and the purity of the obtained fractions was detected by matrix-assisted laser desorption-ionization time-of-flight mass spectrometry.     

Displacement chromatography of proteins on hydrophobic charge induction adsorbent column

Displacement chromatography of protein mixtures is proposed on hydrophobic charge induction chromatography (HCIC). We have used an HCIC medium, MEP-Hypercel as the stationary phase and a quaternary ammonium salt, benzethonium chloride, as the displacer. It was found that the multiple interactions between proteins/displacer and the HCIC sorbent, i.e. hydrophobic interaction and charge repulsion, enabled a greater flexibility for the design of displacement processes and ease of column regeneration by adjustment of pH. The capacity factors of proteins and displacers were used to predict their performances in column displacement, and the experimental results agreed well with the prediction. An isotachic displacement train of lysozyme and alpha-chymotrypsinogen A was formed with benzethonium chloride as the displacer at pH 5.0 with good yields and purities of the two proteins. Column regeneration was efficiently achieved by charge repulsion between the displacer and the adsorbent at lower pH values (pH 3 and 4). The results indicate that the displacement chromatography on HCIC is a good alternative to traditional hydrophobic displacement chromatography.     

Examination of the binding behaviour of several proteins with the immobilized copper(II) complexes of o-, m- and p-xylylene bridged bis(1,4,7-triazacyclononane) macrocycles

Three new IMAC chelating systems, incorporating immobilised xylenyl-bridged bis(1,4,7-triaza-cyclonane) ligands, complexed with Cu(2+) ions to form binuclear species, have been prepared. Their binding properties have been investigated with three small globular proteins (hen egg white lysozyme, horse skeletal muscle myoglobin and horse heart cytochrome c). The effects of buffer pH, ionic strength and composition on the binding behaviour of these proteins to these new IMAC sorbents have been examined and compared with those found for the corresponding immobilized mononuclear copper complex of 1,4,7-triazacyclononane (tacn). Higher protein binding affinities were observed with the Cu(2+)-bis(tacn) sorbents compared to the Cu(2+)-tacn system, consistent with the immobilized binuclear copper(II) species undergoing enhanced coordinative interaction with the surface-exposed histidine residues of these proteins. Moreover, the protein binding characteristics of these IMAC sorbents at higher ionic strengths, such as 1M NaCl, also reflect the presence of the aromatic ring in the bis(tacn) ligands, whereby hydrophobic pi/pi stacking interactions can occur with the proteins.     

Displacement chromatography of biomolecules

Displacement chromatography was used for the preparative-scale separation of peptides, antibiotics, and proteins. The feed components were both purified and concentrated during the separation processes. The components of a peptide mixture were separated on a reverse-phase analytical column using 2-(2-butoxyethoxy) ethanol as the displacer. The use of organic modifiers in the carrier along with an elevated column temperature of 45 degrees C enabled the efficient separation of relatively hydrophobic peptides by displacement chromatography. In addition, the throughput of the process was significantly increased by carrying out the separation at an elevated flow-rate with no adverse effect on product purity. The antibiotic cephalosporin C was isolated from impurities in a fermentation broth using 2-(2-butoxyethoxy)ethanol as the displacer along with a step change in column temperature. The proteins cytochrome c and lysozyme were purified on a weak cation-exchanger column using cationic polymers as the displacers. While polymers of 60 and 20 kilodaltons were both found to be good displacers for these proteins, only the lower molecular weight polymer was readily removed from the column by standard regeneration techniques.     

Hen egg white fractionation by ion-exchange chromatography

Major hen egg white proteins have been widely studied for their functional properties but these studies still are unable to explain, alone, all of the biological properties of hen egg white. Hence, it is still interesting to produce pure and non-altered proteins to improve our knowledge on the biological properties of hen egg white. Presently, identification and characterization of both bioactive peptides and minor proteins from hen egg white is essential work for progressing in the understanding of hen egg white biological properties. With this objective in mind, a new process for a complete "mucin free" hen egg white fractionation based on ion exchange chromatography is proposed. "Mucin free" egg white is fractionated into six different fractions. Four of them are high-recovery yield purified fractions of lysozyme, ovotransferrin, ovalbumin and flavoprotein. The two other fractions are enriched in recently detected minor proteins in hen egg white.     

高效阳离子交换法分离纯化蛋清中的溶菌酶

 建立了用高效阳离子交换分离纯化蛋清中溶菌酶的新方法 ,讨论了纯化的工艺条件。蛋清样品匀浆后 ,用氯化钠初步纯化 ,然后用弱阳离子交换柱XIDACE WCX分离。结果表明 ,被纯化的溶菌酶和杂蛋白得到很好分离。经活性检测 ,溶菌酶过柱后的活性回收率为 10 7% ,蛋白的比活为 15 4 6 7U/mg ,纯化倍数提高了 5 6倍。用尺寸排阻 (SEC)鉴定 ,得到的溶菌酶呈均一性。该法较传统软基质低压离子交换分离速度快 ,纯化效率高。     

Selective displacement chromatography in multimodal cation exchange systems

A library of displacer analogues with varying degrees of electrostatic, hydrophobic and hydrogen bonding moieties was evaluated for their ability to enhance the selectivity of multimodal (MM) chromatography under high loading conditions. The library was screened for displacement of model proteins using a robotic liquid handling system and selective batch separations were achieved for proteins that were inseparable with linear gradient chromatography. Trends in protein displacement were identified and displacers with higher hydrophobicity and net charge exhibited improved protein displacements. Proteins that interacted with the resins primarily via electrostatic interactions were more readily displaced than those that possessed a significant hydrophobic contribution to their binding. In addition, multimodal displacers were found to be more selective than single mode electrostatic displacers. Column chromatography studies were also carried out and baseline separations were achieved for model protein pairs using selective displacement. Finally, operation of these columns in the desorption mode resulted in baseline separation of model proteins which were not separable by selective displacement chromatography. This study indicates that the inherent selectivity of MM resins can be augmented by the selectivity of the displacer under non-linear competitive binding conditions, creating new opportunities for protein separations not possible using traditional gradient operations.     

用蛋白电泳和高效凝胶排阻色谱法分析还原脲变性蛋白溶菌酶稀释复性过程的集聚体

本文利用蛋白电泳和高效凝胶排阻层析法分析了还原脲变性蛋白溶菌酶稀释复性过程中的集聚体。当用复性液稀释复性还原脲变性蛋白溶菌酶时,会迅速产生可观量的沉淀。沉淀和上清液的不连续十二烷基硫酸钠-聚丙烯酰胺凝胶电泳(SDS-PAGE)和高效凝胶排阻层析分析结果表明,还原脲变性蛋白溶菌酶在稀释复性过程中除了能够复性成天然态蛋白溶菌酶分子外,还会形成可溶的蛋白溶菌酶分子二聚体和三聚体,二聚体和三聚体主要是靠分子间二硫键的错配连接而成的;可溶的蛋白溶菌酶分子二聚体之间通过非共价键相互作用而形成集聚体沉淀,而可溶的三聚体溶菌酶分子则仍处于复性液上清液中。     

Fractionation of low-molecular-mass heparin by centrifugal partition chromatography in the ion-exchange displacement mode

Centrifugal partition chromatography in the ion-exchange displacement mode allowed a preparative and efficient fractionation of low-molecular-mass heparins from enoxaparin sodium. Amberlite LA2--a lipophilic liquid secondary amine--was chosen as a weak anion exchanger. The biphasic system methyl isobutyl ketone-water was selected. Protonated LA2 (10%, v/v) was added to the organic stationary phase. Hydroxide (Na+, OH-) was chosen as a displacer in the aqueous mobile phase. The observed pH and concentration profiles are typical of displacement chromatography, as supported by numerical simulation. The Dubois test for the analysis of sugar content and an analysis of sulfur content (and consequently sulfatation rate) were carried out to monitor the effectiveness of the procedure. Moreover, the fractions were analyzed by high-performance size-exclusion chromatography and the 1H NMR spectra confirmed the fractionation of the sample of enoxaparin sodium.     

Mass influences in the performance of oligomeric poly(diallyldimethylammonium chloride) as displacer for cation-exchange displacement chromatography of proteins

A novel type of linear polyelectrolyte, namely poly-DADMAC [poly(diallyldimethylammonium chloride)], was prepared and studied as a displacer for cation-exchange displacement chromatography of proteins. In contrast to the commercially available polymers of that chemistry, the novel type of poly-DADMAC introduced here is characterized by a homogeneous linear structure, a narrow distribution of the (adjustable) molar mass as well as by a defined and homogeneous affinity for the stationary phase. Five poly-DADMACs of different size (17900 to 88000 g/mol) were prepared and compared with regard to their stationary phase affinity and protein separation potential, taking a mixture of basic proteins, namely lysozyme, cytochrome C, and ribonuclease A (from bovine pancreas), as an example. The steric mass action model was employed to aid method development. Under the chosen conditions (low ionic strength of the mobile phase guaranteeing strong binding of both the proteins and the displacer) the poly-DADMAC with the lowest molar masses proved to be the most efficient displacers for the basic proteins with a stationary phase affinity constant of 5.3 x 10(16) and a steric factor of 224. Using this substance as displacer, a sample mixture containing up to three proteins was separated and the proteins recovered at high yields (80-97%) and in high purity and concentration.     

非还原脲变性蛋白溶菌酶稀释复性过程中集聚现象的研究

用十二烷基硫酸钠-聚丙烯酰胺凝胶电泳、阴极聚丙烯酰胺凝胶电泳和高效凝胶排阻色谱法, 研究了非还原脲变性蛋白溶菌酶在稀释复性过程中的集聚现象. 实验发现, 在整个稀释复性过程中, 没有蛋白溶菌酶集聚体沉淀产生. 当最终复性液中蛋白溶菌酶浓度小于4.0 mg/mL时, 复性过程中不会形成蛋白溶菌酶分子集聚体; 当最终复性液中蛋白溶菌酶浓度介于4.0～8.0 mg/mL时, 复性过程中会形成由非共价相互作用所引起的蛋白溶菌酶二分子和三分子集聚体; 而当最终复性液中蛋白溶菌酶浓度大于8.0 mg/mL时, 复性过程中除了会形成二分子和三分子蛋白溶菌酶集聚体外, 还会形成四分子蛋白溶菌酶集聚体. 在此基础上, 结合文献, 对非还原脲变性蛋白溶菌酶的稀释复性过程进行了描述.     

An integrated process for purification of lysozyme, ovalbumin, and ovomucoid from hen egg white

This article describes an integrated process for simultaneous purification of lysozyme, ovalbumin, and ovomucoid from hen egg white. The crude egg white extract was passed through a cation exchanger Streamline trade mark SP and the bound lysozyme was eluted with 5% ammonium carbonate, pH 9.0, containing 1 M NaCl after elution of avidin. This partially purified lysozyme was further purified 639-fold on dye-linked cellulose beads. Ovalbumin and ovomucoid did not bind to Streamline SP. Ovalbumin could be precipitated from this unbound fraction by 5% trichloroacetic acid, and ovomucoid was removed from the supernatant by precipitation with ethanol. The yields of lysozyme, ovomucoid, and ovalbumin were 77, 94, and 98%, respectively. All the purified proteins showed single bands on sodium dodecyl sulfate polyacrylamide gel electrophoresis. All the steps are easily scalable, and the process described here can be used for large-scale simultaneous purification of these proteins in the pure form.     

Cu(II)-loaded iminodiacetic acid-silica particles for protein profiling of human serum samples using surface-enhanced affinity capture: support porosity effects

Silica particles of different porosity were functionalised with iminodiacetic acid (IDA) and loaded with Cu(II) ions to yield Cu(II)-IDA-silica. These immobilised metal affinity chromatography (IMAC) materials were subjected to a comprehensive characterisation study. The Cu(II) content--determined via UV/Vis spectroscopy and atomic absorption spectroscopy (AAS)--was found to be linearly dependent on the specific surface area of the silica particles. The evaluation of protein adsorption isotherms provided information on binding properties towards biomolecules. The data fitted Langmuir's adsorption theory. Binding capacity of hen egg white lysozyme (HEWL) was highest for Cu(II)-IDA-silica with mean pore diameter of 120 A, reaching nearly 350 mg/g. All derivatised materials were applied to the fractionation of human serum samples and subsequent mass spectrometric analysis (m/z: 2000-10,000) according to a surface-enhanced affinity capture (SEAC) protocol. Pore size of the support material affected the appearance of the mass spectra to a great extent, showing that surface morphology is another parameter that has to be considered in addition to surface chemistry. Signal intensity as well as the number of detected masses were strongly dependent on the pore diameter, indicating that the carrier material has to be carefully chosen to assure best results.     

High performance displacement chromatography of proteins: Separation of β-Lactoglobulins A and B

Summary β-Lactoglobulins A and B were separated by high performance displacement chromatography on an anion-exchanger column with chondroitin sulfate as the displacer. A sample of 100 mg containing a mixture of the two β-lactoglublins was separated on a column of 75×7.5 mm in a single chromatographic run. The separation process followed the rules of the classical displacement development: the two proteins formed contiguous rectangular bands and their concentrations were dependent on the displacer concentration. The results demonstrate that high performance displacement chromatography is a useful technique for the separation of proteins in preparative amounts with columns and instrumentation typically used in analytical HPLC. Furthermore, it has the potential to become the method of choice in large scale separation of proteins.     

Displacer concentration effects in displacement chromatography: Implications for trace solute detection

In this paper, the utility of ion-exchange displacement chromatography for the concentration and enrichment of trace proteins is examined. Separations with varying displacer concentrations (1–25 mM neomycin sulfate) indicate that higher concentrations result in elevated protein concentrations, at the price of reduced yields. The results demonstrate that displacement chromatography carried out at relatively low displacer concentrations (2.5 mM) can produce significant concentration (8.5-fold) and enrichment (18-fold) of trace proteins present in the feed. Parametric simulations using the steric mass action model are carried out to investigate the concentration effects and enrichment factors observed over a wide range of feed, displacer and buffer counter-ion concentrations, and solute separation factors. The simulations confirm that trace components can be readily concentrated and enriched by displacement chromatography and that these effects will be more pronounced as the separation factor between trace and abundant components is increased. The results presented in this paper indicate the potential of displacement chromatography for improved separations where trace enrichment is critical such as proteomic applications.     

Ion-exchange displacement chromatography of proteins Dextran-based polyelectrolytes as high affinity displacerss

Dextran-based polyelectrolyte displacers were successfully employed for the displacement purification of proteins in ion-exchange displacement systems. The effect of molecular mass was investigated by examining the efficacy of DEAE-dextran and dextran sulfate displacers of various molecular masses in cation- and anion-exchange systems, respectively. Induced salt gradients produced during these displacement experiments were measured in order to study their effect on the protein separations. The unique characteristics of these displacements were well predicted by simulations obtained from a steric mass action (SMA) ion-exchange model. These displacements differ from the traditional vision of displacement chromatography in several important ways: the isotherm of the displacer does not necessarily lie above the feed component isotherms; the concentration of the displaced proteins can sometimes exceed that of the displacer; higher-molecular-mass displacers are not necesarily more efficacious than lower-molecular-mass compounds; and the salt gradients induced by the adsorption of the displacer produce different salt micro-environments for each displaced protein.     

Characterization and modeling of nonlinear hydrophobic interaction chromatographic systems

A general rate model was employed in concert with a preferential interaction quadratic adsorption isotherm for the characterization of HIC resins and the prediction of solute behavior in these separation systems. The results indicate that both pore and surface diffusion play an important role in protein transport in HIC resins. The simulated and experimental solute profiles were compared for two model proteins, lysozyme and lectin, for both displacement and gradient modes of chromatography. Our results indicate that a modeling approach using the generate rate model and preferential interaction isotherm can accurately predict the shock layer response in both gradient and displacement chromatography in HIC systems. While pore and surface diffusion played a major role and were limiting steps for proteins, surface diffusion was seen to play less of a role for the displacer. The results demonstrate that this modeling approach can be employed to describe the behavior of these non-linear HIC systems, which may have implications for the development of more efficient preparative HIC separations.     

Salt effects in anion exchange displacement chromatography: Comparison of pentosan polysulfate and dextran sulfate displacers

Summary Experimental studies were carried out to investigate the utility of pentosan polysulfate as a low molecular weight polyelectrolyte displacer for the purification of proteins in anion-exchange displacement systems. In addition, the influence of mobile phase salt concentration on displacer efficacy, protein-protein resolution, and displacement development were studied for several anionic displacers. It was found that while large polyelectrolytes (50 kd dextran sulfate) were efficient displacers for a wide range of salt concentrations, relatively small polyelectrolytes (3 kd pentosan polysulfate) were seen to act as an efficient displacer only under conditions of high salt micro-environments. In addition, for proteins exhibiting similar affinities, zone mixing at the protein-protein boundary was found to be quite sensitive to the salt concentration. Finally, displacement chromatography was successfully implemented for the separation of proteins from milk whey.     

Microscale isolation of native forms of lysozyme from chicken egg white by gel isoelectric focusing

To separate and extract the native states of lysozyme from chicken egg white, a hybrid method for the mobilization of proteins after non‐denaturing gel isoelectric focusing (IEF) combined with detection of lysozyme activity was developed. When the proteins in the chicken egg white were first separated using non‐denaturing gel IEF, a lysozyme was obtained at the top of the gel column at the cathode end of the IEF. And, when the IEF‐separated proteins of the egg white were mobilized by replacing the cathodic sodium hydroxide solution with phosphoric acid solution, an additional active state of the lysozyme that could be bound to proteins, such as ovotransferrin, was extracted from the solution. Furthermore, it was shown that the addition of lysozyme, obtained via IEF, to pure ovotransferrin generated a complex manifesting lysozyme activity, clearly indicating a successful reconstruction of the lysozyme‐ovotransferrin complex in vitro. Therefore, the obtained results demonstrated that the native states of lysozymes, such as lysozyme and the lysozyme‐ovotransferrin complex, can be effectively separated and extracted using non‐denaturing gel IEF. Thus, this method can be applied to separate and extract different charge states of native proteins that retain their biological activities.     

Purification of low-abundance lysozyme in egg white via free-flow electrophoresis with gel-filtration chromatography

As an effective separation tool, free-flow electrophoresis has not been used for purification of low-abundance protein in complex sample matrix. Herein, lysozyme in complex egg white matrix was chosen as the model protein for demonstrating the purification of low-content peptide via an FFE coupled with gel fitration chromatography (GFC). The crude lysozyme in egg while was first separated via free-flow zone electrophoresis (FFZE). After that, the fractions with lysozyme activity were condensed via lyophilization. Thereafter, the condensed fractions were further purified via a GFC of Sephadex G50. In all of the experiments, a special poly(acrylamide- co-acrylic acid) (P(AM-co-AA)) gel electrophoresis and a mass spectrometry were used for identification of lysozyme. The conditions of FFZE were optimized as follows: 130 μL/min sample flow rate, 4.9 mL/min background buffer of 20 mM pH 5.5 Tris-Acetic acid, 350 V, and 14 °C as well as 2 mg/mL protein content of crude sample. It was found that the purified lysozyme had the purity of 80% and high activity as compared with its crude sample with only 1.4% content and undetectable activity. The recoveries in the first and second separative steps were 65% and 82%, respectively, and the total recovery was about 53.3%. The reasons of low recovery might be induced by diffusion of lysozyme out off P(AM-co-AA) gel and co-removing of high-abundance egg ovalbumin. All these results indicated FFE could be used as alternative tool for purification of target solute with low abundance.