Effect of charge regulation on steric mass-action equilibrium for the ion-exchange adsorption of proteins

A thermodynamic formalism is developed for incorporating the effects of charge regulation on the ion-exchange adsorption of proteins under mass-overloaded conditions as described by the steric mass-action (SMA) isotherm. To accomplish this, the pH titration behavior of a protein and the associated adsorption equilibrium of the various charged forms of a protein are incorporated into a model which also accounts for the steric hindrance of salt counterions caused by protein adsorption. For the case where the protein is dilute, the new model reduces to the protein adsorption model described recently by the authors which accounts for charge regulation. Similarly, the new model reduces to the steric mass-action isotherm developed by Brooks and Cramer which applies to mass-overloaded conditions for the case where charge regulation is ignored so that the protein has a fixed charge. Calculations using the new model were found to agree with experimental data for the adsorption of bovine serum albumin (BSA) on an anion-exchange column packing when using reasonable physical properties. The new model was also used to develop an improved theoretical criterion for determining the conditions required for an adsorbed species to displace a protein in displacement chromatography when the pH is near the protein pI.     

Steric mass-action model for dye-ligand affinity adsorption of protein

The steric mass-action (SMA) model has been reported in the literature for ion-exchange and metal-affinity interaction adsorption equilibrium of proteins. In this work, an SMA model was developed for protein adsorption equilibrium to dye-ligand affinity adsorbent, Cibacron Blue-modified Sepharose CL-6B (CB-Sepharose). Static adsorption experiments with bovine serum albumin as a model protein were carried out to determine the model parameters, that is, equilibrium constant (K), characteristic number of binding sites (n), and steric factor (sigma). It was found that the linear model parameters, K and n decreased with the increase of ionic strength, while the nonlinear parameter, sigma, increased with ionic strength and the dye-ligand concentration. Thus, expressions correlating these parameters with the dye-ligand concentration and/or ionic strength were derived. With these correlations, the SMA model gave promising results in predicting protein adsorption isotherms. Thus, it is considered that the model would be useful in the theoretical analysis of dye-ligand affinity chromatography.     

Modeling of the salt effects on hydrophobic adsorption equilibrium of protein

A two-state protein model is proposed to describe the salt effects on protein adsorption equilibrium on hydrophobic media. This model assumes that protein molecules exist in two equilibrium states in a salt solution, that is, hydrated and dehydrated states, and only the dehydrated-state protein can bind to hydrophobic ligands. In terms of the two-state protein hypothesis and the steric mass-action theory, protein adsorption equilibrium on hydrophobic media is formulated by a five-parameter equation. The model is demonstrated with the adsorption of bovine serum albumin to Phenyl Sepharose gels as a model system. The effects of salt type (sodium chloride, sodium sulfate and ammonium sulfate) on the model parameters are discussed. Then, the model formulism is simplified in terms of the small magnitude of the protein dehydration equilibrium constant in the model. This simplification has returned the model derived on the basis of the two-state protein hypothesis to its original mechanism of salt effects on the hydrophobic adsorption of protein. This simplified model also creates satisfactory prediction of protein adsorption isotherms.     

Adsorption equilibrium of fructosyltransferase on a weak anion-exchange resin

The adsorption equilibrium of a glycoprotein, fructosyltransferase from Aureobasidium pullulans, on an anion-exchange resin, Sepabeads FP-DA activated with 0.1M NaOH, was investigated. The adsorption isotherms were determined at 20 degrees C in a phosphate-citrate buffer with pH 6.0 using the static method. Sodium chloride was used to adjust the ionic strength in the range from 0.0215 to 0.1215 mol dm(-3) which provided conditions varying from a weak effect of salt concentration on protein binding to its strong suppression. The equilibrium data were very well fitted by means of the steric mass-action model when the ion-exchange capacity of 290 mmol dm(-3) was obtained from independent frontal column experiments. The model fit provided the protein characteristic charge equal to 1.9, equilibrium constant 0.326, and steric factor 1.095 x 10(5).     

基于光波导分光光谱技术研究蛋白质与亚甲基蓝的竞争吸附行为

通过利用时间分辨光波导分光光谱技术原位测量从蛋白质-亚甲基蓝(MB)混合水溶液吸附到亲水玻璃光波导表面的MB可见光吸收谱,观测到在溶液pH值低于蛋白质等电点时MB与牛血清蛋白(BSA)以及MB与血红蛋白(Hb)存在竞争吸附行为,进一步测得这种竞争吸附行为对蛋白质浓度十分敏感,可以用于简单测定溶液中的蛋白质含量.基于Langmuir等温吸附理论推导出了两种分子竞争吸附的动力学方程,并利用该动力学方程对实验测得的吸光度随时间变化曲线进行了最佳拟合,揭示了玻璃表面吸附的MB分子个数在达到最大值后随时间呈指数衰减,同时得出拟合参数与蛋白质浓度呈准线性关系.     

3-氨基苯硼酸为功能单体在壳聚糖上印迹牛血清白蛋白的研究

以壳聚糖为载体, 3-氨基苯硼酸为功能单体对牛血清白蛋白进行了分子印迹的研究, 并对吸附过程进行Langmuir等温吸附模型的数据处理. 结果表明, 印迹聚合物上形成了对于模板分子有较高的吸附容量和选择性的识别位点, Langmuir等温吸附平衡常数为49.5 mL/mg, 结合位点的最大表观结合量为16.3 mg/g, 证明了该印迹聚合物对于牛血红蛋白和溶菌酶这些非模板蛋白的吸附不具有选择性.     

Preparation of Functional Fluorescent Microspheres Used for HTS and Their Interaction with Biomolecules

There is considerable interest in protein adsorption onto microspheres because of its importance in a wide range of biomedical applications, such as artificial tissues and organs, drug delivery systems, biosensors, solid-phase immunoassays, immunomagnetic cell separation and immobilized enzymes or catalyst. It has been well known that the interaction between proteins and microspheres plays important roles in this process. Major interaction involved in the adsorption can be classified as electrostatic, hydrophobic and hydrogen-bonding. Indeed, adsorption of proteins onto microspheres is a complex process and often can involve many dynamic steps, from the initial attachment of the protein on the surface of microspheres to the equilibrium. Also the conformation of proteins probably occurs to a certain degree of deformation or structural change due to the large area of contact. Recently, much interest has been shown in sulfonated microspheres, since sulfonate-group itself is one of components in bio-bodies, as well as is sensitive to the change of pH or ionic strength. Indeed, so far, scanty investigations have been performed in the full range. Also few researches have involved the data on adsorption rate and the maximum amount of protein adsorbed, or the reversibility of the process and conformational change of protein adsorbed as well.In present study, BSA (bovine serum albumin) was chosen as the model protein and sulfonated PMMA [poly(methyl methacrylate)] microspheres as the matrix to investigate the adsorption process.The purpose is to show some information especially the intrinsic information involved by the adsorption process Adsorption of BSA onto sulfonated microspheres (MS) has been investigated as a function of time, protein concentration and pH. The adsorption appears to be a reversible process and the presence of sulfonate groups can play important roles in the adsorption process, so as to increase the amount of protein adsorbed and influences the interaction of BSA molecules. Fig. 1 also shows that the reciprocation between unadsorbed and adsorbed BSA or rearrangement of adsorbed BSA molecules does not produce visible change in the properties of the adsorbed protein. Close to the isoelectric point of BSA (pI 4.7), the amount of protein adsorbed exhibits a maximum. A higher or lower pH results in the significant decrease of the adsorption amount. This is related to the dependence of BSA conformations at different pH conditions.     

Temperature-programmed desorption as a tool for quantification of protein adsorption capacity in micro- and nanoporous materials

The protein adsorption capacity of porous sorbents is generally obtained by measuring the concentration of proteins desorbed from the materials after treatment by a detergent, or by measuring the decrease of protein concentration in the solution. These methods have some drawbacks and often lead to a low precision in the determination of the adsorption capacities. We describe in this paper a new method that allows to directly quantify the amount of proteins adsorbed on porous materials. This method is based on the quantitative analysis by mass spectrometry of some low mass gaseous species which evolve from the biomolecules during the heat treatment of a temperature-programmed desorption analysis (TPD-MS). The method has been applied to bovine serum albumin and cytochrome C adsorbed on an activated carbon. The adsorption uptake of the proteins on the carbon material could be measured by this direct analysis. A comparison with the depletion method was done, it shows that the two methods are complementary. The depletion method allows a determination of the total adsorption capacity, while the TPD-MS method focus on irreversible capacity.     

Interaction of dissolved proteins with spherical polyelectrolyte brushes

We consider the adsorption of bovine serum albumin (BSA) on spherical polyelectrolyte brushes (SPB). The SPB consist of a solid polystyrene core of 100nm diameter onto which linear polyelectrolyte chains (poly(acrylic acid), (PAA)) are grafted. The adsorption of BSA is studied at a pH of 6.1 at different concentrations of added salt and buffer (MES). We observe strong adsorption of BSA onto the SPB despite the effect that the particles as well as the dissolved BSA are charged negatively. The adsorption of BSA is strongest at low salt concentration and decreases drastically with increasing amounts of added salt. The adsorbed protein can be washed out again by raising the ionic strength. The various driving forces for the adsorption are discussed. It is demonstrated that the main driving force is located in the electrostatic interaction of the protein with the brush layer of the particles. All data show that the SPB present a new class of carrier particles whose interaction with proteins can be tuned in a well-defined manner.     

Characterization of non-linear adsorption properties of dextran-based polyelectrolyte displacers in ion-exchange systems

Experimental studies were carried out on the non-linear adsorption properties of dextran-based polyelectrolytes in anion- and cation-exchange chromatographic systems. By monitoring both the induced salt gradients and sequential breakthrough fronts, parameters were determined for use in a Steric Mass Action (SMA) model of non-linear ion-exchange chromatography. These parameters include: total ion capacity of the columns, characteristic charge, steric factor, equilibrium constant, and maximum adsorptive capacity for each of the polyelectrolytes. In addition the number of functional groups were determined by elemental analysis. The values of the SMA parameters were found to be independent of salt and polyelectrolyte bulk phase compositions. Parameters were also determined for a variety of proteins. Experimental isotherms for the polyelectrolytes and proteins were compared with those simulated by the SMA model. Finally, the implications of polyelectrolyte adsorption properties with respect to their ability to act as efficient displacers in ion-exchange displacement systems are discussed.     

Protein adsorption behavior and immunoglobulin separation with a mixed‐mode resin based on p‐aminohippuric acid

p‐Aminohippuric acid is a newly developed ligand for mixed‐mode chromatography with a commercial resin name of Nuvia cPrime. In this study, bovine immunoglobulin G and bovine serum albumin were used as two model proteins, and the adsorption isotherms with Nuvia cPrime were investigated under different pH and salt concentrations. The results showed that pH had a strong but different influence on the adsorption of these two proteins. The adsorption capacity for bovine immunoglobulin G and BSA was 170.4 and 28.1 mg/g at pH 6.0, respectively. Different salts also showed varying effects on the protein adsorption. Moreover, the adsorption and elution behaviors of the two proteins in a column were determined under varying pH and salt concentrations. An optimized process showed that feedstock loaded under pH 6.0 with 0.8 M (NH₄)₂SO₄ and eluted under pH 8.0 with 1.0 M NaCl could effectively purify bovine immunoglobulin G from feedstock containing BSA. The purity of bovine immunoglobulin G could reach 99.8% and the recovery was 92.7%. The results demonstrated that the control of pH and salt addition during the loading and elution processes were two key factors in improving separation efficiency with Nuvia cPrime resin.     

Protein interactions with negatively charged inorganic surfaces

Protein adsorption on charged inorganic solid materials has recently attracted enormous interest owing to its various possible applications, including drug delivery and biomaterial design. The need to combine experimental and computational approaches to get a detailed picture of the adsorbed protein properties is increasingly recognised and emphasised in this review. We discuss the methods frequently used to study protein adsorption and the information they can provide. We focus on model systems containing a silica surface, which is negatively charged and hydrophilic at physiological pH, and two contrasting proteins: bovine serum albumin (BSA) and lysozyme (LSZ) that are both water soluble. At pH 7, BSA has a net negative charge, whereas LSZ is positive. In addition, BSA is moderately sized and flexible, whereas LSZ is small and relatively rigid. These differences in charge and structural nature capture the role of electrostatics and hydrophobic interactions on the adsorption of these proteins, along with the impact of adsorption on protein orientation and function. Understanding these model systems will undoubtedly enhance the potential to extrapolate our knowledge to other systems of interest.     

Adsorption of BSA on the amphiphilic PEG graft copolymer-coated particles

The amphiphilic copolymers comprising several monomethoxy poly(ethylene glycol) (mPEG) and lauryl side chains were prepared and coated on the polystyrene (PS) particles to study the interactions between these particles and bovine serum albumin (BSA). The surface mPEG density and mPEG chain length were the primary parameters of interest. A significant fraction of the graft copolymer was washed away from the particle surface during five cycles of centrifugation-dispersion treatment, especially for the one with the smallest number of lauryl side chains. At pH 5, the BSA adsorption data did not follow the Langmuir isotherm model for the graft copolymer-modified particles. This was attributed to the presence of a surface mPEG layer that severely retarded the approach of BSA to the particle. The amount of the adsorbed BSA decreased with increasing the surface mPEG density. A mechanistic model was proposed to qualitatively describe the adsorption of BSA on the mPEG-containing particles and the native particles as well.     

Preparation of composite monoliths of quaternized chitosan and diatom earth for protein separation

In this study, composite monoliths with porous structures were prepared using quaternized chitosan and diatom earth for protein separation. Quaternized chitosan (N-[(2-hydroxy-3-trimethylammonium)propyl] chitosan chloride) dissolved in water was mixed with diatom earth and crosslinked with glutaraldehyde under low-temperature conditions to form a cryogel. Interconnected porous monoliths were obtained after removing ice crystals from the cryogel. The monoliths adsorbed bovine serum albumin selectively from the solution mixture of bovine serum albumin and bovine ɤ-globulin, and bovine ɤ-globulin was recovered in the flow-through fraction. The adsorption selectivity was enhanced by changing the solution pH from 6.8 to 5.5. The adsorption of bovine serum albumin by the monolith was replicated at least five times following its washing with a buffer containing 400 mM NaCl and subsequent regeneration with a 10 mM acetate buffer. The composited monolith is a promising adsorbent for the removal of acidic proteins, such as serum albumin contamination in neutral proteins, for example, ɤ-globulins, in bioproduction processes.     

羟基磷灰石对牛血清白蛋白的吸附特性研究

研究了羟基磷灰石表面电位随溶液PO₄^3-浓度、Ca²⁺浓度、离子强度和pH的变化规律;测定了不同操作条件下牛血清白蛋白在羟基磷灰石上的吸附容量;吸附等温线的测定结果表明该吸附属于Langmuir型;通过对该吸附过程的动力学研究,计算得到的表观活化能和吸附热数值较低,表明该吸附是物理吸附.     

Effects of ligand density and pore size on the adsorption of bovine IgG with DEAE ion-exchange resins

Immunoglobulin G is an important plasma protein with many applications in therapeutics and diagnostics, which can be purified effectively by ion exchange chromatography. The ligand densities and pore properties of ion-exchange resins have significant effects on the separation behaviors of protein, however, the understandings are quite limited. In this work, with bovine immunoglobulin as the model IgG, the adsorption isotherms and adsorption kinetics were investigated systematically with series of diethylaminoethyl ion-exchange resins with different ligand densities and pore sizes. The Langmuir equation and pore diffusion model were used to fit the experimental data. The influences of ligand density and pore size on the saturated adsorption capacity, the dissociation constant and the effective diffusivity were discussed. The adsorption capacities increased with the increase of ligand density and the decrease of pore size, and an integrative parameter was proposed to describe the combined effects of ligand density and pore size. It was also found that the effective pore diffusion coefficient of the adsorption kinetics was influenced by pore sizes of resins, but was relatively independent on the ligand densities of resins. For a given protein, the ligand density and pore size should be optimized for improving the protein adsorption.     

Flow microcalorimetric measurements for bovine serum albumin on reversed-phase and anion-exchange supports under overloaded conditions

Heat of adsorption data using flow microcalorimetry is reported for the adsorption of bovine serum albumin (BSA) on C18 and C4 chromatographic supports. Exothermic heats were obtained in all cases. Data for the effect of salt indicate that conformational changes in adsorbed protein appear to be greatest in the absence of salt. Also, the specific surface area of the support was found to influence behavior more strongly than the length of the carbon ligand. Heats of adsorption of BSA on an ion-exchange support were also measured. Endothermic heats were obtained in all cases. The data indicate that the observed heat effects may be strongly influenced by the release of water from the surface.     

疏水界面上标准蛋白质吸附等温线的研究

测定了几种具有代表性的标准蛋白质在疏水色谱填料上的吸附等温线.除溶菌酶和牛血清白蛋白的吸附近似呈线性外,细胞色素-c、肌红蛋白、胰岛素、α-淀粉酶和卵清蛋白均呈凸型吸附.用Langmuir、计量置换吸附模型(SDM-A)、BET和Jovanovic吸附模型对这些蛋白的吸附等温线拟合后发现,SDM-A关系式能够良好描述这7种蛋白的吸附,Langmuir关系仅能较好地描述后5种蛋白质的吸附.而Jovanovic和BET关系式对上述两类蛋白质吸附的描述欠妥.实验发现对于不同盐浓度条件下卵清蛋白的吸附,用SDM-A和Langmuir公式拟合所得的参数与盐浓度之间呈现出一定的规律性.