The effective and specific isolation of antibodies from human serum by using thiophilic paramagnetic polymer beads

A rapid and effective method to specifically isolate immunoglobulin G (IgG) from human serum by thiophilic paramagnetic polymer beads was developed. The thiophilic paramagnetic beads were synthesized with vinyl acetate and divinylbenzene by microsuspension polymerization in the presence of magnetite nanoparticles. Divinylsulfone and 2-mercapto-benzothiazole were subsequently used to modify the surface of these beads, resulting in thiophilic particles that exhibited a high specificity to the antibodies in serum at low salt concentration. The adsorbed IgG was eluted by 0.8 M KCl and 72% of the IgG in the serum was recovered. The purity of the isolated IgG reached 98.4% and the bioactivity was fully maintained (>99%). The high efficiency, mild conditions and simplicity make this technology suitable for the economic purification of antibodies in a large scale.     

Preparation and Characterization of PEGylated Thiophilic Nanoparticles for Rapid Antibody Separation

Magnetic nanoparticles with novel core-shell structure were prepared for immunoglobulin (IgG) separation, in which thiophilic property of sulfone groups and protein resistance of poly(ethylene glycol) (PEG) moieties were integrated. The step-wise surface reactions on the nanoparticles were characterized by ¹H nuclear magnetic resonance (NMR) and surface zeta potential measurements. With human IgG and bovine serum albumin (BSA) as model proteins, the effects of PEG chain length, conjugation group, solution pH and salt concentration on IgG selectivity were investigated using static adsorption experiments. The experiment results showed that mPEG2000-NH₂ modified magnetic nanoparticles had an adsorption capacity of 132.8 mg g^?1 and selectivity of 32.5 towards IgG under the condition of pH 7.45 and 0.15 M NaCl. In complex biological fluids, the PEG modified magnetic nanoparticles could separate IgG from fetal calf serum and Omalizumab from cell culture supernatant with purities of 96% and 99%, respectively. Moreover, the binding affinities of the proposed core-shell structure towards IgG from four animal species (human, bovine, rabbit and goat) were quantified by bio-layer interferometer (BLI). The results showed that the selectivity of this structure towards IgG varied from traditional Protein A method, suggesting its potentials in rapid separation and purification of IgG with low affinity towards Protein A.     

New Thiophilic Adsorbent for the Purification of Insulin and Immunoglobulins G

We have synthesized new supports for the purification of insulin and IgG by affinity chromatography. These supports combine the advantages of biospecific ligands with the excellent separation properties of thiophilic sorbents. The existence of N-acetyl-neuraminic acid in insulin receptor and in the antigenic determinant of IgG suggests that such an acid may develop specific interactions usable in affinity chromatography. Therefore, N-acetylneuraminic acid was used as an active ligand in comparison with the β-mercaptoethanol. The performances of these supports were tested under static and dynamic (LC) conditions. The support functionalized by sialic acid appears significantly more selective than the support grafted by β-mercaptoethanol; and its purification yield is better. This new support showed similar adsorption characteristics with thiophilic adsorbent. These affinity supports allowed a one-step separation of the insulin and IgG subclasses from a pancreatic extract and mouse ascitic fluids, respectively, by LC.     

嗜硫类磁性聚合物微球高效分离抗体

用微悬浮聚合技术制备微米级顺磁性的聚合物微球,并通过水解反应在其表面生成丰富的羟基,进而通过二乙烯基砜活化,在其表面修饰2-巯基嘧啶,实现磁性微球对人体免疫球蛋白G(IgG)的特异性识别.进一步探讨了不同解吸附环境,如pH值、温度、离子种类、离子强度等条件,对这种特异性吸附行为的影响.采用此磁性分离技术后,分离抗体的纯度超过92%,抗体活性高于99%.通过连续分离工艺,IgG的分离效率达到86.8%.     

磁性壳聚糖微球的制备及对Cr(Ⅵ)的吸附性能研究

用壳聚糖包埋磁流体,用戊二醛交联制成磁性壳聚糖微球,并用红外光谱表征其结构。用制备的磁性壳聚糖微球吸附Cr(Ⅵ)离子,考察了其对Cr(Ⅵ)离子的吸附性能;探讨了吸附时间、溶液pH值、吸附剂用量、温度、Cr(Ⅵ)起始浓度以及其他离子存在对Cr(Ⅵ)离子去除率的影响。实验结果表明,磁性壳聚糖微球吸附Cr(Ⅵ)离子的最佳条件为:吸附平衡时间40 min,最佳吸附pH值6左右,磁性壳聚糖微球用量10 mg,温度升高有利于提高磁性壳聚糖微球的吸附效率,Cr(Ⅵ)离子起始质量浓度为12μg/mL,无机盐的存在引起磁性壳聚糖微球的吸附性能降低。并且考察了吸附剂的再生性能,实验结果表明磁性壳聚糖微球具有良好的重复使用性。     

Salt promoted adsorption chromatography of malted barley amylases

Summary A sequence for the fractionation of the amylasic components from a malted barley extract is proposed using two salt-promoted, adsorption processes: thiophilic interaction chromatography (TIC) and hydrophobic interaction chromatography (HIC).Two fractions containing -amylase activity were recovered during the thiophilic chromatography; the first was resolved in to -amylase I and -amylase I by HIC on a phenyl-sepharose column; an enrichment factor of 32 was achieved for -amylase I. The other amylasic component eluted from the thiophilic gel was characterized as -amylase II. Although the adsorption of malt amylases on phenylsepharose and the thiophilic adsorbent is salt promoted, the interactions involved in each case are clearly distinguished by the different behaviour and disparate salt effects.     

Removal and recovery of Zn2+ and Pb2+ by imine-functionalized magnetic nanoparticles with tunable selectivity

This research investigated the adsorption of zinc and lead from binary metal solution with tunable selectivity. A nano adsorbent was prepared by introducing imine groups onto the surface of stability enhanced magnetic nanoparticles and then characterized by TEM and FTIR. Binary metal components adsorption was carried out in different concentration of metal and EDTA solution. Due to the interaction between metals and adsorbent in the presence of EDTA, the selective adsorption of zinc and lead could be achieved with 100% selectivity. To only remove zinc from binary metals, the solution condition was [EDTA]/[M(2+)] = 0.7 with pH of 6, and its saturated adsorption capacity was 1.25 mmol/g. For selective adsorption of lead, an equilibrium adsorption capacity of 0.81 mmol/g was obtained under the condition of [EDTA]/[M(2+)] = 0.7 and pH of 2. The exhausted adsorbent could be regenerated by simple acid or alkali wash, and high purity lead and zinc salt solutions were recovered and concentrated.     

Preparation of a magnetic porous carbon with hierarchical structures from waste biomass for the extraction of some carbamates

In this study, corn stalk was used to synthesize a magnetic adsorbent by pyrolysis together with KHCO₃ as the chemical activator and iron(III) salt as the magnetic reagent. The characterization by scanning electron microscopy, transmission electron microscopy and N₂ adsorption–desorption analysis showed that the magnetic carbon adsorbent had a structure of hierarchical pores with a high specific surface area. To evaluate its adsorption performance, the adsorbent was used for the extraction of carbamates pesticides (propoxur, isoprocarb and fenobucarb) from water and zucchini samples before high‐performance liquid chromatography analysis. The result showed that the adsorbent had a good adsorption capability for the analytes. Under the optimized conditions, a good linearity for the analytes existed in the range of 0.1–100.0 ng/mL for water samples and 0.5–100.0 ng/g for zucchini samples with the correlation coefficients of 0.9992–0.9998. The limits of detection for the analytes at a signal to noise ratio of 3 were 0.03 ng/mL for water samples and 0.20–0.50 ng/g for zucchini samples.     

Optimization of cadmium adsorption from aqueous solutions by functionalized graphene and the reversible magnetic recovery of the adsorbent using response surface methodology

Novel functionalized graphene adsorbent was prepared and characterized using different techniques. The prepared adsorbent was applied for the removal of cadmium ions from aqueous solution. A response surface methodology was used to evaluate the simple and combined effects of the various parameters, including adsorbent dosage, pH, and initial concentration. Under the optimal conditions, the cadmium removal performance of 70% was achieved. A good agreement between experimental and predicted data in this study was observed. The experimental results revealed of cadmium adsorption with high linearity follow Langmuir isotherm model with maximum adsorption capacity of 502 mg g^?1, and the adsorption data fitted well into pseudo‐second order model. Thermodynamic studies showed that adsorption process has exothermic and spontaneous nature. The recommended optimum conditions are: cadmium concentration of 970 mg L^?1, adsorbent dosage of 1 g L^?1, pH of 6.18, and T = 25 °C. The magnetic recovery of the adsorbent was performed using a magnetic surfactant to form a noncovalent magnetic functionalized graphene. After magnetic recovery of the adsorbent both components (adsorbent and magnetic surfactant) were recycled by tuning the surface charges through changing the pH of the solution. Desorption behavior studied using HNO₃ solution indicated that the adsorbent had the potential for reusability.     

Comparison of the protein adsorption selectivity of salt-promoted agarose-based adsorbents: Hydrophobic, thiophilic and electron donor–acceptor adsorbents

Protein adsorption of human serum onto six different agarose-based chromatographic gels that were representative of the salt-promoted adsorbent family [octyl- and phenyl-Sepharose, mercaptoethanol–divinyl sulfone agarose (T gel), mercaptomethylene pyridine-derivatized agarose gel (MP gel), tricyanoaminopropene–divinyl sulfone agarose (DVS–TCP gel), tricyanoamino-propene–bisoxirane agarose (bisoxirane–TCP gel)] was studied in the presence of moderate or high concentrations of the water structuring salt, sodium sulfate. Study of the protein adsorption selectivity by two-dimensional gel electrophoresis revealed an opposed selectivity for hydrophobic interaction adsorbents and electron donor–acceptor adsorbents. The T gel, MP gel and TCP gels belonged to the electron donor–acceptor adsorbents, displaying a main selectivity for immunoglobulins, whereas octyl-Sepharose belonged to the hydrophobic adsorbents, displaying a main selectivity for ‘hydrophobic' proteins. Phenyl-Sepharose for its part was described as an example of a composite selectivity of both families. The conclusion of this work is two-fold: (1) hydrophobic interaction chromatography (HIC) and electron donor–acceptor chromatography (EDAC) have opposed protein selectivities and are both salt-promoted. As a main consequence, it means that high concentrations of a water-structuring salt can promote different types of weak molecular interactions, resulting in different protein adsorption selectivities: (2) thiophilic adsorption chromatography (TAC) should be renamed EDAC as similar protein selectivity is demonstrated for electron donor–acceptor ligand devoid of sulfur atoms.     

N-去甲万古霉素亲和吸附剂的合成及性能

将N,N二甲基丙烯酰胺N,N′乙撑双丙烯酰胺共聚物部分水解,在共聚物中引入适量的羧基.含羧基的聚合物与氨基酸甲酯缩合,然后使酯基皂化,将氨基酸引入聚合物.将革兰氏阳性菌细胞壁粘肽的三种类似物(-Gly,-Gly-DAla,-Gly-DAla-DAla)分别引入上述聚合物,合成了3种万古霉素系列抗菌素的亲和吸附剂(Ⅰ,Ⅱ和Ⅲ).结果表明,吸附剂Ⅱ和吸附剂Ⅲ对N去甲万古霉素的吸附量分别为0.80和0.86mmol/g;最佳吸附pH值为6左右;吸附剂Ⅰ的吸附量随着吸附液中盐浓度的增加而显著降低,而吸附液中盐浓度对吸附剂Ⅱ的吸附量影响较小.说明亲和作用在吸附剂Ⅱ的吸附中贡献较大.用0.4mol/LNa₂CO₃(pH9.5)/CH₃CN(体积比为7/3)作为洗脱剂可完全脱附被吸附的N去甲万古霉素.     

Cascade-mode multiaffinity chromatography. Fractionation of human serum proteins.

The group-resolving power of cascade-mode multiaffinity column chromatography (CASMAC), was demonstrated with human serum as a model mixture. More than 99% of the serum proteins were adsorbed in the same high salt-containing buffer on a tandem column consisting of (1) immobilized Zn2+ on triscarboxymethyl diamine gel followed by (2) thiophilic (T) gel, (3) Zn2+ bound to the new tridentate chelating adsorbent dipicolylamine (DPA) agarose, (4) hexyl-thioether C6-S agarose and (5) Ni(2+)-DPA agarose. After the adsorption step the immobilized metal ion affinity gels were attached to the top of tandem columns of other adsorbents (T gel, Sephadex G-25 for desalting and Mono-Q) and the elution conditions were selected such that further group separation was achieved. High resolution, high recovery, easy manipulation and high capacity are characteristic features of the cascade process with these adsorbents. The advantage of CASMAC is particularly striking when, with a given number of adsorbents, the overall number of operations involving adsorption, desorption, washing, buffer change and substance concentration can be effectively minimized.     

On the theory of polyelectrolyte adsorption : The effect on adsorption behavior of the electrostatic contribution to the adsorption free energy

A theory has been developed for the adsorption of polyelectrolytes on charged interfaces from an aqueous salt solution. This adsorption is determined by the electrical charge density of the polyelectrolyte, the adsorption energy, the salt concentration, the molecular weight, solubility, flexibility, and concentration of polymer. The theory relates these parameters to the properties of the adsorbed polymer layer, i.e., the amount of polymer adsorbed, the fraction of the adsorbent interface covered, the fraction of the segments actually adsorbed on the interface versus the fraction of the segments in the dangling loops, the final surface charge density, and the thickness of the adsorbed layer. As polyelectrolyte adsorption should resemble nonionic polymer adsorption at high ionic strength of the solution or low charge density on the polymer, this work is an extension of the nonionic polymer adsorption theory to polyelectrolyte adsorption. The following effects are taken into account: (a) the conformational change upon adsorption of a coil in solution into a sequence of adsorbed trains interconnected by loops dangling in solution; (b) the interactions of the adsorbed trains with the interface and with each other; (c) the interaction of the dangling loops with the solvent; (d) the change in surface charge density of the adsorbent due to adsorption of charged trains and the accompanying changes in the electrical double layer which contains “small” ions as well as charged loops; (e) the (induced) dipole interaction of the adsorbed trains with the charged adsorbent interface. The theory is worked out for low potentials (Debye—Hückel approximation); in Appendix B an outline of a more complete treatment is given. The predicted adsorption isotherms have the experimentally observed high-affinity character. A relation between the adsorption energy, the surface charge density on the adsorbent, the degree of dissociation of the polymer, and the salt concentration predicts the conditions under which no adsorption will occur. For adsorbent and polymer carrying the same type of charge (both positive or both negative) the adsorption is predicted to decrease with increased charge density on polymer or adsorbent and to increase with salt concentration. If adsorbent and polymer carry different type charges, the adsorption as a function of the degree of dissociation, α, goes through a maximum at a relatively low value of α and, depending on the adsorption energy, an increase in the salt concentration can then increase or decrease the adsorption. At finite polymer concentration in solution the number of adsorbed segments and the fraction of the interface covered practically do not change with an increase in polymer concentration, whereas the total number of polymer molecules adsorbed increases slightly, as does the average fraction of segments in loops. The experimental results for polyelectrolyte adsorption have been reviewed in general and, as far as data are available, the predictions of the theory seem to follow the experimentally observed trends quite closely, except for the thickness of the adsorbed layer. This thickness is systematically overestimated by the theory and two reasons for this are given. The theoretical model implies a not too low ionic strength of the solution. Extrapolation of results to solutions of very low ionic strength is not warranted.     

Novel hydrophobic interaction chromatography matrix for specific isolation and simple elution of immunoglobulins (A, G, and M) from porcine serum

A new, highly acetylated agarose matrix (HA-Sepharose) was synthesized and used as a hydrophobic interaction chromatography (HIC) medium to specifically isolate immunoglobulins (Igs) from porcine serum. Recovery of Igs was in a single step and under mild conditions. HA-Sepharose adsorption was studied in terms of salt, gel acetylation time, flow rate, and protein concentration on the loading buffer. At 0.5 M Na2SO4, control with unmodified Sepharose retained a small fraction (0.70 mg/mL of matrix) of serum albumin. On the contrary HA-Sepharose retained primary Igs (IgA, IgG, and 53% of IgM) as revealed by sodium dodecyl sulphate 10% polyacrylamide gel electrophoresis (SDS-PAGE), quantitative radial immunodiffusion and immunodetection. At a flow rate of 1 mL/min, the HA-Sepharose column capacity (3.9 mg/mL of matrix) was similar to the reported capacity for the commercial thiophilic T-gel. However, HA-Sepharose showed higher recovery of IgA and IgM than the T-gel in the same salt conditions, clearly an advantage in terms of immunoglobulin recovery strategies. Acetylation changed the matrix adsorption from albumin to immunoglobulins; thus, the highly acetylated gel rendered recoveries of Igs from unprocessed porcine serum practically free of albumin.     

DNA binding during expanded bed adsorption and factors affecting adsorbent aggregation

DNA-induced aggregation and contraction of expanded bed adsorption chromatography beds have been examined using strong anion exchanger Q HyperZ and calf thymus DNA in buffers containing added NaCl. Two batches of adsorbent with different ionic capacities were used allowing the effects of different ligand densities to be examined. Very high dynamic binding capacities at 10% breakthrough were found in the absence of added salt. However, the highest binding capacities ( approximately 10 and approximately 19mgDNAml(-1) gel) were found in buffers containing added salt at concentrations of either 0.25 or 0.35M, for the low and high ligand density adsorbents, respectively. Bed contraction was observed, but did not correlate with dynamic binding capacity or with the amount of DNA loaded. No differences in bed contraction were seen by varying the concentration of DNA loaded in the range of 20-80mugml(-1) even though the dynamic binding capacity was reduced as DNA concentration was increased. The extent of bed contraction during DNA loading was found to be a function of added salt concentration and ligand density of the adsorbent. The results imply that ligand density significantly affects the salt tolerance of anion exchangers when binding DNA. However, more importantly, with the adsorbents examined here, attempts to reduce bed aggregation by feedstock conditioning with added salt may increase DNA binding leading to a reduction in expanded bed adsorption performance compromising protein capture in real feedstocks.     

Protein adsorption and transport in agarose and dextran-grafted agarose media for ion exchange chromatography: Effect of ionic strength and protein characteristics

This work investigates the effects of ionic strength and protein characteristics on adsorption and transport of lysozyme, BSA, and IgG in agarose-based cation exchangers with short ligand chemistry and with charged dextran grafts. In all cases, the adsorption equilibrium capacity decreased with increasing salt. However, the adsorption kinetics was strongly influenced by the adsorbent structure and protein characteristics. For the smaller and positively charged lysozyme, the effective pore diffusivity was only weakly dependent on salt for the dextran-free media, but declined sharply with salt for the dextran-grafted materials. For this protein, the dextran grafts enhanced the adsorption kinetics at low salt, but the enhancement vanished at higher salt concentrations. For BSA, which was near its isoelectric point for the experimental conditions studied, the effective diffusivity was low for all materials and almost independent of salt. Finally, for the larger and positively charged IgG, the effective diffusivity varied with salt, reaching an apparent maximum at intermediate concentrations for both dextran-free and dextran-grafted media with the kinetics substantially enhanced by the dextran grafts for these conditions. Microscopic observations of the particles during protein adsorption at low ionic strengths showed transient patterns characterized by sharp adsorption fronts for all materials. A theory taking into account surface or adsorbed phase diffusion with electrostatic coupling of diffusion fluxes is introduced to explain the mechanism for the enhanced adsorption kinetics observed for the positively charged proteins.     

High-throughput isotherm determination and thermodynamic modeling of protein adsorption on mixed mode adsorbents

The thermodynamic modeling of protein adsorption on mixed-mode adsorbents functionalized with ligands carrying both hydrophobic and electrostatic groups was undertaken. The developed mixed mode isotherm was fitted with protein adsorption data obtained for five different proteins on four different mixed mode adsorbents by 96-well microtitre plate high throughput batch experiments on a robotic workstation. The developed mixed mode isotherm was capable of describing the adsorption isotherms of all five proteins (having widely different molecular masses and iso-electric points) on the four mixed mode adsorbents and over a wide range of salt concentrations and solution pH, and provided a unique set of physically meaningful parameters for each resin-protein-pH combination. The model could capture the typically observed minimum in mixed mode protein adsorption and predict the precise salt concentration at which this minimum occurs. The possibility of predicting the salt concentration at which minimum protein binding occurs presents new opportunities for designing better elution strategies in mixed mode protein chromatography. Salt-protein interactions were shown to have important consequences on mixed mode protein adsorption when they occur. Finally, the mixed mode isotherm also gave very good fit with literature data of BSA adsorption on a different mixed mode adsorbent not examined in this study. Hence, the mixed mode isotherm formalism presented in this study can be used with any mixed mode adsorbent having the hydrophobic and electrostatic functional groups. It also provides the basis for detailed modeling and optimization of mixed mode chromatographic separation of proteins.     

电导法研究树脂与游离酸的相互作用

利用电导实验技术跟踪树脂吸附游离酸的行为 ,讨论了外加盐和乙醇等因素对吸附的影响 ,利用固 -液相互作用方程求取吸附剂 -吸附质相互作用能。实验结果表明 ,树脂吸附游离酸 ,其表观吸附速率常数随着外加盐离子浓度的增大而减少 ;表观吸附速率常数与吸附剂 -吸附质相互作用能存在线性关系。     

Residue valorization: Preparation of recyclable organic amine adsorbent using laterite residue

This study focuses on exploiting the main component of traditional nickel metallurgical waste for use as a valuable material that can be applied in the removal of organic amines from water systems. Silicon compounds from metallurgic waste were converted into dissolvable sodium silicate by roasting the waste with alkali. Silica with adsorption capacity was combined with magnetic NiFe cores by the carbonation decomposition of purified silicate solution. The composite magnetic adsorbent was characterized, and its adsorption mechanism for organic amines was investigated. The effects of the initial trimethylamine concentration, contact time and temperature on the adsorption efficiency of the composite adsorbent towards trimethylamine were investigated. It was found that the adsorption fit the Freundlich mode well. The adsorption kinetics can be described by a pseudo-second-order kinetic model. The adsorption capacity reached 55.8 μg/mg at 293 K. The use of metallurgical waste to prepare the magnetic composite adsorbent has three advantages, which include benefiting the environment by reducing the amount of solid waste and costs associated with constructing and maintaining storage facilities, generating valuable products in an economical manner and conveniently recycling used adsorbents to avoid secondary pollution.     

麦壳对水溶液中铜离子的动态吸附研究

对麦壳柱吸附铜离子的动态实验进行了研究。pH为5时有利于吸附,Na+和Ca2+的存在不利于吸附,说明在吸附过程中存在离子交换机理。溶液流速、溶液浓度对流出曲线有较大的影响。吸附后的麦壳用0.5mol/L盐酸再生,能重复使用。对不同流速和不同浓度的流出曲线用Thomas和Yoon-Nelson线性模型进行了拟合,并预测了流出曲线。结果表明,饱和吸附量随着初始浓度的增大而增大,随流速的增加而减小;穿透时间随初始浓度和流速的增大均减小。在不同条件下的线性相关系数为0.920～0.948,说明Thomas和Yoon-Nelson模型都可用于描述穿透曲线。