Initial evaluation of protein A modified capillary‐channeled polymer fibers for the capture and recovery of immunoglobulin G

A novel protein A affinity chromatography stationary phase has been developed from polypropylene capillary‐channeled polymer fibers modified with a recombinant protein A ligand for the capture and recovery of immunoglobulin G (IgG) with high specificity and yield. An SPE micropipette tip format was employed so that solvent, protein, and antibody consumption was minimized. The adsorption modification of the fiber surfaces with protein A was evaluated as a function of feed concentration and volume. Optimal modification of the fiber surface with protein A yielded a 5.7 mg/mL (bed volume) ligand capacity with the modified fibers showing stability across numerous solvent environments. Performance was evaluated through exposure to human IgG and myoglobin, individually and as a mixture. Myoglobin was used as a surrogate for host cell proteins common to growth media. The efficacy of the selective binding to the ligand is demonstrated by the 2.9:1 (IgG/protein A) binding stoichiometry. Elution with 0.1 M acetic acid yielded an 89% recovery of the captured IgG based on absorption measurements of the collected eluents. Regeneration was possible with 10 mM NaOH. Protein A modified polypropylene capillary‐channeled polymer fibers show promising initial results as an affinity phase for efficient capture and purification of IgG.     

蛋白A高效亲和膜色谱法测定人血浆中免疫球蛋白G的含量

 研究了蛋白Ａ高效亲和膜色谱对水溶液及人血浆中人免疫球蛋白Ｇ（ＨＩｇＧ）的特异性吸附和定量测定。方法具有较高的精确度和较好的重复性：ＨＩｇＧ标样５次重复进样的相对标准偏差为１．５％，人血浆样品３次重复进样的相对标准偏差为３．６％；所测得的定量标定曲线的线性相关系数达到０．９９９３；不含己二胺间隔臂的亲和介质的非特异性吸附极低，基本检测不出来。快速实验中，一次分析可在０．５ｍｉｎ内完成。实验表明，利用所建立的方法对人血浆中的ＨＩｇＧ进行定量测定可以得到较为满意的结果。     

Selective Extraction and Quantitation of Polyoxyethylene Detergents and its Application in Protein Determination

Abstract

A simple, rapid and selective method for the nearly quantitative extraction of high amounts (10% w/v) of polyoxyethylene nonionic detergents like Triton X-100^R is presented based on solvent extraction with 1, 2-dichloroethane. Protein determination after extraction of protein containing solutions can be accomplished using the Bradford assay¹ or other standard methods. High protein recoveries can be obtained. The detergent analysis by HPLC using reversed-phases is not disturbed in the presence of proteins and therefore provides a fast and elegant method for the exact quantitation of nonionic detergents.     

Protein A tangential flow affinity membrane cartridge for extracorporeal immunoadsorption therapy.

Tangential flow affinity membrane cartridge (TFAMC) is a new model of immunoadsorption therapy for hemoperfusion. Recombinant Protein A was immobilized on the membrane cartridge through Schiff base formation for extracorporeal IgG and immune complex removal from blood. Flow characteristics, immunoadsorption capacity and biocompatibility of protein A TFAMC were studied. The results showed that the pressure drop increased with the increasing flow rate of water, plasma and blood, demonstrating reliable strength of membrane at high flow rate. The adsorption capacities of protein A TFAMC for IgG from human plasma and blood were measured. The cartridge with 139 mg protein A immobilized on the matrix (6 mg protein A/g dry matrix) adsorbed 553 mg IgG (23.8 mg IgG/g dry matrix) from human plasma and 499.4 mg IgG (21.5 mg IgG/g dry matrix) from human blood, respectively. The circulation time had a major influence on IgG adsorption capacity, but the flow rate had little influence. Experiments in vitro and in vivo confirmed that protein A TFAMC mainly adsorbed IgG and little of other plasma proteins, and that blood cell damage was negligible. The extracorporeal circulation system is safe and reliable.     

Purification of a human immunoglobulin G1 monoclonal antibody from transgenic tobacco using membrane chromatographic processes

Efficient purification of protein biopharmaceuticals from transgenic plants is a major challenge, primarily due to low target protein expression levels, and high impurity content in the feed streams. These challenges may be addressed by using membrane chromatography. This paper discusses the use of cation-exchange and Protein A affinity-based membrane chromatographic techniques, singly and in combination for the purification of an anti-Pseudomonas aerugenosa O6ad human IgG1 monoclonal antibody from transgenic tobacco. Protein A membrane chromatography on its own was unable to provide a pure product, mainly due to extensive non-specific binding of impurities. Moreover, the Protein A membrane showed severe fouling tendency and generated high back-pressure. With cation-exchange membrane chromatography, minimal membrane fouling and high permeability were observed but high purity could not be achieved using one-step. Therefore, by using a combination of the cation-exchange and Protein A membrane chromatography, in that order, both high purity and recovery were achieved with high permeability. The antibody purification method was first systematically optimized using a simulated feed solution. Anti-P. aeruginosa human IgG1 type monoclonal antibody was then purified from transgenic tobacco juice using this optimized method.     

Custom synthesis of molecular imprinted polymers for biotechnological application: Preparation of a polymer selective for tylosin

A molecularly imprinted polymer (MIP) selective for tylosin was designed and synthesised using a computational method (MIP “dialling”). In re-binding experiments the MIP demonstrated high affinity for tylosin in aqueous solutions and in organic solvents. The synthesised polymer was tested for re-binding with the template and related metabolites such as tylactone, narbomycin and picromycin. The HPLC analysis showed that the computationally designed polymer is specific and capable of separating the template from its structural analogues. The MIP was capable of recovering tylosin from broth samples. The polymer capacity for tylosin was estimated as 6.4 mg/g for MIP, which was suitable for practical application and tylosin recovery from broth samples. Among the advantages of this was the possibility to adsorb tylosin from a complex media with easy removal of oils and other impurities which are present in significant quantities, which can create problems for its chromatographic purification procedure. The MIP “dialling” procedure can have a general significance for the fast preparation of specific adsorbents for biotechnological applications.     

Application of conjoint liquid chromatography with monolithic disks for the simultaneous determination of immunoglobulin G and other proteins present in a cell culture medium

The aim of this study was to develop a chromatographic method, as a substitute for enzyme-linked immunosorbent assays, for the rapid and simultaneous detection of IgG, insulin, and transferrin present in a cell culture medium. Conjoint liquid chromatography (conjoint LC) using monolithic disks was applied for this purpose. An anion-exchange disk was combined with a Protein G affinity disk in a preparative HPLC system. IgG bound to the Protein G disk, whereas transferrin and insulin were captured on the quaternary ammonium (QA) disk. Using this method, it was possible to simultaneously determine the concentrations of IgG, transferrin, and insulin in the cell culture medium. Thus, conjoint LC could be used for the rapid and simultaneous detection of different proteins present in a cell culture medium.     

Highly selective in situ metal ion determination by hybrid electrochemical "adsorption-desorption" and colorimetric methods

A novel and facile hybrid analytical method coupling electrochemical “adsorption–desorption” and colorimetric analyses was developed to detect heavy metal ions in turbid water samples. The target metal ions were deposited onto an electrode inserted into the original sample, which was referred to as the “adsorption” process. After changing the medium, the concentrated target metal ions were dissolved in a new, clean buffer (blank buffer), which was referred to as the “desorption” process. The concentrations of the target metal ions were measured by colorimetric analyses after the addition of specific indicator amounts. We demonstrated the applicability of this method by detecting Cd²⁺, Pb²⁺ and Cu²⁺ with co-depositing Bi³⁺ on portable screen-printed electrodes (SPEs). A good correlation (correlation coefficient of R = 0.997) was observed between concentrations ranging from 1 to 200 μM and absorbance values. After the multiple “desorption” process, the even better detection limits as low as 10, 10 and 100 nM were achieved for Cd²⁺, Pb²⁺ and Cu²⁺, respectively. The practicality of this hybrid method was confirmed by the detection of Cd²⁺, Pb²⁺ and Cu²⁺ in wastewater samples, and these results were in agreement with inductively coupled plasma atomic emission spectroscopy (ICP-AES). Overall, this hybrid method provides a simple, selective and effective technique for environmental pollutant analyses.     

蛋白A连续床亲和毛细管色谱柱的制备及性能考察

人免疫球蛋白 G(HIg G)是一种重要的生物大分子 ,是人血浆中的主要成分之一 ,通常采用免疫学的方法测定 .蛋白 A(Protein A)与免疫球蛋白 (HIg G)的 Fc区之间具有很强的特异性亲和作用 ,因而固载蛋白 A的亲和介质可用于免疫球蛋白及单克隆抗体的分离、纯化和分析测定[1～ 3 ] .根据固定相存在形式的不同 ,毛细管色谱柱主要有开管、填充和连续床柱 3种方式 .连续床具有相比高、易制备 (一步合成 )、孔径易控制、不需烧塞子和易改性等优点 .连续床与其它常用的亲和介质 (如球型凝胶颗粒、灌流色谱基质 [4、 5] 、膜介质 [6,7] 等 )相比具…     

Probing protein interactions with hydrogen/deuterium exchange and mass spectrometry—A review

Assessing the functional outcome of protein interactions in structural terms is a goal of structural biology, however most techniques have a limited capacity for making structure–function determinations with both high resolution and high throughput. Mass spectrometry can be applied as a reader of protein chemistries in order to fill this void, and enable methodologies whereby protein structure–function determinations may be made on a proteome-wide level. Protein hydrogen/deuterium exchange (H/DX) offers a chemical labeling strategy suitable for tracking changes in “dynamic topography” and thus represents a powerful means of monitoring protein structure–function relationships. This review presents the exchange method in the context of interaction analysis. Applications involving interface detection, quantitation of binding, and conformational responses to ligation are discussed, and commentary on recent analytical developments is provided.     

Determination of monoclonal antibody production in cell culture using novel microfluidic and traditional assays

This study compares microfluidic technology (Protein 200 LabChip Assay kit, Agilent 2100 Bioanalyzer, referred to here as Protein 200) to the traditional approach for protein analysis, one-dimensional sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE), for the sizing and quantification of immunoglobulin G (IgG) in hybridoma cell cultures. Internal references differ between each method: purified IgG was used alone in SDS-PAGE while myosin (the upper marker) was added to each sample in Protein 200. The IgG used here were produced in cultures propagated in either a serum-free or a serum-containing medium. With serum-containing samples, there was a significant difference in the IgG concentrations (p < 0.05) between SDS-PAGE and Protein 200. The concentration determined by SDS-PAGE was significantly higher (> 30%) than by Protein 200 or by high-pressure liquid chromatography (HPLC) because the large amounts of serum albumin in the samples affect the accuracy of SDS-PAGE. Protein 200 can determine size similarly to SDS-PAGE in serum-free samples (standard error of the mean, SEM, < 1%, 95% confidence < +/-1%), unlike in serum-containing samples. The Protein 200 assay was more effective than the traditional one-dimensional SDS-PAGE in determining concentration and size of IgG in cell culture samples and it provided a miniaturized and convenient platform for rapid analysis.     

Depletion of high-abundance proteins from human plasma using a combination of an affinity and pseudo-affinity column

Human serum albumin (HSA) and immunoglobulin G (IgG) represent over 75% of all proteins present in human plasma. These high-abundance proteins prevent the detection of low-abundance proteins which are potential markers for various diseases. The depletion of HSA and IgG is therefore essential for further proteome analysis. In this paper we describe the optimization of conditions for selective depletion of HSA and IgG using affinity and pseudo-affinity chromatography. A BIA Separations CIM (convective interaction media) Protein G disk was applied for the removal of IgG and the Mimetic Blue SA A6XL stationary phase for the removal of HSA. The binding and the elution buffer for CIM Protein G disk were chosen on the basis of the peak shape. The dynamic binding capacity was determined. It was shown to be dependent on the buffer system used and independent of the flow rate and of the concentration of IgG. Beside the binding capacity for the IgG standard, the binding capacity was also determined for IgG in human plasma. The Mimetic Blue SA A6XL column was characterized using human plasma. The selectivity of the depletion was dependent on the amount of human plasma that was loaded on the column. After the conditions on both supports had been optimized, the Mimetic Blue SA A6XL stationary phase was combined with the CIM Protein G disk in order to simultaneously deplete samples of human plasma. A centrifuge spin column that enables the removal of IgG and HSA from 20 μL of human plasma was designed. The results of the depletion were examined using sodium dodecyl sulfate polyacrylamide gel electrophoresis and two-dimensional gel electrophoresis.     

Characterization of metal chelate methacrylate monolithic disk for purification of polyclonal and monoclonal immunoglobulin G

Dynamic binding capacity (DBC) of commercial metal-chelate methacrylate monolith-convective interaction media (CIM) was performed with commercial human immunoglobulin G (IgG) (Cohn fraction II, III). Monoliths are an attractive stationary phase for purification of large biomolecules because they exhibit very low back pressure even at high flow rates and flow-unaffected binding properties. Adsorption of IgG onto CIM-IDA disk immobilized with Cu²⁺, Ni²⁺ and Zn²⁺ were studied with Tris-acetate (TA), phosphate-acetate (PA) and MMA (MES, MOPS and acetate) buffer systems at different flow rates. Adsorption and elution of IgG varied with different buffers and adsorption of IgG was maximum with MMA buffer. Adsorption of human IgG from Cohn fractions (II, III) was high when Cu²⁺ was used as ligand. CIM-IDA disk showed dynamic binding capacity in the range of 14–16 mg/ml with Cu²⁺ and 7–9 mg/ml with Ni²⁺ for human IgG with MMA buffer. In the case of CIM-IDA-Zn²⁺ column, the binding capacity was only about 0.5 mg/ml of support. Different desorption strategies like lowering of pH and increasing of competitive agent were also studied to achieve maximum recovery. Chromatographic runs with human serum and mouse ascites fluid were also carried out with metal chelate methacrylate monolithic disk and the results indicate the potential of this technique for polyclonal human IgG and monoclonal IgG purification from complex biological samples.     

Accelerated purification process development of monoclonal antibodies for shortening time to clinic. Design and case study of chromatography processes

For accelerating the purification process development of human monoclonal antibodies (hmAbs) for pharmaceutical drugs, we designed a standardized method for setting the conditions of the purification process, which could be applied to hmAbs for the early phase of pharmaceutical development. The process includes three sequential chromatography steps: Protein A affinity chromatography (AFC), anion-exchange chromatography (AIEC) and cation-exchange chromatography (CIEC), and also includes a low pH virus inactivation step after the AFC step. We predicted the elution pH in the AFC and elution salt concentration in the CIEC from the amino acid sequences of hmAbs, as described in our previous paper. The mobile phase pH in AIEC and the pH for virus inactivation were also predicted based on the amino acid sequence of hmAb. As a case study, six hmAbs (two of IgG(1), two of IgG(2) and two of IgG(4)) were purified with the standardized method. The recovery, purity and clearance of impurities (DNA, host cell proteins (HCP), and Protein A) were examined. All the six hmAbs were purified with high recovery and high clearance of the impurities. Factors affecting the impurities level in the purified products are also discussed.     

Factorial screening of antibody purification processes using three chromatography steps without protein A

Protein A affinity chromatography is often employed as a capture step to meet the purity, yield, and throughput requirements for pharmaceutical antibody purification. However, a trade-off exists between step performance and price. Protein A resin removes 99.9% of feed stream impurities; however, its price is significantly greater than those of non-affinity media. With many therapeutic indications for antibodies requiring high doses and/or chronic administration, the consideration of process economics is critical. We have systematically evaluated the purification performance of cation-exchange, anion-exchange, hydroxyapatite, hydrophobic interaction, hydrophobic charge induction, and small-molecule ligand resins in each step of a three-step chromatographic purification process for a CHO-derived monoclonal antibody. Host cell proteins were removed to less-than-detectable for three processes (cation-exchange-anion-exchange-hydrophobic interaction chromatography, cation-exchange-anion-exchange-mixed cation-exchange chromatography, and cation-exchange-mixed cation-exchange-anion-exchange chromatography). The order of the process steps affected purification performance significantly.     

In vivo and in vitro 99mTc-protein bound of renal agents: 99mTc-prylidinomethyltetracycline (99mTc-Sn-Pmt) and 99mTc-Sn-Gluco-ene-diolate (99mTc-Gluco)

Protein binding affects tissue distribution, plasma clearance and uptake of renal radiopharmaceuticals. The ^99mTc bound to plasma protein after incubation ^99mTc-Gluco-ene-diolate (^99mTc-Sn-Gluco) agent or ^99mTc-prylidinomethyl-tetracycline (^99mTc-Sn-PMT) agent with plasma protein. It was observed that the protein bound to ^99mTc is lesser extent with (^99mTc-Sn-Gluco) agent than with the ^99mTc-PMT agent. ^99mTc-Sn-PMT is excreted more rapidly than ^99mTc-Sn-Gluco. On the other hand the percentage binding to protein seems to depend on the origin of the protein and or the type of protein (human or animal). However lower human protein binding or higher protein binding were observed with ^99mTc-Sn-Gluco or with ^99mTc-Sn-PMT, respectively compared with the binding to rat protein. The unbroken down of the chemical form of the origin of these two agents and the highest of ^99mTc-Sn-Gluco remained as origin in urine indicate that ^99mTc-Sn-Gluco are more stable than ^99mTc-Sn-PMT.Concerning the type of protein binding to ^99mTc-Sn-PMT or to ^99mTc-Sn-Gluco, it was observed that Human Plasma Protein is greater binding than Human serum protein or than IgG.     

Combining Low Pressure Liquid Affinity Chromatography and Flow Injection Analysis for the Quantitation of Immunoglobulins

Abstract

A simple, accurate method combining low pressure liquid affinity chromatography and flow injection analysis is described for the quantitation of immunoglobulins in biologicals fluids. The affinity matrix consists of Protein A covalently immobilized to a 2-fluoro-1 methylpyridinium salt activated Fractogel support. Utilizing a 1 cm³ affinity column, optimized binding and eluting buffer flow rates of 0.7 and 1.5 mL min^?1, respectively, and a sample loop size of 100 μL, IgG's can be eluted from the affinity column in about 9 min. Linear standard curves (r > 0.99) were obtained at concentrations up to at least 4.0 and 8.0 mg mL^?1 respectively for human and bovine IgG. Recovery yields are good ranging from 96–100%. The within day CV for human and bovine IgG was found to be less than 3.0% whereas the day to day CV was less than 3.4% (n=10). IgG concentrations of spiked and unspiked bovine plasma samples obtained by the low pressure affinity/flow injection method when compared to those obtained by the radial immunodiffusion agreed to within 4%.     

“Parallel factor analysis of multi-excitation ultraviolet resonance Raman spectra for protein secondary structure determination”

Protein secondary structural analysis is important for understanding the relationship between protein structure and function, or more importantly how changes in structure relate to loss of function. The structurally sensitive protein vibrational modes (amide I, II, III and S) in deep-ultraviolet resonance Raman (DUVRR) spectra resulting from the backbone C–O and N–H vibrations make DUVRR a potentially powerful tool for studying secondary structure changes. Experimental studies reveal that the position and intensity of the four amide modes in DUVRR spectra of proteins are largely correlated with the varying fractions of α-helix, β-sheet and disordered structural content of proteins. Employing multivariate calibration methods and DUVRR spectra of globular proteins with varying structural compositions, the secondary structure of a protein with unknown structure can be predicted. A disadvantage of multivariate calibration methods is the requirement of known concentration or spectral profiles. Second-order curve resolution methods, such as parallel factor analysis (PARAFAC), do not have such a requirement due to the “second-order advantage.” An exceptional feature of DUVRR spectroscopy is that DUVRR spectra are linearly dependent on both excitation wavelength and secondary structure composition. Thus, higher order data can be created by combining protein DUVRR spectra of several proteins collected at multiple excitation wavelengths to give multi-excitation ultraviolet resonance Raman data (ME-UVRR). PARAFAC has been used to analyze ME-UVRR data of nine proteins to resolve the pure spectral, excitation and compositional profiles. A three factor model with non-negativity constraints produced three unique factors that were correlated with the relative abundance of helical, β-sheet and poly-proline II dihedral angles. This is the first empirical evidence that the typically resolved “disordered” spectrum represents the better defined poly-proline II type structure.     

Oscillatory transverse electric field enhances protein resolution and capacity of size-exclusion chromatography

Protein separations by a novel size-exclusion electrochromatography (SEEC) are presented. The present SEEC, denoted as pSEEC, was established with an oscillatory low-voltage electric field perpendicular to the mobile-phase streamline. Retention experiments with different proteins indicated that the influence of electric field strength on the partition coefficient is different for different proteins as well as for the same protein under different mobile-phase conditions. These results of protein retention led to the experimental design of protein separations with binary mixtures of BSA and immunoglobulin G (IgG), myoglobin (Myo) and lysozyme (Lys), as well as ovalbumin (Oval) and Myo. The separation results for the binary protein systems sufficiently exhibited the applicability of the pSEEC for various separations in terms of their molecular weights (MWs) as well as pIs. For example, it was possible to separate the gel-excluded proteins (BSA/IgG) as well as gel-permeable and similar-molecular-weight proteins (Myo/Lys) by the pSEEC. Moreover, in the cases of Oval/ Myo, which could be partially separated by size-exclusion chromatography, the use of the pSEEC greatly improved the resolution and the separation became possible at high sample loading. The results indicate that the pSEEC technology is promising for preparative protein separations.     

莱克多巴胺免疫亲和柱的制备与应用研究

用多元酸酐与混合酸酐相结合的方法合成了莱克多巴胺(Rac)抗原,免疫动物获得特异性抗体,并以蛋白A柱纯化得到IgG抗体。琼脂糖凝胶(Sepharose 4B)经溴化氰(CNBr)活化后与IgG抗体偶联,制备莱克多巴胺免疫吸附剂。据此建立了尿液中莱克多巴胺的免疫亲和柱净化/液相色谱-荧光法(HPLC-FL)测定的分析方法。免疫制备特异抗体50%抑制浓度(IC50)为5μg/L。Sepharose 4B经CNBr活化后与2 mg抗体的偶联率达87.4%。1 mL吸附剂的柱容量为67.57 ng。尿液中莱克多巴胺的回收率为76%~90%。