Chromatographic separation of three monoclonal antibody variants using multicolumn countercurrent solvent gradient purification (MCSGP)

Multicolumn countercurrent solvent gradient purification (MCSGP) is a continuous chromatographic process developed in recent years (Aumann and Morbidelli, 2007a; Aumann et al., 2007) that is particularly suited for applications in the field of bioseparations. Like batch chromatography, MCSGP is suitable for three-fraction chromatographic separations and able to perform solvent gradients but it is superior in terms of solvent consumption, yield, purity, and productivity due to the countercurrent movement of the liquid and the solid phases. In this work, the MCSGP process is applied to the separation of three monoclonal antibody variants on a conventional preparative cation exchange resin. The experimental process performance was compared to simulations based on a lumped kinetic model. Yield and purity values of the target variant of 93%, respectively were obtained experimentally. The batch reference process was clearly outperformed by the MCSGP process.     

Countercurrent tangential chromatography for large-scale protein purification

Recent advances in cell culture technology have created significant pressure on the downstream purification process, leading to a "downstream bottleneck" in the production of recombinant therapeutic proteins for the treatment of cancer, genetic disorders, and cardiovascular disease. Countercurrent tangential chromatography overcomes many of the limitations of conventional column chromatography by having the resin (in the form of a slurry) flow through a series of static mixers and hollow fiber membrane modules. The buffers used in the binding, washing, and elution steps flow countercurrent to the resin, enabling high-resolution separations while reducing the amount of buffer needed for protein purification. The results obtained in this study provide the first experimental demonstration of the feasibility of using countercurrent tangential chromatography for the separation of a model protein mixture containing bovine serum albumin and myoglobin using a commercially available anion exchange resin. Batch uptake/desorption experiments were used in combination with critical flux data for the hollow fiber filters to design the countercurrent tangential chromatography system. A two-stage batch separation yielded the purified target protein at >99% purity with 94% recovery. The results clearly demonstrate the potential of using countercurrent tangential chromatography for the large-scale purification of therapeutic proteins.     

Parametric study of a 6-column countercurrent solvent gradient purification (MCSGP) unit

The novel "multicolumn countercurrent solvent gradient purification" (MCSGP) process has been modeled for the purification of a polypeptide mixture characterized by a strong non-linear competitive adsorption isotherm. As a model system, the purification of an industrial polypeptide mixture containing 46% of the hormone calcitonin has been selected. The many impurities contained in the mixture have been lumped into three key impurities, which are selected as the ones eluting closer to the main component. The simulation model allows for a better understanding of the complex operating behavior of the multicolumn system, which has been experimentally investigated in a previous work. Through a systematic parametric analyses of the model behavior, the main operating parameters controlling the process performance in terms of purity and yield are investigated. The study of internal liquid and adsorbed phase concentration profiles along the unit for the different operating conditions allow elucidating the working principle of the new separation process. It is found that the MCSGP unit achieves much higher yields for a given product purity than the corresponding single-column batch units.     

Separation of egg yolk immunoglobulins using an automated liquid chromatography system

An automated liquid chromatography system was developed to carry out the separation of an egg yolk immunoglobulin (IgY) using cation exchange media. Industrially separated egg yolk was diluted 10 times with distilled water, the pH adjusted to 5.5, and the water-soluble protein fraction separated from lipoproteins by sedimentation. The supernatant was filtered and then applied to a column packed with a cation exchanger within an automated liquid chromatography system. Different operating conditions were investigated using phosphate buffer in order to assess the effect on recovery and purity. Fractions as pure as 80% could be collected and a recovery of the chromatography step of about 65% was obtained for a purity of 60% using either a linear or step gradient. The overall recovery for the process was 34% if one-step dilution/extraction is used for lipoprotein separation by sedimentation, and 51% if two-step dillution/extraction is used. Further improvement of the yield to about 60% is possible using centrifugation for lipoprotein separation. The automated system confers many advantages, the key elements being the time savings and accurate control of the process. (c) 1992 John Wiley & Sons, Inc.     

高速逆流色谱技术在生物大分子分离纯化中的应用

高速逆流色谱是一种连续液-液色谱技术,具有无固相载体、样品无需严格预处理等优点。近10年来,在设备结构和溶剂体系等方面进行了大量的研究开发,已推广应用于生物技术、医药、天然产物、环境监测、食品等领域。为适应生物大分子和活性细胞的分离,采用条件温和的双水相体系,研究开发相应的高速逆流色谱设备已成为热点。针对双水相体系的特点,已经开发出了多种具有较高固定相保留率的新型高速逆流色谱设备,通过优化实验条件,成功地进行了多种蛋白质的分离纯化。本对该领域的最新进展进行了综述与评价。     

Evaluation of differences between dual salt‐pH gradient elution and mono gradient elution using a thermodynamic model: Simultaneous separation of six monoclonal antibody charge and size variants on preparative‐scale ion exchange chromatographic resin

The efficiencies of mono gradient elution and dual salt‐pH gradient elution for separation of six mAb charge and size variants on a preparative‐scale ion exchange chromatographic resin are compared in this study. Results showed that opposite dual salt‐pH gradient elution with increasing pH gradient and simultaneously decreasing salt gradient is best suited for the separation of these mAb charge and size variants on Eshmuno^® CPX. Besides giving high binding capacity, this type of opposite dual salt‐pH gradient also provides better resolved mAb variant peaks and lower conductivity in the elution pools compared to single pH or salt gradients. To have a mechanistic understanding of the differences in mAb variants retention behaviors of mono pH gradient, parallel dual salt‐pH gradient, and opposite dual salt‐pH gradient, a linear gradient elution model was used. After determining the model parameters using the linear gradient elution model, 2D plots were used to show the pH and salt dependencies of the reciprocals of distribution coefficient, equilibrium constant, and effective ionic capacity of the mAb variants in these gradient elution systems. Comparison of the 2D plots indicated that the advantage of opposite dual salt‐pH gradient system with increasing pH gradient and simultaneously decreasing salt gradient is the noncontinuous increased acceleration of protein migration. Furthermore, the fitted model parameters can be used for the prediction and optimization of mAb variants separation in dual salt‐pH gradient and step elution. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:973–986, 2018     

疏水层析结合冷乙醇沉淀纯化人血清白蛋白

将层析技术与冷乙醇工艺相结合用于人血清白蛋白的纯化 ,对各过程所采用的层析介质及层析条件进行了探索 ,得到了一条从人血浆中制备血清白蛋白的新路线 :将一步冷乙醇沉淀后的血浆上清进行脱盐除乙醇 ,用阳离子交换介质CMSepharoseFF以透过式层析的模式吸附非白蛋白组分 ,最后选用ButylSepharoseFF一步疏水层析后所得样品经SDS-PAGE银染显示一条单带 ,分析其纯度大于 99% ,计算工艺收率为 81.2%。与传统冷乙醇工艺相比较 ,该工艺最终样品纯度更高 ,且层析可以在常温下操作 ,易实现自动化控制.     

高速逆流双水相色谱法纯化卵白蛋白

生物大分子的液_固色谱纯化过程中固相载体会产生产物吸附、变性等不良影响。高速逆流色谱无需固相载体 ,且具有高分便率和高回收率的优点 ,其中有机相 水相体系在分离天然产物中应用广泛 ,而应用双水相体系分离生物大分子尚处于研究阶段。双水相高速逆流色谱体系的建立与仪器设备及操作工艺条件密切相关 ,因此利用多分离柱高速逆流色谱仪 ,研究了PEG1000-无机盐双水相体系对标准蛋白质混合物以及卵白蛋白的分离。pH值和PEG浓度对不同种类蛋白质的分配系数影响不同 ,实验发现在pH9.2的150% (W/W)PEG1000 170% (W/W)磷酸钾盐体系中 ,细胞色素C、溶菌酶和肌红蛋白的分配系数差异较大 ,且分布合理 ,因而采用该体系在 0 8mL min流速 ,85 0r min转速的条件下 ,成功分离了细胞色素C、溶菌酶和肌红蛋白的混合物。实验也发现在pH9 2的 16 0 % (W/W)PEG10 0 0 17 0 % (W/W)磷酸钾盐体系中 ,鸡蛋清样品中的主要蛋白质成分:卵转铁蛋白、卵白蛋白和溶菌酶的分配系数差异最大 ,因而采用该体系在 1 8mL min流速、85 0r mi转速的条件下,200min内从鸡蛋清样品中成功分离卵白蛋白,其电泳纯度为100%,收率为95%.     

Preparative Enantioseparation of β‐Substituted‐2‐Phenylpropionic Acids by Countercurrent Chromatography With Substituted β‐Cyclodextrin as Chiral Selectors

Preparative enantioseparation of four β‐substituted‐2‐phenylpropionic acids was performed by countercurrent chromatography with substituted β‐cyclodextrin as chiral selectors. The two‐phase solvent system was composed of n‐hexane‐ethyl acetate‐0.10 mol L‐1 of phosphate buffer solution at pH 2.67 containing 0.10 mol L^‐1 of hydroxypropyl‐β‐cyclodextrin (HP‐β‐CD) or sulfobutylether‐β‐cyclodextrin (SBE‐β‐CD). The influence factors, including the type of substituted β‐cyclodextrin, composition of organic phase, concentration of chiral selector, pH value of the aqueous phase, and equilibrium temperature were optimized by enantioselective liquid–liquid extraction. Under the optimum separation conditions, 100 mg of 2‐phenylbutyric acid, 100 mg of tropic acid, and 50 mg of 2,3‐diphenylpropionic acid were successfully enantioseparated by high‐speed countercurrent chromatography, and the recovery of the (±)‐enantiomers was in the range of 90–91% for (±)‐2‐phenylbutyric acid, 91–92% for (±)‐tropic acid, 85–87% for (±)‐2,3‐diphenylpropionic acid with purity of over 97%, 96%, and 98%, respectively. The formation of 1:1 stoichiometric inclusion complex of β‐substituted‐2‐phenylpropionic acids with HP‐β‐CD was determined by UV spectrophotometry and the inclusion constants were calculated by a modified Benesi‐Hildebrand equation. The results showed that different enantioselectivities among different racemates were mainly caused by different enantiorecognition between each enantiomer and HP‐β‐CD, while it might be partially caused by different inclusion capacity between racemic solutes and HP‐β‐CD. Chirality 27:795–801, 2015. © 2015 Wiley Periodicals, Inc.     

Increasing the activity of monoclonal antibody therapeutics by continuous chromatography (MCSGP)

The charged monoclonal antibody (mAb) variants of the commercially available therapeutics Avastin®, Herceptin® and Erbitux® were separated by ion‐exchange gradient chromatography in batch and continuous countercurrent mode (MCSGP process). Different stationary phases, buffer conditions and two MCSGP configurations were used in order to demonstrate the broad applicability of MCSGP in the field of charged protein variant separation. Batch chromatography and MCSGP were compared with respect to yield, purity, and productivity. In the case of Herceptin®, also the biological activity of the product stream was taken into account as performance indicator. The robustness of the MCSGP process against feed composition variations was confirmed experimentally and by model simulations. Biotechnol. Bioeng. 2010;107:652–662. © 2010 Wiley Periodicals, Inc.     

小麦小花高纯度线粒体的分离及其蛋白质双向电泳体系建立

应用差速离心和Percoll不连续密度梯度法分离纯化小麦三核期小花线粒体. 在裂解液选择、IPG胶条pH值范围、SDS-PAGE胶浓度及蛋白质上样量等方面对线粒体蛋白质双向电泳体系进行探索和优化,确立了一套适用于小麦小花高纯度完整线粒体的分离方法及其蛋白质双向电泳的技术体系. 结果表明,采用20%、24%和40% Percoll密度梯度和28% Percoll自形成密度高速离心体系,获得了有活性、高纯度且较完整的线粒体;经TCA-丙酮法提取蛋白,以7 mol/L尿素,2 mol/L硫脲,4% CHAPS(W/V),65 mmol/L DTT,0.5% IPG缓冲液(V/V),0.001% 溴酚蓝(W/V)裂解液溶解蛋白,采用17 cm,pH 4～7 IPG胶条和11% SDS-PAGE分离胶,上样量为160 μg,硝酸银染色法,更适合小麦小花线粒体蛋白质组双向电泳分离. 经PDQuest 2DE 8.0.1软件包统计分析,在2-DE图谱上分辨出约150个蛋白点,蛋白点清晰呈圆形,无横条纹干扰,这为利用双向电泳技术在亚细胞水平对线粒体进行蛋白质组学研究与分析奠定了基础,更为进一步分析研究线粒体与雄性不育的关系提供了理论与技术支撑.     

Effect of glycation on the heterogeneity of human serum albumin analysed by reversed-phase high-performance liquid chromatography in a solvent containing formic acid

Non-enzymic glycation of human serum albumin (HSA) induces a change in its charge heterogeneity that may account for its particular renal clearance in patients with early diabetic nephropathy. A new high-performance liquid chromatographic analysis for the study of HSA heterogeneity is described based on a high content of formic acid in the mobile phase combined with a concave gradient of isopropanol. Under these conditions, native HSA was separated into three individual components (I, II and III). When glycated HSA was analysed, it was found that although the present method is not suitable for the separation of glycated from non-glycated HSA, it shows the effect of glycation in producing changes in HSA heterogeneity that are different from those reported on surface change. This finding suggests an additional factor (probably conformational changes) that is contributing to the heterogeneity of glycated HSA.     

Albumin recovery with centrifugal adsorption technology (CAT)

Centrifugal adsorption technology (CAT) is a new compact, countercurrent technology for efficient adsorption from large liquid streams by using adsorbent particles in the micrometer range. CAT seems particularly suited for the recovery of macromolecules at low concentrations, because the small particle dimensions lead to fast mass transfer rates. In this work, the potential of CAT for protein recovery is studied by model and experiment. A predictive model for the separation performance of CAT is presented, incorporating mass transfer resistance and axial dispersion transport in the liquid and the adsorbent phases. The model calculations were compared to experimental data for the adsorption of bovine serum albumin (BSA) on a standard commercial anion-exchange resin with particle diameter d(p) = 50 microm in a pilot-scale CAT apparatus. The model calculations accurately predicted the separation efficiency of CAT. The experimental set-up is shown to be mass transfer limited for the conducted experiments, which agrees with the model predictions. The model was also used to estimate the dimensions and performance of a CAT apparatus for the large-scale recovery of human serum albumin (HSA) from fermentation broth at the scale of 40 tons per year. The resulting equipment dimensions proved to be very small indeed, making CAT a potentially very attractive technology.     

Dependence of the efficiency of the fractionation of summary E. coli cell membranes on the method of their disintegration

The efficiency of fractionation in the sucrose density gradient of E. coli cell membranes obtained after cell disintegration by ultrasonic, ballistic and extrusion methods was measured. The purity of individual membrane fractions was estimated by electron microscopy and polyacrylamide gel electrophoresis. The application of ballistic disintegration and solid state extrusion did not separate inner and outer membranes. Cell disintegration by means of ultrasonic treatment and liquid state extrusion allowed reproducible separation of membranes of the two types with a sufficiently high degree of purity.     

Determination of denaturated proteins and biotoxins by on-line size-exclusion chromatography-digestion-liquid chromatography-electrospray mass spectrometry

A multidimensional analytical method for the rapid determination and identification of proteins has been developed. The method is based on the size-exclusion fractionation of protein-containing samples, subsequent on-line trypsin digestion and desalination, and reversed-phase high-performance liquid chromatography-electrospray mass spectrometry detection. The present system reduces digestion times to 20 min and the total analysis time to less than 100 min. Using bovine serum albumin and myoglobin as model proteins, optimization of key parameters such as digestion times and interfacing conditions between the different pretreatment steps was performed. The automated system was tested for the identification of infectious disease agents such as cholera toxin and staphylococcal enterotoxin B. This resulted typically in a positive identification by a total sequence coverage of approximately 40%.     

Purification of optical imaging ligand-Cybesin by high-speed counter-current chromatography

Fluorescent Cybesin (Cypate-Bombesin Peptide Analogue Conjugate) was synthesized from Indocyanine Green (ICG) and the bombesin receptor ligand as a contrast agent for detecting pancreas tumors. However, the LC-MS analysis indicated that the target compound was only a minor component in the reaction mixture. Since preparative HPLC can hardly separate such a small amount of the target compound directly from the original crude reaction mixture without a considerable adsorptive loss onto the solid support, high-speed counter-current chromatography (HSCCC) was used for purification since the method uses no solid support and promises high sample recovery. A suitable two-phase solvent system composed of hexane/ethyl acetate/methanol/methyl t-butyl ether/acetonitrile/water) at a volume ratio of 1:1:1:4:4:7 was selected based on the partition coefficient of Cybesin (K≈0.9) determined by LC-MS. The separation was performed in two steps using the same solvent system with lower aqueous mobile phase. From 400 mg of the crude reaction mixture the first separation yielded 7.7 mg of fractions containing the target compound at 12.8% purity, and in the second run 1 mg of Cybesin was obtained at purity of 94.0% with a sample recovery rate of over 95% based on the LC-MS analysis.     

Phosphoproteomic analysis using immobilized metal ion affinity chromatography on the basis of cellulose powder

Detailed characterization of phosphoproteins as well as other post-translationally modified proteins such as glycoproteins, is required to fully understand protein function and regulatory events in cells and organisms. Therefore, an experimental strategy for the isolation of phosphoproteins using a new immobilized metal ion affinity chromatograph (IMAC) material on the basis of cellulose has been developed and characterized. Different approaches have been used to test the material. Recovery rates were determined by 32P labelling of a myelin basic protein fragment and by reversed-phase high-performance liquid chromatography-electrospray ionization mass spectrometry using a tryptic digest of the model protein bovine beta-casein. Selectivity was demonstrated by enrichment and separation of phosphopeptides from different samples, such as from a digest of horse myoglobin as well as from a digest of in vitro phosphorylated extracellular signal regulates kinase 2 (ERK2) mixed with synthetic phosphopeptides, phosphorylated on different amino acid residues. Furthermore, simplification and optimization of sample pretreatment was achieved by combining the separating (IMAC) and desalting (C18) step during preparative high performance liquid chromatography. The comparison between our material and a commercially available IMAC system (POROS 20 MC; Perspective BioSystems) emphasizes the competitiveness of the cellulose. Confirmed by the obtained data, the cellulose material performed as well as the commercially available sorbent, however with the advantage, that it can be produced rather easily and at very low cost.     

Preparative separation of amino acid enantiomers as N-TFA,O-isopropyl derivatives by continuous countercurrent gas-liquid chromatography

Preparative separation of derivatives of amino acid enantiomers was carried out by a countercurrent gas–liquid chromatography (CCGLC) with chiral liquid phases, N-stearoyl-L -valine tert-butylamide and/or N-stearoyl-L -leucine tert-butylamide. In order to make effective use of these phases and also to lower the viscosity, Apiezon C was added as diluent. Through a repeated operation of a temperature gradient, purities more than 99% of leucine and α-amino butyric acid derivatives were proved to be obtained. © 1993 Wiley-Liss, Inc.     

Isolation of four high-purity dammarane saponins from extract of Panax notoginseng by centrifugal partition chromatography coupled with evaporative light scattering detection in one operation

Introduction – Centrifugal partition chromatography (CPC), as a continuous liquid–liquid partition chromatography with no solid support matrix, combined with evaporative light scattering detection (ELSD) was employed for systematic separation and purification of weak‐chromophoric saponins from a highly valued and important traditional Chinese herbal medicine, Panax notoginseng. Objective – To separate and isolate high‐purity saponins from extract of Panax notoginseng using CPC‐ELSD with a simple and low toxicity solvent system. Methodology – Samples were preparaed by extracting the root material with acetone, treated with n‐butanol and then freeze‐dried. CPC‐ELSD was applied in the separation and detection of notoginsenoside and ginsenosides from extract of Panax notoginseng using a solvent system composed of ethyl acetate–n‐butanol–water (1:1:2, v/v/v). The saponins were analysed and identified by their retention time with high‐performance liquid chromatography (HPLC) coupled with ELSD, as well as electrospray ionisation tandem mass spectrometry (ESI‐MSⁿ ) in the negative and positive ion modes with the authentic standards. Results – A total of 9.6 mg of notoginsenoside R₁, 67.8 mg of ginsenoside Rg₁, 2.3 mg of Re and 286.5 mg of Rb₁ were purified from 487.2 mg of n‐butanol extract of P. notoginseng. The purities of obtained saponins in a single run were assessed to be over 98% by HPLC‐ELSD. Conclusion – CPC‐ELSD was proved to be a very fast and efficient tool for separation of high‐purity dammarane saponins. Copyright © 2011 John Wiley & Sons, Ltd.     

Countercurrent chromatography with a new horizontal flow-through coil planet centrifuge

A versatile horizontal flow-through coil planet centrifuge has been introduced for performing countercurrent chromatography. The apparatus carries a pair of coiled separation columns. Both of these allow continuous elution simultaneously without the use of rotating seals. One column enables preparative-scale separations and the other, analytical-scale separations, both with a high partition efficiency comparable to that obtained in liquid chromatography but without the complications arising from the use of solid supports. Capability of the apparatus was demonstrated on separation of dinitrophenyl amino acids using a two-phase solvent system composed of CHCl₃/CH₃COOH/0.1 HCl at a 2/2/1 volume ratio.