Comparison of different ligand densities for the manufacture of CB Hep-1 immunosorbents

Different ligand densities of monoclonal antibody (Mab) CB.Hep-1 were studied during covalent coupling on Sepharose CL-4B for recombinant hepatitis B surface antigen (rHBsAg) immunoaffinity purification. Ligand densities of 2.2, 3.2, 4.2 and 5.2 mg Mab/ml immunosorbents, respectively, were assayed during five cycles of immunoaffinity chromatography (IAC). Adsorption capacities averaged either 3.2 mg/ml (0.57 mg rHBsAg/ml immunosorbent/5.42 mg of total purified protein) or 5.2 mg/ml (0.56 mg rHBsAg/ml immunosorbent/5.05 mg total purified protein). Immunosorbents showed ligand leakage levels below 3 ng Mab/microg rHBsAg. Antigen purity was higher than 95% in all cases. The results suggest that a ligand density (LD) of 3.2 mg Mab/ml immunosorbent should be used for immunoaffinity chromatography because no significant differences were found in the ligand densities studied (P-value=0.012), which saves 40% of CB.Hep-1 immunosorbent manufacturing cost in comparison with 5 mg Mab/ml immunosorbent, which is currently used in large-scale production.     

Purification of cell culture‐derived modified vaccinia ankara virus by pseudo‐affinity membrane adsorbers and hydrophobic interaction chromatography

A purification scheme for cell culture‐derived smallpox vaccines based on an orthogonal downstream process of pseudo‐affinity membrane adsorbers (MA) and hydrophobic interaction chromatography (HIC) was investigated. The applied pseudo‐affinity chromatography, based on reinforced sulfated cellulose and heparin‐MA, was optimized in terms of dynamic binding capacities, virus yield and process productivity. HIC was introduced as a subsequent method to further reduce the DNA content. Therefore, two screens were undertaken. First, several HIC ligands were screened for different adsorption behavior between virus particles and DNA. Second, elution from pseudo‐affinity MA and adsorption of virus particles onto the hydrophobic interaction matrix was explored by a series of buffers using different ammonium sulfate concentrations. Eventually, variations between different cultivation batches and buffer conditions were investigated.The most promising combination, a sulfated cellulose membrane adsorber with subsequent phenyl HIC resulted in overall virus particle recoveries ranging from 76% to 55% depending on the product batch and applied conditions. On average, 61% of the recovered virus particles were infective within all tested purification schemes and conditions. Final DNA content varied from 0.01% to 2.5% of the starting material and the level of contaminating protein was below 0.1%. Biotechnol. Bioeng. 2010;107: 312–320. © 2010 Wiley Periodicals, Inc.     

重组人粒细胞-巨噬细胞集落刺激因子复性和纯化方法的比较

比较重组人粒细胞-巨噬细胞集落刺激因子(rhGM-CSF)在用疏水色谱(HIC)、离子交换色谱(IEC)和体积排阻色谱(SEC)3种液相色谱进行复性和纯化,选择较好的复性和纯化方法.通过对比rhGM-CSF在液相色谱上复性和纯化的主要指标,包括比活、纯度和质量回收率,结果发现采用HIC和IEC对rhGM-CSF进行复性和纯化时,其比活可以达到国家标准,纯度和质量回收率也比较高,而采用SEC,其比活、纯度和质量回收率远低于HIC和IEC.     

A rapid and universal tandem-purification strategy for recombinant proteins

A major goal in the production of therapeutic proteins, subunit vaccines, as well as recombinant proteins needed for structure determination and structural proteomics is their recovery in a pure and functional state using the simplest purification procedures. Here, we report the design and use of a novel tandem (His)(6)-calmodulin (HiCaM) fusion tag that combines two distinct purification strategies, namely, immobilized metal affinity (IMAC) and hydrophobic interaction chromatography (HIC), in a simple two-step procedure. Two model constructs were generated by fusing the HiCaM purification tag to the N terminus of either the enhanced green fluorescent protein (eGFP) or the human tumor suppressor protein p53. These fusion constructs were abundantly expressed in Escherichia coli and rapidly purified from cleared lysates by tandem IMAC/HIC to near homogeneity under native conditions. Cleavage at a thrombin recognition site between the HiCaM-tag and the constructs readily produced untagged, functional versions of eGFP and human p53 that were >97% pure. The HiCaM purification strategy is rapid, makes use of widely available, high-capacity, and inexpensive matrices, and therefore represents an excellent approach for large-scale purification of recombinant proteins as well as small-scale protein array designs.     

Improving the recovery of clarification process of recombinant hepatitis B surface antigen in large-scale by optimizing adsorption-desorption parameters on Aerosil-380

Abstract

In the downstream process of recombinant hepatitis B surface antigen (rHBsAg), nano-colloidal silica adsorbent (Aerosil-380) is one of the possible methods to separate the antigen from other main impurities partially. The current study aimed to maximize the adsorptive capacity of Aerosil-380 as well as rHBsAg recovery for large-scale production of recombinant hepatitis B vaccine. The experimental design methodology was used to optimize the eight critical parameters influencing the efficiency, rHBsAg recovery, of the adsorption-desorption process in the lab-scale. These examined parameters were the adsorption–desorption temperature, pH, contact time, agitation speed, antigen concentration, and desorption buffer. Under optimal condition, the maximum adsorption capacity of Aerosil-380 was equal to 3333?μg.g^?1 (rHBsAg/adsorbent), and we could recover about 95% of rHBsAg with purity of 54% (rHBsAg/total protein) in the lab scale. Using the optimum parameters for rHBsAg clarification process in large-scale by Aerosil-380, we recovered about 78% of rHBsAg with 43% purity. Based on the obtained experimental data, Langmuir adsorption isotherm and pseudo-first-order kinetic model provide the best correlations of experimental data for the adsorbent. Findings of this study significantly increase the recovery of clarification process of rHBsAg in large-scale compared to previous reports.     

Semi-Automated Hydrophobic Interaction Chromatography Column Scouting Used in the Two-Step Purification of Recombinant Green Fluorescent Protein

Background

Hydrophobic interaction chromatography (HIC) most commonly requires experimental determination (i.e., scouting) in order to select an optimal chromatographic medium for purifying a given target protein. Neither a two-step purification of untagged green fluorescent protein (GFP) from crude bacterial lysate using sequential HIC and size exclusion chromatography (SEC), nor HIC column scouting elution profiles of GFP, have been previously reported.

Methods and Results

Bacterial lysate expressing recombinant GFP was sequentially adsorbed to commercially available HIC columns containing butyl, octyl, and phenyl-based HIC ligands coupled to matrices of varying bead size. The lysate was fractionated using a linear ammonium phosphate salt gradient at constant pH. Collected HIC eluate fractions containing retained GFP were then pooled and further purified using high-resolution preparative SEC. Significant differences in presumptive GFP elution profiles were observed using in-line absorption spectrophotometry (A₃₉₅) and post-run fluorimetry. SDS-PAGE and western blot demonstrated that fluorometric detection was the more accurate indicator of GFP elution in both HIC and SEC purification steps. Comparison of composite HIC column scouting data indicated that a phenyl ligand coupled to a 34 µm matrix produced the highest degree of target protein capture and separation.

Conclusions

Conducting two-step protein purification using the preferred HIC medium followed by SEC resulted in a final, concentrated product with >98% protein purity. In-line absorbance spectrophotometry was not as precise of an indicator of GFP elution as post-run fluorimetry. These findings demonstrate the importance of utilizing a combination of detection methods when evaluating purification strategies. GFP is a well-characterized model protein, used heavily in educational settings and by researchers with limited protein purification experience, and the data and strategies presented here may aid in development other of HIC-compatible protein purification schemes.     

蛋白质层析用离子交换和疏水作用层析介质的发展概况

层析是蛋白质纯化的关键技术之一 ,作为层析技术的核心———层析介质一直以来是层析技术研究的一个热点。近年来 ,越来越多的新型层析介质被开发出来 ,如粒度均匀的交联多糖、人工合成的大孔聚合物、触角型吸附剂、软胶包裹在硬胶表面等介质。主要介绍应用较为广泛的IEC和HIC介质的组成、特性及其在蛋白质纯化中的应用 ,还研究了与HIC技术相关的两种新技术 :亲硫层析和疏水电荷诱导层析 (HCIC) ,重点介绍了HCIC的介质及其应用 ,同时也讨论了在蛋白质纯化中应用的三相纯化策略 (富集、中间纯化和精制 )。结合我国的实际情况 ,就当前蛋白质纯化的离子交换和疏水层析介质面临的挑战和未来的发展进行讨论并提出了建议     

Purification of glucose oxidase from complex fermentation medium using tandem chromatography

A fast and efficient purification method for recombinant glucose oxidase (rGOx) for flask fermentation scale (up to 2L) was designed for the purposes of characterization of rGOx mutants during directed protein evolution. The Aspergillus niger GOx was cloned into a pYES2-alphaMF-GOx construct and expressed extracellularly in yeast Saccharomyces cerevisiae. Hydrophobic interaction (HIC)/size exclusion (SEC)-tandem chromatographic system was designed for direct purification of rGOx from a conditioned complex expression medium with minimum preceding sample preparation (only adjustments to conductivity, pH and coarse filtering). HIC on Butyl 650s (50 mM ammonium acetate pH 5.5 and 1.5 M ammonium sulphate) absorbs GOx from the medium and later it is eluted by 100% stepwise gradient with salt free buffer directly into SEC column (Sephadex 200) for desalting and final polishing separation. The electrophoretic and UV-vis spectrophotometric analyses have proven enzyme purity after purification.     

Development of a polishing step using a hydrophobic interaction membrane adsorber with a PER.C6®‐derived recombinant antibody

Membrane chromatography has already proven to be a powerful alternative to polishing columns in flow‐through mode for contaminant removal. As flow‐through utilization has expanded, membrane chromatography applications have included the capturing of large molecules, including proteins such as IgGs. Such bind‐and‐elute applications imply the demand for high binding capacity and larger membrane surface areas as compared to flow‐through applications. Given these considerations, a new Sartobind Phenyl? membrane adsorber was developed for large‐scale purification of biomolecules based on hydrophobic interaction chromatography (HIC) principles. The new hydrophobic membrane adsorber combines the advantages of membrane chromatography—virtually no diffusion limitation and shorter processing time—with high binding capacity for proteins comparable to that of conventional HIC resins as well as excellent resolution. Results from these studies confirmed the capability of HIC membrane adsorber to purify therapeutic proteins with high dynamic binding capacities in the range of 20 mg‐MAb/cm³‐membrane and excellent impurity reduction. In addition the HIC phenyl membrane adsorber can operate at five‐ to ten‐fold lower residence time when compared to column chromatography. A bind/elute purification step using the HIC membrane adsorber was developed for a recombinant monoclonal antibody produced using the PER.C6® cell line. Loading and elution conditions were optimized using statistical design of experiments. Scale‐up is further discussed, and the performance of the membrane adsorber is compared to a traditional HIC resin used in column chromatography. Biotechnol. Bioeng. 2010; 105: 296–305. © 2009 Wiley Periodicals, Inc.     

乳腺生物反应器表达的重组人乳清白蛋白的高效分离纯化

利用乳腺生物反应器高效地表达重组人乳清白蛋白,但是目标产物分离纯化的难度较大。通过分子模拟计算比较待分离原料中主要蛋白组分的物化性质,包括表面电势和表面疏水性,在此基础上设计了高分辨率、快速的分离纯化工艺。通过硫酸铵沉淀的正交试验条件优化,有效地去除了干扰层析精制过程的IgG杂质,提高了后续疏水层析的稳定性,从而成功地分离开目标蛋白及与其同源的牛乳清白蛋白杂质,得到纯度>95%的rHLA纯品,工艺回收率48.6%。乳糖合成活性和圆二色谱检测结果表明,纯化rHLA具有调节β-1,4-半乳糖苷转移酶活性和天然的空间结构。     

Considerations for operational space definition and optimization of a no-salt flowthrough hydrophobic interaction chromatography purification step

No-salt flowthrough hydrophobic interaction chromatography (HIC) has been shown to effectively remove process and product-related impurities from bioprocess streams. In this publication, a panel of six antibodies has been used to demonstrate operating principles for the application of no-salt flowthrough HIC in antibody purification processes. The results indicate that no-salt flowthrough HIC provides robust aggregate clearance across operating conditions including flow rate, and variations in resin ligand density. Additionally, HMW reduction has an optimal pH range relative to the isoelectric point of each molecule and high molecular weight (HMW) reduction can be improved by altering the total protein load and/or HMW concentration to drive binding of high molecular weight species to the resin.     

New method for the selective capture of antibodies under physiolgical conditions

Hydrophobic charge induction chromatography is a recently developed method for protein separation based on the use of dual-mode ligands. They are designed in such a way so as to combine a molecular interaction supported by a mild hydrophobic association effect in the absence of salts. When environmental pH is changed, the ligand becomes ionically charged resulting into the desorption of the protein. This method is applied to the separation of antibodies from ascite fluids and culture supernatants from hybridomas cultured in the presence of fetal bovine serum or in protein free environment. Typically adsorption from cell culture supernatants is accomplished without any pH or ionic strength adjustment; the column is then washed with a typical buffer to eliminate protein impurities. Antibodies are then desorbed using acetate buffer, pH 4. Antibody binding capacity is in the range of 30 mg per ml of resin at 10% breakthrough. Antibody purity varies according to the initial feed stock and can reach values higher than 90% in a single pass. One example of antibody purification process involving hydrophobic charge induction chromatography as a capture step followed by a polishing phase with DEAE Ceramic HyperD is described. Longevity and ligand leakage are compatible with large-scale applications.     

Optimisation of the coupled monoclonal antibody density for recombinant hepatitis B virus surface antigen immunopurification

Using immunosorbents based upon cyanogen bromide-Sepharose CL-4B, we have examined different ligand densities in coupling of monoclonal antibody (MAb) to find the best performance, for recombinant hepatitis B surface antigen (rHBsAg) purification. Three replicates of 5 and 15 cycles of densities ranges: 2.17-2.19, 3.18-3.62, 4.06-4.17, and 5.13-5.40 mg/ml (control); or 1.81-2.47, 3.17-3.41, 4.16-4.28, and 5.16-5.19 mg/ml (control), respectively were evaluated in terms of binding capacity, antigen recovery, ligand leakage and purity of antigen, and compared to the control. Adsorption and antigen recovery of immunosorbents manufactured were not different statistically, eventhough increased 8.08 and 9.90% at a range of 3.17-3.41 mg/ml. At this range, efficiency expressed as productivity and MAb saving was optimal. Ligand leakage and purity of antigen showed similar behaviour among all densities. Aspects related to ligand density in antigen immunoaffinity purification are discussed.     

Automated Hydrophobic Interaction Chromatography Column Selection for Use in Protein Purification

In contrast to other chromatographic methods for purifying proteins (e.g. gel filtration, affinity, and ion exchange), hydrophobic interaction chromatography (HIC) commonly requires experimental determination (referred to as screening or "scouting") in order to select the most suitable chromatographic medium for purifying a given protein ¹. The method presented here describes an automated approach to scouting for an optimal HIC media to be used in protein purification.HIC separates proteins and other biomolecules from a crude lysate based on differences in hydrophobicity. Similar to affinity chromatography (AC) and ion exchange chromatography (IEX), HIC is capable of concentrating the protein of interest as it progresses through the chromatographic process. Proteins best suited for purification by HIC include those with hydrophobic surface regions and able to withstand exposure to salt concentrations in excess of 2 M ammonium sulfate ((NH₄)₂SO₄). HIC is often chosen as a purification method for proteins lacking an affinity tag, and thus unsuitable for AC, and when IEX fails to provide adequate purification. Hydrophobic moieties on the protein surface temporarily bind to a nonpolar ligand coupled to an inert, immobile matrix. The interaction between protein and ligand are highly dependent on the salt concentration of the buffer flowing through the chromatography column, with high ionic concentrations strengthening the protein-ligand interaction and making the protein immobile (i.e. bound inside the column) ². As salt concentrations decrease, the protein-ligand interaction dissipates, the protein again becomes mobile and elutes from the column. Several HIC media are commercially available in pre-packed columns, each containing one of several hydrophobic ligands (e.g. S-butyl, butyl, octyl, and phenyl) cross-linked at varying densities to agarose beads of a specific diameter ³. Automated column scouting allows for an efficient approach for determining which HIC media should be employed for future, more exhaustive optimization experiments and protein purification runs ⁴.The specific protein being purified here is recombinant green fluorescent protein (GFP); however, the approach may be adapted for purifying other proteins with one or more hydrophobic surface regions. GFP serves as a useful model protein, due to its stability, unique light absorbance peak at 397 nm, and fluorescence when exposed to UV light ⁵. Bacterial lysate containing wild type GFP was prepared in a high-salt buffer, loaded into a Bio-Rad DuoFlow medium pressure liquid chromatography system, and adsorbed to HiTrap HIC columns containing different HIC media. The protein was eluted from the columns and analyzed by in-line and post-run detection methods. Buffer blending, dynamic sample loop injection, sequential column selection, multi-wavelength analysis, and split fraction eluate collection increased the functionality of the system and reproducibility of the experimental approach.Download video file.^{(63M, mov)}     

Scale-up of hydrophobic interaction chromatography for the purification of a DNA vaccine against rabies

The purification of a DNA vaccine against rabies by hydrophobic interaction chromatography (HIC) using a Sepharose gel derivatised with 1,4-butanediol diglycidyl ether was scaled up 60 times. The purification profile was not affected by increased loadings (up to 15 mg DNA) and a product with a consistent quality was obtained. Fourteen mg of plasmid with an HPLC purity of 100% were obtained in one run, corresponding to a 95% yield.     

Purification of antibacterial attacins induced in Hyalophora cecropia pupae immunized with Enterobacter cloacae C7-501 using ion-exchange chromatography,hydrophobic interaction chromatography,and Rotofor® isoelectric focusing

Hyalophora cecropia pupae were infected by Enterobacter cloacae C7-501 to induce antibacterial attacins for purification. The induction of attacins in immunized pupae was confirmed by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). Ion-exchange chromatography (IEC), hydrophobic interaction chromatography (HIC), and Rotofor® isoelectric focusing (ISEF) were applied to isolate attacins from the hemolymph. IEC separated attacins from most hemolymph proteins, but the fractions containing attacins also had other proteins of 20 and 64 kDa in length. In IEC, attacin was eluted with ~0.2 M NaCl. The best conditions for IEC were pH 9, flow rate of 2 mL/min, with step elution (0.025, 0.05, 0.075, 0.1, 0.2, 0.4 and 1.0 M NaCl). In HIC, most other proteins were eluted with the ammonium persulfate treatment. HIC isolated attacin proteins under hydrophobic conditions, at ~50% EtOH. However, the fraction with attacins also contained other proteins. The Rotofor® ISEF produced fractions containing attacins at isoelectric points ranging between 5.7 and 8.3. However, non-specific proteins were detected in the fraction samples, and the recovery of attacins was low. The purification efficiency of ISEF was lower than IEC and HIC. In this study, the expression of attacins was induced in H. cecropia pupae infected with E. cloacae C7-501, and attacins could be purified by IEC and ISEF. Overall, IEC provided better separation of attacins from the hemolymph of H. cecropia pupae immunized with E. cloacae bacteria than HIC and Rotofor® ISEF.     

A Procedure for Human Pregnancy Zone Protein (and Human α2-Macroglobulin) Purification Using Hydrophobic Interaction Chromatography on Phenyl–Sepharose CL-4B Column

In the present work we describe a procedure for the purification of human pregnancy zone protein (PZP) from pooled late pregnancy plasma by using hydrophobic interaction chromatography (HIC) on a phenyl–Sepharose column. The HIC step allowed the complete isolation of haptoglobins and the partial separation of human α₂-macroglobulin (α₂-M) from a protein fraction containing PZP previously obtained by a DEAE-Sephacel chromatography. Pure and native PZP, with a recovery of nearly 25% and biological activity of protease-binding, was obtained by two definitive final steps consisting of zinc-chelate and size-filtration chromatographies. Moreover, we further present an alternative procedure for the purification of α₂-M from the same pregnancy plasma, based on the differential elution of PZP and α₂-M from the HIC. This purification step gave rise to a highly purified product with a recovery of 10%. This differential elution could be explained by differences in surface hydrophobicity observed between both proteins. In addition, considering the different hydrophobic properties exhibited by native PZP and PZP–protease complexes, HIC on phenyl–Sepharose column could also be used for separating both conformational states of PZP.     

用疏水色谱法复性并同时纯化重组人粒细胞-巨噬细胞集落刺激因子

目的：建立一种简单、快速复性并同时纯化大肠杆菌表达的重组人粒细胞一巨噬细胞集落刺激因子（rhGM-CSF）的方法。方法：研究rhGM-CSF在疏水色谱（HIC）上的复性和纯化机理,并对固定相和流动相进行选择和优化,包括固定相配基、流动相中盐的种类、流动相pH值、流动相中还原型谷胱甘肽（GSH）和氧化型谷胱甘肽（GSSG）的比例,以及流动相中尿素的浓度。结果：优化后的固定相为PEG600,流动相中的盐为（NH4）2SO4,流动相pH值为7．0,流动相中添加2．0mol／L尿素、1．8mmol／LGSH和0-3mmol／LGSSG。在优化条件下,HIC可使rhGM-CSF在分离纯化的同时得到复性,比活达1．58×10^7U／mg,纯度为95．7％,质量回收率为56．8％。结论：建立的疏水色谱复性和纯化工艺可简化操作步骤,缩短生产周期。     

Purification of a Penicillium citrinum lipase by chromatographic processes

A lipase from a wild strain of Penicillium citrinum was purified by ammonium sulphate precipitation, gel filtration chromatography on a Superose 6 column and hydrophobic interaction chromatography (HIC) on a Phenyl Superose column. The yield and purification factor were 15.2% and 379 fold, respectively. The gel filtration step was efficiently scaled-up in a Superose 6 preparative grade column and after this step, the lipase was recovered in the form of a high molecular weight aggregate. The partial disaggregation of the complex was achieved by HIC and elution with 1.0% (w/v) CHAPS. The lipase produced by Penicillium citrinum forms a dimmer of 63?000 Da, as determined by SDS-PAGE, and it accumulates in the fermentation broth as high molecular weight aggregates (>2?00?000 Da). The analysis of the dimmer showed two subunits with similar molecular weights (31?000–33?000 Da) and isoelectric points (4.8–5.0).