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.     

An alternative assay to hydrophobic interaction chromatography for high-throughput characterization of monoclonal antibodies

The effectiveness of therapeutic monoclonal antibodies (mAbs) is governed not only by their bioactivity, but also by their biophysical properties. Assays for rapidly evaluating the biophysical properties of mAbs are valuable for identifying those most likely to exhibit superior properties such as high solubility, low viscosity and slow serum clearance. Analytical hydrophobic interaction chromatography (HIC), which is performed at high salt concentrations to enhance hydrophobic interactions, is an attractive assay for identifying mAbs with low hydrophobicity. However, this assay is low throughput and thus not amenable to processing the large numbers of mAbs that are commonly generated during antibody discovery. Therefore, we investigated whether an alternative, higher throughput, assay could be developed that is based on evaluating antibody self-association at high salt concentrations using affinity-capture self-interaction nanoparticle spectroscopy (AC-SINS). Our approach is to coat gold nanoparticles with polyclonal anti-human antibodies, use these conjugates to immobilize human mAbs, and evaluate mAb self-interactions by measuring the plasmon wavelengths of the antibody conjugates as a function of ammonium sulfate concentration. We find that hydrophobic mAbs, as identified by HIC, generally show significant self-association at low to moderate ammonium sulfate concentrations, while hydrophilic mAbs typically show self-association only at high ammonium sulfate concentrations. The correlation between AC-SINS and HIC measurements suggests that our assay, which can evaluate tens to hundreds of mAbs in a parallel manner and requires only small (microgram) amounts of antibody, will enable early identification of mAb candidates with low hydrophobicity and improved biophysical properties.     

An alternative assay to hydrophobic interaction chromatography for high-throughput characterization of monoclonal antibodies

The effectiveness of therapeutic monoclonal antibodies (mAbs) is governed not only by their bioactivity, but also by their biophysical properties. Assays for rapidly evaluating the biophysical properties of mAbs are valuable for identifying those most likely to exhibit superior properties such as high solubility, low viscosity and slow serum clearance. Analytical hydrophobic interaction chromatography (HIC), which is performed at high salt concentrations to enhance hydrophobic interactions, is an attractive assay for identifying mAbs with low hydrophobicity. However, this assay is low throughput and thus not amenable to processing the large numbers of mAbs that are commonly generated during antibody discovery. Therefore, we investigated whether an alternative, higher throughput, assay could be developed that is based on evaluating antibody self-association at high salt concentrations using affinity-capture self-interaction nanoparticle spectroscopy (AC-SINS). Our approach is to coat gold nanoparticles with polyclonal anti-human antibodies, use these conjugates to immobilize human mAbs, and evaluate mAb self-interactions by measuring the plasmon wavelengths of the antibody conjugates as a function of ammonium sulfate concentration. We find that hydrophobic mAbs, as identified by HIC, generally show significant self-association at low to moderate ammonium sulfate concentrations, while hydrophilic mAbs typically show self-association only at high ammonium sulfate concentrations. The correlation between AC-SINS and HIC measurements suggests that our assay, which can evaluate tens to hundreds of mAbs in a parallel manner and requires only small (microgram) amounts of antibody, will enable early identification of mAb candidates with low hydrophobicity and improved biophysical properties.     

Purification of monoclonal antibodies from whole hybridoma fermentation broth by fluidized bed adsorption

To achive the coarse purification of a monoclonal antibody from whole hybridoma fermentation broth a fluidized bed cation exchange process was used. The procedure consisted of application of the crude sample and washing of the bed in a fluidized mode and elution in a fixed bed mode. A completely clarified eluate was obtained with purification factors between 4 and 8 and a concentration of the desired product (monoclonal antibody) by a factor of more than 3 was achived. Thus, a combination of the three early steps of the downstream process clarification, concentration and coarse purification was possible. Two different materials were tested: a commercially available agarose-based matrix (Stream-line-SP), and a self-derivatized material based on controlled-pore glass (Bioran). Initial experiments were performed to describe the fluidization of the glass material. Comparison with the agarose material showed several differences, the agarose matrix allowing liquid flow closer to plug flow than the glass material. Increased backmixing in the liquid phase was detected when fluidizing the glass adsorbent compared with the agarose-based matrix. Despite this fact, comparison of the two materials with respect to antibody binding and elution demonstrated a similar performance. (c) 1995 John Wiley & Sons, Inc.     

Increase in synthesis of human monoclonal antibodies by transfected Sp2/0 myeloma mouse cell line under conditions of microgravity

Microgravity can influence cell growth and function. A transfected Sp2/0 myeloma cell line P3A2 producing a human IgG1 anti-TNF monoclonal antibody was cultivated in static culture, spinner flasks and simulated microgravity using a rotating wall vessel bioreactor. Microgravity significantly decreased cell growth (from 1.7×10⁶ to 7.9×10⁵ cells/ml), but facilitated the synthesis of antibodies, (1.8, 1.3 and 0.5 g of anti-TNF hmAb per 10⁶ viable cells for cells cultivated under microgravity, in spinner flasks and static cultures, respectively). The results suggest that microgravity could be applied to improve the specific productivity of cell lines producing potentially important therapeutic proteins.     

Purification of monoclonal antibodies derived from transgenic goat milk by ultrafiltration

With the goal of recovering heterologous immunoglobulin (IgG), which comprises 10-15% of the total proteins, from transgenic goat milk at 80% yield and 80% purity, we have developed and tested a two-step membrane isolation and purification process. In the first step, reported earlier by Baruah and Belfort, microfiltration was used to fractionate the milk proteins and recover > 90% of the original IgG at a purity of about 15-20% in the permeate stream. Here, we focus on ultrafiltration (UF) to increase the purity of the target protein to 80%, while maintaining a relatively high IgG yield (80%). Tangential flow UF experiments in diafiltration mode were conducted with 100 kDa cellulosic membranes to evaluate the optimal pH, ionic strength, and uniform transmembrane pressure (TMP). The TMP was kept uniform by permeate circulation in co-flow mode. The traditional approach of conducting the UF process close to the pI of the predominant whey proteins (15-40 kDa, pI 5.2), to transmit these proteins while retaining heterologous IgG (155 kDa), could not be applied here because of precipitation of residual casein at pH values lower than 8.5. Instead, the packing characteristics of the cake layer on the membrane wall, as elucidated in the Aggregate Transport Model presented by Baruah et al. was utilized to achieve a selectivity of > 15, which was sufficient to meet the stated goals of purity and yield for this difficult separation. This combined process is expected to reduce the load on subsequent purification and polishing steps for eventual therapeutic use.     

Influence of osmolarity and pH increase to achieve a reduction of monoclonal antibodies aggregates in a production process

Anti PSA monoclonal antibodies for diagnostic use were produced in an in vitro system. After purification using Protein G affinity chromatography a percentage of about 10% of antibody aggregates remained. The use of monoclonal antibodies containing aggregates as a capture antibody in a diagnostic kit reduces the performance of the test making it often unacceptable. The aggregates could be eliminated using gel filtration chromatography but, in that way, the final recovery of the whole production process was only about 50%. Aggregation is favoured when the working pH is near to the isoelectric point of the antibody. We varied the culture medium composition, modifying pH and osmolarity. We tested different values of pH and osmolarity: 7.1, 7.5, 8.0, 8.5 for pH, and 300, 340, 367, 395 mOsm/kg H2O for osmolarity. By modification of the cell culture medium we obtained a significant decrease of monoclonal antibody aggregates in the production cycle. In this way we achieved higher recovery rate and could avoid gel filtration polishing step. The experiments were performed in two stages: first in culture flasks changing one parameter in each experiment, and then in spinner bottle using the best conditions obtained in the first stage. During scale up we used the modifications achieved from the experiment showed in this paper in our production by hollow fibre bioreactor with positive results.     

Weak partitioning chromatography for anion exchange purification of monoclonal antibodies

Weak partitioning chromatography (WPC) is an isocratic chromatographic protein separation method performed under mobile phase conditions where a significant amount of the product protein binds to the resin, well in excess of typical flowthrough operations. The more stringent load and wash conditions lead to improved removal of more tightly binding impurities, although at the cost of a reduction in step yield. The step yield can be restored by extending the column load and incorporating a short wash at the end of the load stage. The use of WPC with anion exchange resins enables a two-column cGMP purification platform to be used for many different mAbs. The operating window for WPC can be easily established using high throughput batch-binding screens. Under conditions that favor very strong product binding, competitive effects from product binding can give rise to a reduction in column loading capacity. Robust performance of WPC anion exchange chromatography has been demonstrated in multiple cGMP mAb purification processes. Excellent clearance of host cell proteins, leached Protein A, DNA, high molecular weight species, and model virus has been achieved.     

Purification of monomeric mAb from associated aggregates using selective desorption chromatography in hydroxyapatite systems

Selective desorption on ceramic hydroxyapatite (CHT) was implemented for the purification of monomeric monoclonal antibody (mAb) from associated aggregates and other post-protein A step impurities. A robotic liquid handling system was employed to carry out a parallel batch screen of selective desorbents on a post-protein A step mAb mixture. The effect of different phosphate concentrations was also investigated. Selective batch separations were achieved between monomeric mAb and associated aggregates/impurities. The batch screen results also established optimal mobile phase conditions for each selective desorbent. These initial batch results were then used to guide column separations, and baseline separation of monomeric mAb from associated aggregates and impurities was achieved, validating the screening results. Selective desorption also resulted in improved separations on CHT, with 100% yield of pure monomeric mAb as compared to 61% and 79%, respectively, for conventional linear and step gradient operations. This proof of concept study demonstrates selective desorption on CHT as an effective separation technique for the purification of monomeric mAb from associated aggregates and other post-protein A step impurities in a single process step.     

Select host cell proteins coelute with monoclonal antibodies in protein A chromatography

The most significant factor contributing to the presence of host cell protein (HCP) impurities in Protein A chromatography eluates is their association with the product monoclonal antibodies (mAbs) has been reported previously, and it has been suggested that more efficacious column washes may be developed by targeting the disruption of the mAbs-HCP interaction. However, characterization of this interaction is not straight forward as it is likely to involve multiple proteins and/or types of interaction. This work is an attempt to begin to understand the contribution of HCP subpopulations and/or mAb interaction propensity to the variability in HCP levels in the Protein A eluate. We performed a flowthrough (FT) recycling study with product respiking using two antibody molecules of apparently different HCP interaction propensities. In each case, the ELISA assay showed depletion of select subpopulations of HCP in Protein A eluates in subsequent column runs, while the feedstock HCP in the FTs remained unchanged from its native harvested cell culture fluid (HCCF) levels. In a separate study, the final FT from each molecule's recycling study was cross-spiked with various mAbs. In this case, Protein A eluate levels remained low for all but two molecules which were known as having high apparent HCP interaction propensity. The results of these studies suggest that mAbs may preferentially bind to select subsets of HCPs, and the degree of interaction and/or identity of the associated HCPs may vary depending on the mAb.     

Paper-PEG-based membranes for hydrophobic interaction chromatography: purification of monoclonal antibody

This article discusses the preparation of novel Paper-PEG interpenetrating polymer network-based membranes as inexpensive alternative to currently available adsorptive membranes. The Paper-PEG membranes were developed for carrying out hydrophobic interaction membrane chromatography (HIMC). PEG is normally very hydrophilic but can undergo phase separation and become hydrophobic in the presence of high antichaotropic salt concentrations. Two variants of the Paper-PEG membranes, Paper-PEG 1 and Paper-PEG 2 were prepared by grafting different amounts of the polymer on filter paper and these were tested for their hydraulic properties and antibody binding capacity. The better of the two membranes (Paper-PEG 1) was then used for purifying the monoclonal antibody hIgG1-CD4 from simulated mammalian cell culture supernatant. The processing conditions required for purification were systematically optimized. The dynamic antibody binding capacity of the Paper-PEG 1 membrane was about 9 mg/mL of bed volume. A single step membrane chromatographic process using Paper-PEG 1 membrane gave high monoclonal antibody purity and recovery. The hydraulic permeability of the paper-based membrane was high and was maintained even after many runs, indicating that membrane fouling was negligible and the membrane was largely incompressible.     

Purification of factor X by hydrophobic interaction chromatography

Human factor X has been purified to homogeneity by hydrophobic interaction chromatography on phenyl-sepharose. The coagulation protein did not interact with the resin in the presence of 2–3 M NaCl whereas contaminants were retained. This single purification step, in conjunction with classical purification strategies, is a powerful tool in generating high purity factor X and is based on resins which are readily available.     

Mouse monoclonal antibodies specific for endothelial cells

Summary Balb/c mice were immunized with a human endothelial cell pool. Spleen cells were then fused with a NS-0 hybridoma cell line. A number of hybridomas secreted antibodies that reacted with the immunizing endothelial cell pool as well as with every other tested umbilical cord vein~derived human endothelial cell. These monoclonal antibodies also stained pig, rabbit and ox aortic endothelial cells indicating their specificity for this cell type. Five of 16 monoclonal antibodies additionally reacted with human fibroblasts (HFIB). The produced monoclonal antibodies did not recognize FVIIIRAG or MHC determinants. They can therefore be regarded as additional and reliable markers for endothelial cells in vitro.     

单克隆抗体亲和层析法纯化重组溶葡萄球菌酶

溶葡萄球菌酶能够特异性杀灭金黄色葡萄球菌且不易产生耐药性, 有望成为治疗葡萄球菌属细菌引发感染的特效药物。为获得高纯度的重组溶葡萄球菌酶以达到药用标准, 本研究构建了一种以重组溶葡萄球菌酶单克隆抗体为配体的亲和层析纯化方法。纯化后的重组溶葡萄球菌酶纯度大于95%, 得率大于90%, 即使重复使用30多次, 纯化效率不变。且经比色法鉴定纯化后的重组溶葡萄球菌酶仍具有良好的活性。该方法步骤简单, 纯化效果好, 为生产高纯度重组溶葡萄球菌酶奠定了基础。     

金属螯合亲和层析法纯化抗乙肝核心抗原单克隆抗体

采用金属螯合亲和层析法,纯化了小鼠腹水来源的抗乙肝核心抗原单克隆抗体,对上样缓冲液的pH和离子强度、洗脱液种类和洗脱方式进行优化。结果表明,采用降低pH分步洗脱时,最佳上样缓冲液为pH8.0,20mmol/LPB+0.5mol/LNaCl,抗体在pH5.0被洗脱下来,抗体回收率80%,纯度85%。采用咪唑浓度梯度洗脱时,最佳的上样缓冲液为pH8.0,20mmol/LPB+5mmol/L咪唑,抗体纯度大于95%,回收率65%;在上样缓冲液中不添加NaCl而添加少量的咪唑,更有利于抗体分离。以上洗脱方式都能较好地保持mAb的生物学活性,为该抗体的应用提供了必要的实验基础。     

Industrial production of monoclonal antibodies and therapeutic proteins by dialysis fermentation

A novel and powerful fermentation method is reported for the large-scale growth of mammalian cells and their secreted products. The system described illustrates many of the advantages of conventional batch fermentation processes but in addition has been shown to yield cell densities in excess of 1×10⁷ cells/ml with concomitant increase in product concentration.Abbreviations MAb Monoclonal Antibody - STR Stirred Tank Reactor - FBS Foetal Bovine Serum     

Immunological approach to characterize proacrosin and various acrosin forms in boar and man by monoclonal antibodies

Three different monoclonal rat antibodies, Acr1, Acr2, and Acr3, have been established against boar proacrosin. They are shown by enzyme-linked immunosorbent and immunoblot assays to react with boar proacrosin and several different acrosin molecules derived therefrom during activation. The epitopes detected by the three antibodies are different from each other, one being highly sensitive to reduction and periodate treatment. The antibodies crossreact with various proacrosin and acrosin molecules derived from human sperm extract; they also show indirect immunofluorescent staining of the acrosomal region of ejaculated sperm from normal men but fail to react with round-headed spermatozoa.     

Serological study of yeast killer toxins by monoclonal antibodies

Yeast killer toxins coded by determined and undetermined killer plasmids or presumptive nuclear gene(s) in various genera (Saccharomyces, Kluyveromyces, Pichia and Candida) have been serologically investigated by a monoclonal antibody (KT4), produced against the yeast killer toxin of Pichia (Hansenula) anomala UCSC 25F. Double immunodiffusion with the killer toxins as antigens and indirect immunofluorescence on whole cells of the corresponding killer yeast have been used. In both the serological procedures, monoclonal antibody KT4 proved to be reacting only with the killer toxins and the whole cells of yeasts belonging to the genus Pichia.     

Biotyping of pathogenic fungi by the killer system and with monoclonal antibodies

Biotyping of pathogenic yeasts and hyphomycetes based on their suceptibility to selected killer yeasts and their reactivity with monoclonal antibodies are described. Both methods were used to differentiate fungi isolated from patients providing valuable epidemiological information on mycotic infections. The functional biotyping obtained with the two systems and the conventional auxenographic biocoding approaches commercially available for opportunistic yeasts are comparatively evaluated. The potential for biotyping of industrial fungal isolates is also discussed.     

Efficient bispecific monoclonal antibody purification using gradient thiophilic affinity chromatography

Bispecific monoclonal antibodies (bsMAbs), due their unique design, have a wide range of potential applications in immunodiagnostics and immunotherapy. One of the major limitations for the use of bsMAbs produced by hybrid–hybridomas is the concomitant production of parental monospecific antibodies. The relative amount of bsMAb secreted may vary between different hybrid–hybridomas. Hence, the purification of the desired bispecific molecule from other forms is crucial. Current purification methods include anion-exchange, HPLC on different matrices, and dual affinity methods. Most of those methods include multiple steps and have limitations on the purity or yield of the desired species. We report here a simple single-step purification method, using inexpensive thiophilic chromatography. This new method can potentially be scaled up, for industrial proposes. Finally, based on the amino acid sequences and assembly of the two heavy chains we attempt to explain the possible mechanism by which thiophilic chromatography was able to resolve the bsMAbs from the monospecific species.