Continuous annular chromatography: General characterization and application for the isolation of recombinant protein drugs

Isolation of recombinant protein drugs from cell culture supernatant is usually performed in batch mode, even if the fermentation process itself is continuous. As a novel approach, continuous separation techniques like continuous annular chromatography (CAC) can be used for continuous isolation. The potential of CAC for industrial application is demonstrated by continuous isolation of rFVIII from cell culture supernatant in pilot scale (i.e., 144-288 l/day). Thirty-fold concentration can be achieved at 94% yield, while purity is increased 3-5-fold. For this a batch direct feed ion exchange chromatography method was adapted to a commercial preparative CAC system (P-CAC). A headspace loading technique was used to maximize the concentration factor, while buffer incompatibility problems were addressed by a specifically modified inlet geometry. To allow sterile on-line coupling to FVIII-producing perfusion fermenters, an autoclavable pilot scale P-CAC prototype was developed. General characterization of P-CAC revealed a current limitation of the technology, i.e., variations in the outlet flow rates of up to +/-20%. These flow variations are shown to be caused mainly by a nonuniform annular resin bed and in turn result in "peak wobbling," i.e., the slight variation of peak position (up to +/-4 degrees ) and shape (e.g., A(s) = 0.9-1.4) as a specific function of column position. Some additional peak broadening, although less significant, is caused by a "peak oscillation" effect that results from the necessary segmentation of flow into discrete outlets. Both effects are only measurable if peaks are either monitored continuously or at least measured at multiple column positions. For isolation processes, these nonideal flow phenomena mean that more outlet streams have to be collected in order to achieve maximum yield and thus the achievable concentration factor is somewhat lower than the theoretical maximum.     

Expanded bed protein A affinity chromatography of a recombinant humanized monoclonal antibody: process development, operation, and comparison with a packed bed method.

We show that expanded bed protein A affinity chromatography using Streamline rProtein A media is an efficient method for purifying a recombinant humanized monoclonal antibody from unclarified Chinese hamster ovary cell culture fluid and that it provides purification performance comparable to using a packed bed. We determined that the dynamic capacity of the expanded bed media is related to flow rate (measured in column volumes per hour) by a power function, which allows a high capacity at a low flow rate. At 250 cm h-1 with a 25 cm bed height (10 column volumes h-1), the dynamic capacity is 30 g l-1. The yield and purity (measured by the amount of host cell proteins, DNA, SDS-PAGE, and turbidity) of the antibody purified by expanded bed is comparable to the yield and purity obtained on a standard packed bed method using Prosep A media.     

Evaluation of commercial chromatographic adsorbents for the direct capture of polyclonal rabbit antibodies from clarified antiserum

We have carried out a rigorous evaluation of eight commercially available packed bed chromatography adsorbents for direct capture and purification of immunoglobulins from clarified rabbit antiserum. Three of these materials featured rProtein A (rProtein A Sepharose Fast Flow, Mabselect, Prosep rProtein A) as the affinity ligand, and differed from one another primarily with respect to the underlying base matrix. The remaining five matrices comprised various synthetic low molecular weight ligands immobilised on hydrophilic porous supports and these included: MEP HyperCel, MabSorbent A1P, MabSorbent A2P, FastMabsA and Kaptiv-GY. The general experimental approach taken was to sequentially challenge packed beds of each matrix with a series of different strengths of a clarified antiserum; beginning with the weakest and ending with the strongest. Marked differences in performance (principally evaluated on the basis of dynamic binding capacity, recovery, and purity) were obtained, which allowed clear recommendations concerning the choice of adsorbents best suited for antibody capture from rabbit antisera, to be made.     

Production and purification of a chimeric monoclonal antibody against botulinum neurotoxin serotype A

Production of recombinant antibodies against botulinum neurotoxin is necessary for the development of a post-exposure treatment. CHO-DG44 cells were transfected with a plasmid encoding the light and heavy chains of a chimeric monoclonal antibody (S25) against botulism neurotoxin serotype A. Stable cell lines were obtained by dilution cloning and clones were shown to produce nearly equivalent levels of light and heavy chain antibody by an enzyme-linked immunosorbent assay (ELISA). In suspension culture, cells produced 35 μg/ml of chimeric antibody after 6 days, corresponding to a specific antibody productivity of 3.1 pg/cell/day. A method for the harvest and recovery of an antibody against botulism neurotoxin serotype A was investigated utilizing ethylenediamine-N,N′-tetra(methylphosphonic) acid (EDTPA) modified zirconia and MEP-hypercel, a hydrophobic charge interaction chromatography resin. Purification of the S25 antibody was compared to that achieved using rProtein A–Sepharose Fast Flow resin. After the direct load of culture supernatant, analysis by ELISA and gel electrophoresis showed that S25 antibody could be recovered at purities of 41 and 44%, from the EDTPA modified zirconia and MEP-hypercel columns, respectively. Although the purity obtained from each of these columns was low, the ability to withstand high column pressures and nearly 90% recovery of the antibody makes EDTPA modified zirconia well suited as an initial capture step. Combining the EDTPA modified zirconia and HCIC columns in series resulted in both purity and final product yield of 72%.     

Hyphenation of multi-dimensional chromatography and mass spectrometry for the at-line-analysis of the integrity of recombinant protein drugs

A robust tool is proposed for the rapid at-line verification of the identity and integrity of (recombinant) proteins, namely the hyphenation of multidimensional chromatography and mass spectrometry (MS). A recombinant human antibody produced in Chinese hamster ovary cells is taken as pertinent example. The recombinant human antibody is first captured from the production environment by affinity chromatography (rProtein A, isolation/concentration of the target molecule) and automatically transferred to an enzyme reactor (immobilized trypsin column) for digestion, thereby yielding different peptides corresponding to the protein sequence. The peptides are then separated on a reversed-phase column before being analyzed and identified by MS. This step does not require a fine resolution since the mass spectrometer can identify a variety of substances at the same time. The results are then analyzed in silico with suitable bio-informatic tools. When the gene sequence of the protein product is known, proteolytic cleavages can be predicted and the exact mass and hence the amino acid sequence of each peptide can thereby be deduced. Fitting experimental data and reference peptide sequences then provides important information about the integrity of the protein and more particularly about its sequence. In our case, the integrity of 45% of the light and 75% of the heavy chain sequences of the antibody could be verified within minutes.     

抗甲肝病毒基因工程单抗分离纯化与鉴定

为克服血源免疫球蛋白制品的不足,开发了抗甲肝病毒基因工程单克隆抗体anti-HAV IgG。用无血清培养基培养rCHO工程细胞株,上清液经过rProtein A SFF亲和层析→脱盐→离子交换层析→超滤换液纯化后,所得anti-HAV IgG纯度达99%以上,比活性约100IU/mg,anti-HAV IgG活性回收率40%。所纯化的anti-HAV IgG分子量150kD,等电点8.4～9.3。免疫印迹实验证实anti-HAV IgG为人源全抗体分子。亲和层析介质rProtein A SFF确实存在亲和配基脱落问题,但通过后续纯化步骤可有效除去。在亲和层析过程中加入高盐清洗步骤,可有效降低宿主DNA残留量水平。对样品中自由巯基含量进行了测定,认为非还原电泳图谱中低分子量条带是由于抗体分子内存在自由巯基引起。用该工艺制备的anti-HAV IgG各项纯度检测指标均达到我国对基因工程产品的质量要求。     

Interaction of mammalian cell culture broth with adsorbents in expanded bed adsorption of monoclonal antibodies

The interaction of a mammalian cell culture broth with two commercially available adsorbents for the use in expanded bed adsorption (EBA) has been studied. A cation exchange resin (Streamline SP) and an affinity adsorbent (Streamline rProtein A) were compared with regard to adsorption of hybridoma cells during sample application as well as potential cell damage. The results showed that hybridoma cells interact significantly with an expanded bed of cation exchange adsorbents but not with the Protein A adsorbent. After application of 17–20 sedimented bed volumes a saturation of the Streamline SP resin with cells was noted. With both adsorbents no measurable cell damage was found and IgG₁ was recovered in approximately 95% yield. The capacity for IgG₁ adsorption at 3% breakthrough was 2.7 mg IgG₁/ml Streamline rProtein A at a constant fluid velocity of 380 cm/h and 1.0 mg IgG_l/ml Streamline SP at 215–240 cm/h fluid velocity.     

Heterogeneous profiles of a factor that renders neutrophils cytotoxic obtained from a concanavalin A-stimulated spleen cell culture in partial purification process

Concanavalin A (Con A)-stimulated rat spleen cells were cultured in a serum-free conditioned medium. This culture supernatant contained a certain factor(s) that renders neutrophil cytotoxic for various tumor cells. The factor was tentatively termed neutrophil-activating factor (NAF). Rat NAF was partially purified from the serum-free culture supernatant by using ion exchange chromatography of DEAE-Sephadex A-50, gel filtration of Sephadex G-100, and affinity chromatography of Con A-Sepharose 4B. NAF activity was eluted in broad fractions by the ion exchange chromatography and the gel filtration. Moreover, on the Con A column, some NAF activities were bound to the column, but other activities passed through the column. These results showed the heterogeneity or polydispersity of NAF activity in both molecular size and charge-based separation properties. Monoclonal antibodies were produced by fusing BALB/c myeloma cells (P3-X63 Ag8.653) with spleen cells from syngeneic mice immunized with partially purified NAF (pNAF) obtained from the gel filtration. Absorbent beads which were linked with one monoclonal antibody (ANAF-10) partially absorbed NAF activity from supernatants of a Con A-stimulated spleen cell culture. Further purification of pNAF was performed with the use of affinity chromatography of ANAF-10-linked Sepharose. Through these procedures, the NAF activity was concentrated about 10,000-fold. Heterogeneity of NAF activity, however, did not disappear in even this affinity chromatography. On the other hand, 125I-labeled material of the final product migrated to one major band corresponding with an m.w. of about 20,000 as determined by SDS-PAGE analysis, and NAF activity was detected in the same band.     

Antibody Binding Heterogeneity of Protein A Resins

Protein A affinity chromatography is a core unit operation in antibody manufacturing. Nevertheless, there is not enough understanding of in‐column antibody adsorption in the Protein A capture step. This work aims to investigate in situ the establishment of an antibody (trastuzumab) layer during Protein A chromatography both in terms of energetic contributions and uptake kinetics. Flow microcalorimetry is employed as a technique with an in situ operating detector, which provides an understanding of the thermodynamics of the adsorption process. In addition, the antibody uptake rate is also investigated in order to establish a correlation between its diffusion on the stationary phase and the associated thermodynamics. Two resins with different particle size, intraparticle porosity, and a Protein A ligand structure are studied: the synthetically engineered B‐domain tetrameric MabSelect SuRe and the synthetically engineered C‐domain hexameric TOYOPEARL AF‐rProtein A HC. The uptake rate follows a pore diffusion model at low equilibrium time, showing a slower diffusivity after a certain time because of the heterogeneous binding nature of these two resins. In addition, the microcalorimetric studies show that adsorption enthalpy is highly favourable at low isotherm concentrations and evolves toward an equilibrium with increasing surface concentration. These data suggest that the relationship between adsorption enthalpy and the establishment of the antibody layer in the Protein A chain is consistent with heterogeneous adsorption.     

H1亚型猪流感病毒抗体间接ELISA检测方法的建立及其应用

为建立H1亚型猪流感病毒抗体检测方法,扩增了H1N1亚型猪流感病毒流行株的血凝素基因HA1部分,构建原核表达载体pET30a-HA1,并转化大肠杆菌BL21表达重组蛋白。对重组蛋白包涵体进行变性、复性和Ni-NTA亲和层析纯化。以纯化后的蛋白作包被抗原,建立间接ELISA检测方法。利用该检测方法检测了2008?2009年采集的猪血清785份,阳性率为15.54％,不同省份的阳性率存在差异 (8％~47％)。以IDEXX相关试剂盒检测结果作为参照,该方法的诊断特异性达到91％,诊断敏感性达到95％。     

增殖细胞核抗原蛋白在Spodoptera frugiperda昆虫细胞中的表达及纯化

目的:利用昆虫细胞表达系统生产重组的人增殖细胞核抗原(proliferating cell nuclear antigen,PCNA),并进行纯化和抗体结合特性鉴定。方法:以HeLa细胞逆转录的cDNA为模板,扩增人PCNA基因,并插入杆状病毒载体AcMNPV。利用昆虫细胞得到PCNA基因的重组杆状病毒。病毒感染细胞表达蛋白,联合镍柱亲和层析和离子交换层析获得高纯度的重组人PCNA蛋白。ELISA法测定抗体结合特异性。结果:以HeLa细胞cDNA为模板得到的基因序列同GenBank的人PCNA基因序列一致。草地贪夜蛾细胞(Spodoptera frugiperda,Sf9)表达重组人PCNA(recombinant human PCNA,rPCNA)的最佳感染值(MOI)和感染时间分别为0.05h和144h。rPCNA的产量高达110mg/L细胞,纯度95%。间接ELISA法检测抗体结合特性,rPCNA的敏感性和特异性分别为93.3%和85.0%。结论:建立了rPCNA的表达和纯化方法,获得了高效表达、高度抗体结合特异性的PCNA蛋白,该蛋白质能进一步开发为PCNA相关疾病的体外诊断试剂盒,具较大的应用价值。     

Maximizing productivity of chromatography steps for purification of monoclonal antibodies

The large scale production of monoclonal antibodies presents a challenge to design efficient and cost effective downstream purification processes. We explored a two stage resin screening approach to identify the best candidates to be utilized for the platform purification of monoclonal antibodies. The study focused on commercially available affinity resins including Protein A, mimetic and mixed-mode interaction resins as well as ion exchangers used in polishing steps. An initial screening using pure proteins was followed by a final screening where selected resins were utilized for the purification of MAbs in complex mixtures. Initial screenings aimed to measure the theoretical upper limit for dynamic binding capacity (DBC) at 1% breakthrough and productivity. We confirmed that DBC of affinity, mimetic and mixed-mode resins was a strong function of the linear velocity used for loading. Productivities >27 g/(L-h), were obtained for rProtein A FF, Mabselect and Prosep rA Ultra at 2 min residence time. For the cation exchangers, we identified UNOsphere S and Fractogel SO(3) as the best candidates for our purification based on DBC. For anion exchangers operated in flowthrough mode, Q Sepharose XL and UNOsphere Q were selected from the initial screening based on DBC and resolution of IgG from BSA. Finally, a three step purification scheme was implemented using the selected affinity and ion exchangers for the purification of IgG from complex feedstocks. We found that Mabselect followed by UNOsphere Q and UNOsphere S provided the best purification scheme for our applications based on productivity.     

Elevated level of hyaluronic acid binding protein in diabetic rats.

Hyaluronic acid binding protein (HABP), an extracellular matrix glycoprotein which interacts specifically with hyaluronic acid (HA) has been purified to homogeneity by HA affinity chromatography. Antibody was raised against it and the specificity of antibody towards HABP was confirmed by western blot analysis. A specific and sensitive assay method has been developed adopting solid phase non-competitive double sandwich method of ELISA. This new assay method enabled us to determine the levels of HABP in different tissue extracts of normal, diabetic and reverse diabetic rats. A significant increase in the levels of HABP was observed in diabetic animals, which however attained normal levels with insulin treatment.     

Purification to apparent homogeneity of the somatostatin receptor of the human cell line HGT-1 of gastric origin

This communication reports the isolation and the purification of the gastric somatostatin receptor from the human cell line HGT-1. The receptor has been extracted from the cell membrane by Triton X 100, and a monoclonal antibody to this was prepared. A series of affinity chromatographies (Sepharose-antibody and Sepharose-somatostatin-14) and a final purification by steric exclusion on high performance liquid chromatography columns (HPLC) allowed us to obtain a fraction enriched 20,000 fold in 125I-Tyrll-somatostatin-14 specific binding (apparent dissociation constant: 7.6 x 10(-8) M). This fraction corresponded to a molecular mass of about 90 kDa (in presence of detergent) and to a maximal binding capacity of more than 10,000 pmol/protein. It therefore has a theoretical homogeneity close to 100%.     

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.     

抗 CD20融合蛋白在 CHO 细胞中的表达及其纯化与鉴定

目的：构建CD20胞外区与Igβ胞外区和人IgG1 Fc融合基因的表达载体,并在CHO细胞中表达。方法与结果：根据已知的IgM的CH2区域和Igp胞外区序列,分别设计PCR引物并进行PCR扩增,然后用重叠PCR法扩增得到900bp的Igp-CH2序列,插入本实验室构建的pIRIS-EGFP-Fc载体,转化大肠杆菌,得到pIRIS-Igβ-CH2-Fc重组质粒,将其转染CHO-K1细胞,在G418抗性培养基中培养,荧光显微镜观察结合ELISA法筛选高表达细胞系,细胞系扩大培养后,通过亲和层析rProteinA柱纯化得到纯度融合蛋白,SDS-PAGE显示目的蛋白去糖基化后,相对分子质量约为42×10^3。结论：得到了Igβ-CH2-Fc重链抗体样分子,并鉴定为糖蛋白;须进一步对所得蛋白的生物学活性进行检测,验证其是否能够通过胞外区蛋白定位于B细胞淋巴瘤细胞表面对B淋巴瘤细胞进行杀伤。     

Visualisation of hyaluronan and hyaluronan-binding proteins within ovine vertebral cartilages using biotinylated aggrecan G1-link complex and biotinylated hyaluronan oligosaccharides

The aim of this study was to localise hyaluronan (HA)-binding proteins (HABPs) in ovine vertebral tissues using biotinylated HA oligosaccharides (bHA oligos) as novel affinity probes and to compare this with the distribution of tissue HA visualised using biotinylated aggrecan G1 domain-link protein complex. The bHA oligos, with a size of 6-18 disaccharides were prepared by partial digestion of HA with ovine testicular hyaluronidase, labelled with biotin hydrazide and purified by a combination of aggrecan G1 domain and avidin affinity chromatography. Hyaluronan and HABPs were both prominent pericellular components of hypertrophic cells of the vertebral epiphyseal growth plate and enlarged cells in the cartilaginous end plate of the disc. The bHA oligo probe also visualised HABPs intracellularly in hypertrophic cells, which also contained intracellular HA. Monolayer cultures of ovine annulus fibrosus and nucleus pulposus cells rapidly internalised the bHA oligo affinity probe which was subsequently visualised by indirect fluorescence using avidin-FITC, to cytoplasm and discrete nuclear regions. The results indicate that the abundant pericellular and intracellular HA associated with cartilaginous cells in the vertebral tissues is colocalised with HABPs. The bHA oligo affinity probe may have further applications in investigations of intracellular HABPs, HA endocytosis and the roles they play in cellular regulatory processes.     

Purification and characterization of monoclonal antibodies against the free α-subunit of human chorionic gonadotrophin

Monoclonal antibodies (Mabs) against human chorionic gonadotropin hormone (hCG) were raised by hybridoma technology using Sp2/0 myeloma cells as fusion partner. Sixty-five percent of the total culture wells exhibited hybrid growth and 8% of the total wells (13 culture wells) contained anti-hCG secreting hybrids. A positive hybrid cell line secreting antibodies against the free alpha-subunit of hCG was cloned twice by limiting dilution method and eighty four clones were obtained that secreted monoclonal antibodies anti-alpha hCG. One of these hybridoma clones (1C4) secreting monoclonal antibodies against the free alpha-subunit of hCG was selected for purification and characterization purposes. This hybridoma cell line secreted monoclonal antibodies of IgG1 subclass, which were purified by affinity chromatography on Protein A Sepharose CL-4B column with a final relative recovery of antibody activity of 75% and a purification factor of about 12. The purified preparation was analyzed by SDS-PAGE, native PAGE, and IEF. Specificity studies of this Mab revealed that it recognized specifically an epitope on the free alpha-subunits of hCG, FSH, LH, and TSH as determined by enzyme immunoassays. On the other hand, this Mab exhibited crossreactivity with other pituitary hormones either as free subunits or intact molecules as follows: alpha hCG 100%; intact hCG 1.8%; beta hCG 0.14%; alpha FSH 24.5%; intact FSH 0.8%; beta FSH 0.09%; alpha LH 20.5%; intact LH 0.9%; beta LH 0.08%; alpha TSH 50.5%; intact TSH 3.7%; beta TSH 0.07%; The affinity constant (K) of this Mab with respect to free alpha-subunit of hCG was found to be 1.5 x 10(7) I/mol as determined by the simple antibody dilution analysis method.     

Lymphoblastoid cell-produced immunoglobulins: preparative purification from culture medium by hydroxylapatite chromatography

Hydroxylapatite (HA) is a chromatography matrix capable of separating nucleic acid as well as protein species. HA adsorbs biomolecules as a function of the extent and distribution of their surface charge. HA has been evaluated for its ability to differentially retain immunoglobulin molecules, which are planar relative to the generally globular serum proteins, particularly albumin, contained in tissue culture medium. HA chromatography provides a single-step method to purify and concentrate immunoglobulin proteins secreted by lymphoblastoid cells into culture medium from the vast excess of serum proteins used to supplement the medium. A human lambda light-chain protein was recovered in 5% of the applied volume of medium, and was separated from 95% of the total protein. More than 75% of a hybridoma-produced complete immunoglobulin was recovered essentially free of serum protein contamination. HA appears to provide a valuable alternative chromatographic medium for the purification of immunoglobulin proteins secreted by lymphoblastoid cells.