Optimized signal peptides for the development of high expressing CHO cell lines

Recombinant biotherapeutic proteins such as monoclonal antibodies are mostly produced in Chinese hamster ovary (CHO) cells and pharmaceutical companies are interested in an appropriate platform technology for the development of large‐scale production processes. A major aim of our study was therefore to improve the secretion efficiency of a recombinant biotherapeutic antibody by optimizing signal peptides. Reporter molecules such as gaussia and vargula luciferase or secreted alkaline phosphatase are frequently used to this end. In striking contrast, we used a biotherapeutic antibody that was fused to 16 different signal peptides during our study. In this way, the secretion efficiency of the recombinant antibody has been analyzed by transient expression experiments in CHO cell lines. Compared to the control signal peptide, it was not possible to achieve higher efficiencies with signal peptides derived from a variety of species or even natural immunoglobulin G signal peptides. The best results were obtained with natural signal peptides derived from human albumin and human azurocidin. These results were confirmed by fed‐batch experiments with stably transfected cell pools, in which cell‐specific productivities up to 90 pg cell^?1 day^?1 and product concentrations up to 4 g L^?1 could be determined using the albumin signal peptide. Finally, the applicability of the identified signal peptides for both different antibodies and non‐antibody products was demonstrated by transient expression experiments. In conclusion, it was found that signal peptides derived from human albumin and human azurocidin are most appropriate to generate cell lines with clearly improved production rates suitable for commercial purposes in a product‐independent manner. Biotechnol. Bioeng. 2013; 110: 1164–1173. © 2012 Wiley Periodicals, Inc.     

Cleavage efficient 2A peptides for high level monoclonal antibody expression in CHO cells

Linking the heavy chain (HC) and light chain (LC) genes required for monoclonal antibodies (mAb) production on a single cassette using 2A peptides allows control of LC and HC ratio and reduces non-expressing cells. Four 2A peptides derived from the foot-and-mouth disease virus (F2A), equine rhinitis A virus (E2A), porcine teschovirus-1 (P2A) and Thosea asigna virus (T2A), respectively, were compared for expression of 3 biosimilar IgG1 mAbs in Chinese hamster ovary (CHO) cell lines. HC and LC were linked by different 2A peptides both in the absence and presence of GSG linkers. Insertion of a furin recognition site upstream of 2A allowed removal of 2A residues that would otherwise be attached to the HC. Different 2A peptides exhibited different cleavage efficiencies that correlated to the mAb expression level. The relative cleavage efficiency of each 2A peptide remains similar for expression of different IgG1 mAbs in different CHO cells. While complete cleavage was not observed for any of the 2A peptides, GSG linkers did enhance the cleavage efficiency and thus the mAb expression level. T2A with the GSG linker (GT2A) exhibited the highest cleavage efficiency and mAb expression level. Stably amplified CHO DG44 pools generated using GT2A had titers 357, 416 and 600 mg/L for the 3 mAbs in shake flask batch cultures. Incomplete cleavage likely resulted in incorrectly processed mAb species and aggregates, which were removed with a chromatin-directed clarification method and protein A purification. The vector and methods presented provide an easy process beneficial for both mAb development and manufacturing.     

Cleavage efficient 2A peptides for high level monoclonal antibody expression in CHO cells

Linking the heavy chain (HC) and light chain (LC) genes required for monoclonal antibodies (mAb) production on a single cassette using 2A peptides allows control of LC and HC ratio and reduces non-expressing cells. Four 2A peptides derived from the foot-and-mouth disease virus (F2A), equine rhinitis A virus (E2A), porcine teschovirus-1 (P2A) and Thosea asigna virus (T2A), respectively, were compared for expression of 3 biosimilar IgG1 mAbs in Chinese hamster ovary (CHO) cell lines. HC and LC were linked by different 2A peptides both in the absence and presence of GSG linkers. Insertion of a furin recognition site upstream of 2A allowed removal of 2A residues that would otherwise be attached to the HC. Different 2A peptides exhibited different cleavage efficiencies that correlated to the mAb expression level. The relative cleavage efficiency of each 2A peptide remains similar for expression of different IgG1 mAbs in different CHO cells. While complete cleavage was not observed for any of the 2A peptides, GSG linkers did enhance the cleavage efficiency and thus the mAb expression level. T2A with the GSG linker (GT2A) exhibited the highest cleavage efficiency and mAb expression level. Stably amplified CHO DG44 pools generated using GT2A had titers 357, 416 and 600 mg/L for the 3 mAbs in shake flask batch cultures. Incomplete cleavage likely resulted in incorrectly processed mAb species and aggregates, which were removed with a chromatin-directed clarification method and protein A purification. The vector and methods presented provide an easy process beneficial for both mAb development and manufacturing.     

The generation of stable,high MAb expressing CHO cell lines based on the artificial chromosome expression (ACE) technology

The manufacture of recombinant proteins at industrially relevant levels requires technologies that can engineer stable, high expressing cell lines rapidly, reproducibly and with relative ease. Commonly used methods incorporate transfection of mammalian cell lines with plasmid DNA containing the gene of interest. Identifying stable high expressing transfectants is normally laborious and time consuming. To improve this process, the ACE System has been developed based on pre‐engineered artificial chromosomes with multiple recombination acceptor sites. This system allows for the targeted transfection of single or multiple genes and eliminates the need for random integration into native host chromosomes. To illustrate the utility of the ACE System in generating stable, high expressing cell lines, CHO based candidate cell lines were generated to express a human monoclonal IgG1 antibody. Candidate cell lines were generated in under 6 months and expressed over 1 g/L and with specific productivities of up to 45 pg/cell/day under non‐fed, non‐optimized shake flask conditions. These candidate cell lines were shown to have stable expression of the monoclonal antibody for up to 70 days of continuous culture. The results of this study demonstrate that clonal, stable monoclonal antibody expressing CHO based cell lines can be generated by the ACE System rapidly and perform competitively with those cell lines generated by existing technologies. The ACE System, therefore, provides an attractive and practical alternative to conventional methods of cell line generation. Biotechnol. Bioeng. 2009; 104: 540–553 © 2009 Wiley Periodicals, Inc.     

Strategies for selecting recombinant CHO cell lines for cGMP manufacturing: Improving the efficiency of cell line generation

Transfectants with a wide range of cellular phenotypes are obtained during the process of cell line generation. For the successful manufacture of a therapeutic protein, a means is required to identify a cell line with desirable growth and productivity characteristics from this phenotypically wide‐ranging transfectant population. This identification process is on the critical path for first‐in‐human studies. We have stringently examined a typical selection strategy used to isolate cell lines suitable for cGMP manufacturing. One‐hundred and seventy‐five transfectants were evaluated as they progressed through the different assessment stages of the selection strategy. High producing cell lines, suitable for cGMP manufacturing, were identified. However, our analyses showed that the frequency of isolation of the highest producing cell lines was low and that ranking positions were not consistent between each assessment stage, suggesting that there is potential to improve upon the strategy. Attempts to increase the frequency of isolation of the 10 highest producing cell lines, by in silico analysis of alternative selection strategies, were unsuccessful. We identified alternative strategies with similar predictive capabilities to the typical selection strategy. One alternate strategy required fewer cell lines to be progressed at the assessment stages but the stochastic nature of the models means that cell line numbers are likely to change between programs. In summary, our studies illuminate the potential for improvement to this and future selection strategies, based around use of assessments that are more informative or that reduce variance, paving the way to improved efficiency of generation of manufacturing cell lines. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Immunodetection of partially glycosylated isoforms of alpha-dystroglycan by a new monoclonal antibody against its beta-dystroglycan-binding epitope

The alpha/beta dystroglycan (DG) complex links the extracellular matrix to the actin cytoskeleton. The extensive glycosylation of alpha-DG is believed to be crucial for the interaction with its extracellular matrix-binding partners. We characterized a monoclonal antibody, directed against the beta-DG-binding epitope ( approximately positions 550-565), which recognizes preferentially hypoglycosylated alpha-DG. In Western blot, the antibody was able to detect a number of partially glycosylated alpha-DG isoforms from rat brain and chicken skeletal muscle tissue samples. In addition, we demonstrated its inhibitory effect on the interaction between alpha- and beta-DG in vitro and preliminary immunostaining experiments suggest that such hypoglycosylated alpha-DG isoforms could play a role within cells.     

Eliminating tyrosine sequence variants in CHO cell lines producing recombinant monoclonal antibodies

Amino acid sequence variants are defined as unintended amino acid sequence changes that contribute to product variation with potential impact to product safety, immunogenicity, and efficacy. Therefore, it is important to understand the propensity for sequence variant (SV) formation during the production of recombinant proteins for therapeutic use. During the development of clinical therapeutic products, several monoclonal antibodies (mAbs) produced from Chinese Hamster Ovary (CHO) cells exhibited SVs at low levels (≤3%) in multiple locations throughout the mAbs. In these examples, the cell culture process depleted tyrosine, and the tyrosine residues in the recombinant mAbs were replaced with phenylalanine or histidine. In this work, it is demonstrated that tyrosine supplementation eliminated the tyrosine SVs, while early tyrosine starvation significantly increased the SV level in all mAbs tested. Additionally, it was determined that phenylalanine is the amino acid preferentially misincorporated in the absence of tyrosine over histidine, with no other amino acid misincorporated in the absence of tyrosine, phenylalanine, and histidine. The data support that the tyrosine SVs are due to mistranslation and not DNA mutation, most likely due to tRNA^Tyr mischarging due to the structural similarities between tyrosine and phenylalanine. Biotechnol. Bioeng. 2013; 110: 1087–1097. © 2012 Wiley Periodicals, Inc.     

Role of iron and sodium citrate in animal protein-free CHO cell culture medium on cell growth and monoclonal antibody production

Chemically defined iron compounds were investigated for the development of animal protein-free cell culture media to support growth of CHO cells and production of monoclonal antibodies (mAb). Using a multivessel approach of 96-well plates, shake flasks, and bioreactors, we identified iron and its chemical partner citrate as critical components for maintenance of continuous cell growth and mAb production. The optimized iron concentration range was determined to be 0.1-0.5 mM and that for citrate 0.125-1 mM. This complete formulation is able to maintain cell growth to similar levels as those supplemented with iron compounds alone; however, mAb productivity was enhanced by 30-40% when citrate was present. The addition of sodium citrate (SC) did not affect product quality as determined by size exclusion chromatography, ion exchange chromatography, reversed phase and normal phase-HPLC. No significant changes in glucose and lactate profiles, amino acid utilization, or mAb heavy and light chain expression ratios were observed. Cellular ATP level was ～30% higher when SC was included suggesting that SC may have a role in enhancing cellular energy content. When cell lysates were analyzed by LC-MS to assess the overall cellular protein profile, we identified that in the SC-containing sample, proteins involved in ribosome formation and protein folding were upregulated, and those functions in protein degradation were downregulated. Taken together, this data demonstrated that iron and citrate combination significantly enhanced mAb production without altering product quality and suggested these compounds had a role in upregulating the protein synthetic machinery to promote protein production.     

Quantitation of soluble aggregates in recombinant monoclonal antibody cell culture by pH-gradient protein A chromatography

Monoclonal antibodies (mAbs) produced from mammalian cell culture may contain significant amounts of dimers and higher order aggregates. Quantitation of soluble aggregates in the cell culture is time-consuming and labor-intensive, usually involving a purification step to remove the impurities that interfere with the subsequent size exclusion chromatography (SEC) analysis. We have developed a novel pH-gradient protein A chromatography for rapid, non-size based separation of the aggregates in mAb cell culture samples. Our results demonstrate that this method has excellent correlation with SEC and can be applied to both human immunoglobulin gamma 1 (IgG1) and IgG2 antibodies. This approach can be useful in the quantitation of soluble aggregates in crude cell culture samples.     

Model-based optimization of antibody galactosylation in CHO cell culture

Exerting control over the glycan moieties of antibody therapeutics is highly desirable from a product safety and batch-to-batch consistency perspective. Strategies to improve antibody productivity may compromise quality, while interventions for improving glycoform distribution can adversely affect cell growth and productivity. Process design therefore needs to consider the trade-off between preserving cellular health and productivity while enhancing antibody quality. In this work, we present a modeling platform that quantifies the impact of glycosylation precursor feeding – specifically that of galactose and uridine – on cellular growth, metabolism as well as antibody productivity and glycoform distribution. The platform has been parameterized using an initial training data set yielding an accuracy of ±5% with respect to glycoform distribution. It was then used to design an optimized feeding strategy that enhances the final concentration of galactosylated antibody in the supernatant by over 90% compared with the control without compromising the integral of viable cell density or final antibody titer. This work supports the implementation of Quality by Design towards higher-performing bioprocesses.     

Strategies for selecting Recombinant CHO cell lines for cGMP manufacturing: Realizing the potential in bioreactors

Manufacture of recombinant proteins from mammalian cell lines requires the use of bioreactor systems at scales of up to 20,000 L. The cost and complexity of such systems can prohibit their extensive use during the process to construct and select the manufacturing cell line. It is therefore common practice to develop a model of the production process in a small scale vessel, such as a shake‐flask, where lower costs, ease of handling, and higher throughput are possible. This model can then be used to select a small number of cell lines for further evaluation in bioreactor culture. Here, we extend our previous work investigating cell line construction strategies to assess how well the behavior of cell lines in such a shake‐flask assessment predicts behavior in the associated bioreactor production process. A panel of 29 GS‐CHO cell lines, all producing the same antibody, were selected to include a mixture of high and low producers from a pool of 175 transfectants. Assessment of this panel in 10 L bioreactor culture revealed wide variation in parameters including growth, productivity, and metabolite utilization. In general, those cell lines which were high producing in the bioreactor cultures had also been higher producing in an earlier shake‐flask assessment. However, some changes in rank position of the evaluated cell lines were seen between the two systems. A potential explanation of these observations is discussed and approaches to improve the predictability of assessments used for cell line selection are considered. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

CHO细胞表达抗血管内皮生长因子单克隆抗体工艺优化

抗血管内皮生长因子单克隆抗体(VEGF-MA)能够抑制肿瘤生长,具有良好的市场前景。本研究利用一株重组中国仓鼠卵巢细胞(Chinese hamster ovary cell,CHO)细胞株表达VEGF-MA。首先对培养基种类进行优化,筛选最优的基础培养基、补料培养基和外源添加物。研究结果表明:最有利于重组CHO细胞株表达VEGF-MA的基础培养基、补料培养基和外源添加物分别为ActiCHO P Powder CD、CD Efficient Feed C AG和Sheff-CHO Plus PF ACF。利用这一培养基配比在摇瓶和3 L发酵罐中培养重组CHO细胞,VEGF-MA产量均可达到3.20 g/L。在3 L发酵罐中进一步优化培养条件,结果表明:最优的接种密度、pH、溶解氧浓度、前期培养温度和后期培养温度分别为1.0×10^6个/mL、7.10、40%、36.5℃和34℃,此时的VEGF-MA产量能够达到4.10 g/L。VEGF-MA质量指标均处于标准范围内:电荷异质性、糖基化水平和蛋白纯度分别为26.1%、59.1%和95.1%。     

Evaluation of piggyBac‐mediated CHO pools to enable material generation to support GLP toxicology studies

Generating purified protein for GLP toxicology studies (GLP‐Tox) represents an important and often rate limiting step in the biopharmaceutical drug development process. Toxicity testing requires large amounts of therapeutic protein (>100 g), typically produced in a single 500–2,500 L bioreactor, using the final CHO clonally derived cell line (CDCL). One approach currently used to save time is to manufacture GLP‐Tox material using pools of high‐producing CHO CDCLs instead of waiting for the final CDCL. Recently, we reported CHO pools producing mAb titers >7 g/L using piggyBac‐mediated gene integration (PB CHO pools). In this study, we wanted to leverage high titer PB CHO pools to produce GLP‐Tox material. A detailed product quality attribute (PQA) assessment was conducted comparing PB CHO pools to pooled Top4 CDCLs. Four mAbs were evaluated. First, we found that PB CHO pools expressed all four mAbs at high titers (2.8–4.4 g/L in shake flasks). Second, all four PB CHO pools were aged to 55 generations (Gen). All four PB CHO Pools were found to be suitable over 55 Gen. Finally, we performed bioreactor scale‐up. PB CHO pool titers (3.7–4.8 g/L) were similar or higher than the pooled Top 4 CDCLs in 5 L bioreactors (2.4–4.1 g/L). The PQAs of protein derived from PB CHO pools were very similar to pooled Top 4 CHO CDCLs according to multiple orthogonal techniques including peptide mapping analysis. Taken together, these results demonstrate the technical feasibility of using PB CHO pools to manufacture protein for GLP‐Tox. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1436–1448, 2017     

Characterization of a monoclonal antibody reactive with a glycolipid antigen expressed by tumorigenic and certain immortalized,non-tumorigenic rat esophageal epithelial cell lines

A monoclonal antibody (mAb 5G) was produced against a tumorigenic rat esophageal epithelial cell line, designated B2T. Using an enzyme-linked immunosorbent assay, immunofluorescence assay (IFA), thin-layer chromatography (TLC) and immunoperoxidase staining, it was found that mAb 5G reacted specifically with a glycolipid antigen expressed by three tumorigenic rat esophageal epithelial cell lines, and two out of the three nontumorigenic, immortalized rat esophageal epithelial cell lines tested; but did not react with primary cultures of normal rat esophageal epithelial cells or fibroblasts. mAb 5G did not bind to rat respiratory tract carcinoma cell lines, to immortalized rat tracheal epithelial cell lines, or to primary cultures of normal rat tracheal epithelial cells. In addition, mAb 5G did not react with any of the human or mouse cell lines tested. In IFA experiments, mAb 5G stained imprints prepared from in vivo propagated B2T tumor tissues, but did not react with normal rat esophageal, tracheal, lung, liver, and kidney tissues. The antigen was identified by TLC as a neutral glycolipid, consisting of two bands, withR _F = 0.45 and 0.41, which migrated in proximity to the ceramide trihexoside standard on TLC plates. Densitometric scanning of the antigen bands indicated that the tumorigenic rat esophageal cell lines possessed 50%–90% more mAb-5G-reactive antigen than the nontumorigenic esophageal cell lines. The results show that mAb 5G reacts specifically with a glycolipid antigen expressed by tumorigenic and certain non-tumorigenic, immortalized rat esophageal epithelial cell lines that might be at the late stages of transformation and early malignancy.     

Anxa2- and Ctsd-knockout CHO cell lines to diminish the risk of contamination with host cell proteins

Chinese hamster ovary (CHO) cells have been used as host cells in the production of a range of recombinant therapeutic proteins, including monoclonal antibodies and Fc-fusion proteins. Host cell proteins (HCP) represent impurities that must be removed from therapeutic formulations because of their potential risks for immunogenicity. While the majority of HCP impurities are effectively removed in typical downstream purification processes, clearance of a small population of HCP remains challenging. In this study, we knocked out the Anxa2 and Ctsd genes to assess the feasibility of knockout approaches for diminishing the risk of contamination with HCP. Using the CRISPR/Cas9 system, Anxa2-, and Ctsd-knockout CHO cell lines were successfully established, and we confirmed the complete elimination of the corresponding HCP in cell lysates. Importantly, all knockout cell lines showed similar growth and viability to those of the wild-type control during 8 days of cultivation. Thus, knockout of unrequired genes can reduce contamination with HCP in the production of recombinant therapeutic proteins.     

Glycosylation profiling of a therapeutic recombinant monoclonal antibody with two N-linked glycosylation sites using liquid chromatography coupled to a hybrid quadrupole time-of-flight mass spectrometer

Monoclonal antibodies have been used increasingly as therapeutic agents to target various diseases. Although most monoclonal antibodies have only one N-linked glycosylation site in the Fc region, N-linked glycosylation sites in the Fab region have also been observed. Because glycosylation of a monoclonal antibody can have a significant impact on its effector function, efficacy, clearance, and immunogenicity, it is essential to assess the glycosylation profile during cell line and clone selection studies and to assess the impact of cell culture conditions on the glycoform distribution during process optimization studies to ensure that the antibody is being produced with appropriate and consistent glycosylation. This article describes a liquid chromatography-mass spectrometry-based approach, in combination with papain digestion and partial reduction, to obtain site-specific glycosylation profile information for a therapeutic monoclonal antibody with two N-linked glycosylation sites in the heavy chain.