Red colored IgG4 caused by vitamin B12 from cell culture media combined with disulfide reduction at harvest

While many antibody therapeutics are formulated at low concentration (~10–20 mg/mL) for intravenous administration, high concentration (> 100 mg/mL) formulations may be required for subcutaneous delivery in certain clinical indications. For such high concentration formulations, product color is more apparent due to the higher molecular density across a given path-length. Color is therefore a product quality attribute that must be well-understood and controlled, to demonstrate process consistency and enable clinical trial blinding. Upon concentration of an IgG4 product at the 2000 L manufacturing scale, variability in product color, ranging from yellow to red, was observed. A small-scale experimental model was developed to assess the effect of processing conditions (medium composition and harvest conditions) on final bulk drug substance (BDS) color. The model was used to demonstrate that, for two distinct IgG4 products, red coloration occurred only in the presence of disulfide reduction-mediated antibody dissociation. The red color-causing component was identified as vitamin B₁₂, in the hydroxocobalamin form, and the extent of red color was correlated with the cobalt (vitamin B₁₂) concentration in the final pools. The intensity of redness in the final BDS was modulated by changing the concentration of vitamin B₁₂ in the cell culture media.     

Population-based modeling of the progression of apoptosis in mammalian cell culture

The production of biopharmaceuticals from mammalian cell culture is hindered by apoptosis, which is the primary cause of cell death in these cultures. As a tool for optimization of culture yield, this study presents a population-based model describing the progression of apoptosis in a monoclonal antibody (mAb)-producing Chinese hamster ovary (CHO) cell culture. Because mAb production does not cease when apoptosis begins, the model was designed to incorporate subpopulations at various stages in the progression of apoptosis. The model was validated against intracellular measurements of caspase activity as well as cell density, nutrient levels, and toxic metabolites. Since the specific details of apoptotic mechanisms have not been elucidated in this cell line, we employed a model comparison analysis that suggests the most plausible pathways of activation.     

Improving culture performance and antibody production in CHO cell culture processes by reducing the Warburg effect

Lactate is one of the key waste metabolites of mammalian cell culture. High lactate levels are caused by high aerobic glycolysis, also known as the Warburg effect, and are usually associated with adverse culture performance. Therefore, reducing lactate accumulation has been an ongoing challenge in the cell culture development to improve growth, productivity, and process robustness. The pyruvate dehydrogenase complex (PDC) plays a crucial role for the fate of pyruvate, as it converts pyruvate to acetyl coenzyme A (acetyl‐CoA). The PDC activity can be indirectly increased by inhibiting the PDC inhibitor, pyruvate dehydrogenase kinase, using dichloroacetate (DCA), resulting in less pyruvate being available for lactate formation. Here, Chinese hamster ovary cells were cultivated either with 5 mM DCA or without DCA in various batch and fed‐batch bioreactor processes. In all cultures, DCA increased peak viable cell density (VCD), culture length and final antibody titer. The strongest effect was observed in a fed batch with media and glucose feeding in which peak VCD was increased by more than 50%, culture length was extended by more than 3 days, and the final antibody titer increased by more than twofold. In cultures with DCA, lactate production and glucose consumption during exponential growth were on average reduced by approximately 40% and 35%, respectively. Metabolic flux analysis showed reduced glycolytic fluxes, whereas fluxes in the tricarboxylic acid (TCA) cycle were not affected, suggesting that cultures with DCA use glucose more efficiently. In a proteomics analysis, only few proteins were identified as being differentially expressed, indicating that DCA acts on a posttranslational level. Antibody quality in terms of aggregation, charge variant, and glycosylation pattern was unaffected. Subsequent bioreactor experiments with sodium lactate and sodium chloride feeding indicated that lower osmolality, rather than lower lactate concentration itself, improved culture performance in DCA cultures. In conclusion, the addition of DCA to the cell culture improved culture performance and increased antibody titers without any disadvantages for cell‐specific productivity or antibody quality.     

Thioredoxin 1 is responsible for antibody disulfide reduction in CHO cell culture

During large-scale manufacturing of an IgG1 monoclonal antibody in Chinese hamster ovary (CHO) cells, reduction of the antibody's disulfide bonds was observed. We present evidence that mammalian thioredoxin 1 (TXN1) is the terminal enzyme responsible for this reduction event. We demonstrate a marked prevention of IgG1 disulfide bond reduction in a cell-density dependent manner by knocking down expression of TXN1 via lentivirus transduction of short hairpin RNA.     

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%。     

Impact of micro and macroporous TFF membranes on product sieving and chromatography loading for perfusion cell culture

Bioprocess intensification can be achieved through high cell density perfusion cell culture with continuous protein capture integration. Protein passage and cell retention are commonly accomplished using tangential flow filtration systems consisting of microporous membranes. Significant challenges, including low efficiency and decaying product sieving over time, are commonly observed in these cell retention devices. Here, we demonstrate that a macroporous membrane overcomes the product sieving challenges when comparing to several other membrane chemistries and pore sizes within the microporous range. This way, variable chromatography column loading is avoided. The macroporous membrane yielded a 13,000 L/m² volumetric throughput. The membrane's cut-off size results in an increased permeate turbidity due to particles passage, such as cell debris, through pores ranging from 1 to 4 µm. In addition, successful chromatography column plugging mitigation was achieved by employing depth filtration before the chromatographic step. Depth filtration volumetric throughputs were between 600 and 1,000 L/m². Combing a macroporous cell retention device with a depth filter not only provided an alternative to address the challenge of undesired long protein residence times in the bioreactor due to product sieving decay, but also exhibited a throughput increase, making the integration of multicolumn capture chromatography with a perfusion cell culture a more robust process.     

Screening for improved cell performance: selection of subclones with altered production kinetics or improved stability by cell sorting

One of the major problems in the biotechnology industry is the selection of cell lines well suited for production of biopharmaceutical proteins. Usually, the most important selection criterion is the cell specific production rate. Nevertheless, a good producer cell line should have a number of additional advantageous properties, which allow the cell line to perform well in the type of bioreactor chosen for the process. However, the time and work required to select for high production rates as well as the lack of methods to specifically select for other cellular properties, usually prevents researchers from including such criteria into their screening program.With the Single Cell Secretion Assay it is possible to measure the specific production rates of individual cells by catching secreted product in an artificial matrix applied to the cell surface. Flow cytometric cell sorting then allows selection of rare cells with high production rates, which occur at frequencies as low as 10(-6). By combining this method with culture conditions that bring out a desired cellular property, we were able to isolate subclones with similar production rates, but improved performance from a recombinant Chinese hamster ovary cell line producing a human monoclonal antibody. The two desired cellular properties screened for were a non-growth associated production kinetic and improved stability in the absence of selective pressure.     

Fed-batch bioreactor performance and cell line stability evaluation of the artificial chromosome expression technology expressing an IgG1 in Chinese hamster ovary cells

The artificial chromosome expression (ACE) technology system uses an engineered artificial chromosome containing multiple site-specific recombination acceptor sites for the rapid and efficient construction of stable cell lines. The construction of Chinese hamster ovary(CHO) cell lines expressing an IgG1 monoclonal antibody (MAb) using the ACE system has been previously described (Kennard et al., Biotechnol Bioeng. 2009;104:540-553). To further demonstrate the manufacturing feasibility of the ACE system, four CHO cell lines expressing the human IgG1 MAb 4A1 were evaluated in batch and fed-batch shake flasks and in a 2-L fed-batch bioreactor. The batch shake flasks achieved titers between 0.7 and 1.1 g/L, whereas the fed-batch shake flask process improved titers to 2.5–3.0 g/L. The lead 4A1 ACE cell line achieved titers of 4.0 g/L with an average specific productivity of 40 pg/(cell day) when cultured in a non optimized 2-L fed-batch bioreactor using a completely chemically defined process. Generational stability characterization of the lead 4A1-expressing cell line demonstrated that the cell line was stable for up to 75 days in culture. Product quality attributes of the 4A1 MAb produced by the ACE system during the stability evaluation period were unchanged and also comparable to existing expression technologies such as the CHO-dhfr system. The results of this evaluation demonstrate that a clonal, stable MAb-expressing CHO cell line can be produced using ACE technology that performs competitively using a chemically defined fed-batch bioreactor process with comparable product quality attributes to cell lines generated by existing technologies.     

Peak antibody production is associated with increased oxidative metabolism in an industrially relevant fed‐batch CHO cell culture

Cell metabolism can vary considerably over the course of a typical fed‐batch antibody production process. However, the intracellular pathway alterations associated with various phases of growth and antibody production have yet to be fully elucidated using industrially relevant production hosts. Therefore, we performed ¹³C labeling experiments and metabolic flux analysis (MFA) to characterize CHO cell metabolism during four separate phases of a fed‐batch culture designed to closely represent industrial process conditions. First, we found that peak specific growth rate was associated with high lactate production and minimal TCA cycling. Conversely, we found that lactate metabolism switched from net production to net consumption as the culture transitioned from peak growth to peak antibody production. During the peak antibody production phase, energy was primarily generated through oxidative phosphorylation, which was also associated with elevated oxidative pentose phosphate pathway (oxPPP) activity. Interestingly, as TCA cycling and antibody production reached their peaks, specific growth rate continued to diminish as the culture entered stationary phase. However, TCA cycling and oxPPP activity remained high even as viable cell density began to decline. Overall, we found that a highly oxidative state of metabolism corresponded with peak antibody production, whereas peak cell growth was characterized by a highly glycolytic metabolic state. Biotechnol. Bioeng. 2013; 110: 2013–2024. © 2013 Wiley Periodicals, Inc.     

In vitro immunization of human peripheral blood lymphocytes: establishment of B cell lines secreting IgM specific for cholera toxin B subunit from lymphocytes stimulated with IL-2 and IL-4

In vitro immunization (IVI) techniques have a great potential in the production of human monoclonal antibodies (MAbs) against various antigens. An IVI method of human peripheral blood lymphocytes (PBL) has been developed with a human lung adenocarcinoma cell line in our laboratory. Although several cancer specific human MAbs were successfully generated by using this IVI method, it was not available for soluble antigens, which prompted us to improve the method for generation of human MAbs against soluble antigens. IVI with soluble antigens was effectively caused by the addition of muramyl dipeptides, interleukin-2 and interleukin-4. It was found that the difference of sensitivity of lymphocytes depending upon donors could be overcome by finding the optimal concentrations of IL-2 and IL-4. IVI of human PBL was performed with cholera toxin B subunit (CTB) and the immunized B cells were transformed by Epstein-Barr virus. Anti-CTB antibody was detected using an indirect ELISA. B cells producing anti-CTB antibodies were directly cloned by a soft agar cloning method. This revised version was published online in August 2006 with corrections to the Cover Date.     

Combining high-throughput screening of caspase activity with anti-apoptosis genes for development of robust CHO production cell lines

A set of anti-apoptotic genes were over-expressed, either singly or in combination, in an effort to develop robust Chinese Hamster Ovary host cell lines suitable for manufacturing biotherapeutics. High-throughput screening of caspase 3/7 activity enabled a rapid selection of transfectants with reduced caspase activity relative to the host cell line. Transfectants with reduced caspase 3/7 activity were then tested for improved integrated viable cell count (IVCC), a function of peak viable cell density and longevity. The maximal level of improvement in IVCC could be achieved by over-expression of either single anti-apoptotic genes, e.g., Bcl-2Δ (a mutated variant of Bcl-2) or Bcl-XL, or a combination of two or three anti-apoptotic genes, e.g., E1B-19K, Aven, and XIAPΔ. These cell lines yielded higher transient antibody production and a greater number of stable clones with high antibody yields. In a 5 L fed-batch bioreactor system, BΔ31-1, a stable clone expressing Bcl-2Δ, had a product titer that was 180% as compared to an optimal clone (Con-1) from the control cell line. Although lactate accumulated to more than 5 g/L in the control culture, its concentration was reduced in the anti-apoptotic BΔ31-1 cultures to below 1 g/L, confirming our earlier findings that cells over-expressing anti-apoptotic genes consume the lactate that would otherwise accumulate as a by-product in the culture medium. To the best of our knowledge, this is the first study to use the high throughput caspase screening method to identify CHO host cell lines with superior anti-apoptotic characteristics.     

Neutralization of leukotriene C4 and D4 activity by monoclonal and single-chain antibodies

Background

Cysteinyl leukotrienes (LTs) are key mediators in inflammation. To explore the structure of the antigen-recognition site of a monoclonal antibody against LTC₄ (mAbLTC), we previously isolated full-length cDNAs for heavy and light chains of the antibody and prepared a single-chain antibody comprising variable regions of these two chains (scFvLTC).

Methods

We examined whether mAbLTC and scFvLTC neutralized the biological activities of LTC₄ and LTD₄ by competing their binding to their receptors.

Results

mAbLTC and scFvLTC inhibited their binding of LTC₄ or LTD₄ to CysLT₁ receptor (CysLT₁R) and CysLT₂ receptor (CysLT₂R) overexpressed in Chinese hamster ovary cells. The induction by LTD₄ of monocyte chemoattractant protein-1 and interleukin-8 mRNAs in human monocytic leukemia THP-1 cells expressing CysLT₁R was dose-dependently suppressed not only by mAbLTC but also by scFvLTC. LTC₄- and LTD₄-induced aggregation of mouse platelets expressing CysLT₂R was dose-dependently suppressed by either mAbLTC or scFvLTC. Administration of mAbLTC reduced pulmonary eosinophil infiltration and goblet cell hyperplasia observed in a murine model of asthma. Furthermore, mAbLTC bound to CysLT₂R antagonists but not to CysLT₁R antagonists.

Conclusions

These results indicate that mAbLTC and scFvLTC neutralize the biological activities of LTs by competing their binding to CysLT₁R and CysLT₂R. Furthermore, the binding of cysteinyl LT receptor antagonists to mAbLTC suggests the structural resemblance of the LT-recognition site of the antibody to that of these receptors.

General significance

mAbLTC can be used in the treatment of inflammatory diseases such as asthma.