Bradley R. Snedecor

Decreasing lactate level and increasing antibody production in Chinese Hamster Ovary cells (CHO) by reducing the expression of lactate dehydrogenase and pyruvate dehydrogenase kinases

Large-scale fed-batch cell culture processes of CHO cells are the standard platform for the clinical and commercial production of monoclonal antibodies. Lactate is one of the major by-products of CHO fed-batch culture. In pH-controlled bioreactors, accumulation of high levels of lactate is accompanied by high osmolality due to the addition of base to control pH of the cell culture medium, potentially leading to lower cell growth and lower therapeutic protein production during manufacturing. Lactate dehydrogenase (LDH) is an enzyme that catalyzes the conversion of the substrate, pyruvate, into lactate and many factors including pyruvate concentration modulate LDH activity. Alternately, pyruvate can be converted to acetyl-CoA by pyruvate dehydrogenases (PDHs), to be metabolized in the TCA cycle. PDH activity is inhibited when phosphorylated by pyruvate dehydrogenase kinases (PDHKs). In this study, we knocked down the gene expression of lactate dehydrogenase A (LDHa) and PDHKs to investigate the effect on lactate metabolism and protein production. We found that LDHa and PDHKs can be successfully downregulated simultaneously using a single targeting vector carrying small inhibitory RNAs (siRNA) for LDHa and PDHKs. Moreover, our fed-batch shake flask evaluation data using siRNA-mediated LDHa/PDHKs knockdown clones showed that downregulating LDHa and PDHKs in CHO cells expressing a therapeutic monoclonal antibody reduced lactate production, increased specific productivity and volumetric antibody production by approximately 90%, 75% and 68%, respectively, without appreciable impact on cell growth. Similar trends of lower lactate level and higher antibody productivity on average in siRNA clones were also observed from evaluations performed in bioreactors.

Controlling glycation of recombinant antibody in fed‐batch cell cultures

Protein glycation is a non‐enzymatic glycosylation that can occur to proteins in the human body, and it is implicated in the pathogenesis of multiple chronic diseases. Glycation can also occur to recombinant antibodies during cell culture, which generates structural heterogeneity in the product. In a previous study, we discovered unusually high levels of glycation (>50%) in a recombinant monoclonal antibody (rhuMAb) produced by CHO cells. Prior to that discovery, we had not encountered such high levels of glycation in other in‐house therapeutic antibodies. Our goal here is to develop cell culture strategies to decrease rhuMAb glycation in a reliable, reproducible, and scalable manner. Because glycation is a post‐translational chemical reaction between a reducing sugar and a protein amine group, we hypothesized that lowering the concentration of glucose—the only source of reducing sugar in our fed‐batch cultures—would lower the extent of rhuMAb glycation. When we decreased the supply of glucose to bioreactors from bolus nutrient and glucose feeds, rhuMAb glycation decreased to below 20% at both 2‐L and 400‐L scales. When we maintained glucose concentrations at lower levels in bioreactors with continuous feeds, we could further decrease rhuMAb glycation levels to below 10%. These results show that we can control glycation of secreted proteins by controlling the glucose concentration in the cell culture. In addition, our data suggest that rhuMAb glycation occurring during the cell culture process may be approximated as a second‐order chemical reaction that is first order with respect to both glucose and non‐glycated rhuMAb. The basic principles of this glycation model should apply to other recombinant proteins secreted during cell culture. Biotechnol. Bioeng. 2011;108: 2600–2610.

Chinese hamster ovary K1 host cell enables stable cell line development for antibody molecules which are difficult to express in DUXB11‐derived dihydrofolate reductase deficient host cell

Therapeutic monoclonal antibodies (mAb) are often produced in Chinese hamster ovary (CHO) cells. Three commonly used CHO host cells for generating stable cell lines to produce therapeutic proteins are dihydrofolate reductase (DHFR) positive CHOK1, DHFR‐deficient DG44, and DUXB11‐based DHFR deficient CHO. Current Genentech commercial full‐length antibody products have all been produced in the DUXB11‐derived DHFR‐deficient CHO host. However, it has been challenging to develop stable cell lines producing an appreciable amount of antibody proteins in the DUXB11‐derived DHFR‐deficient CHO host for some antibody molecules and the CHOK1 host has been explored as an alternative approach. In this work, stable cell lines were developed for three antibody molecules in both DUXB11‐based and CHOK1 hosts. Results have shown that the best CHOK1 clones produce about 1 g/l for an antibody mAb1 and about 4 g/l for an antibody mAb2 in 14‐day fed batch cultures in shake flasks. In contrast, the DUXB11‐based host produced ∼0.1 g/l for both antibodies in the same 14‐day fed batch shake flask production experiments. For an antibody mAb3, both CHOK1 and DUXB11 host cells can generate stable cell lines with the best clone in each host producing ∼2.5 g/l. Additionally, studies have shown that the CHOK1 host cell has a larger endoplasmic reticulum and higher mitochondrial mass.

Carboxypeptidase D is the only enzyme responsible for antibody C-terminal lysine cleavage in Chinese hamster ovary (CHO) cells

Heterogeneity of C‐terminal lysine levels often observed in therapeutic monoclonal antibodies is believed to result from the proteolysis by endogenous carboxypeptidase(s) during cell culture production. Identifying the responsible carboxypeptidase(s) for C‐terminal lysine cleavage in CHO cells would provide valuable insights for antibody production cell culture processes development and optimization. In this study, five carboxypeptidases, CpD, CpM, CpN, CpB, and CpE, were studied for message RNA (mRNA) expression by qRT‐PCR analysis in two most commonly used blank hosts (DUXB‐11 derived DHFR‐deficient DP12 host and DHFR‐positive CHOK1 host), used for therapeutic antibody production, as well an antibody‐expressing cell line derived from each host. Our results showed that CpD had the highest mRNA expression. When CpD mRNA levels were reduced by RNAi (RNA interference) technology, C‐terminal lysine levels increased, whereas there was no obvious change in C‐terminal lysine levels when a different carboxypeptidase mRNA level was knocked down suggesting that carboxypeptidase D is the main contributor for C‐terminal lysine processing. Most importantly, when CpD expression was knocked out by CRISPR (Clustered Regularly Interspaced Short Palindromic Repeats) technology, C‐terminal lysine cleavage was completely abolished in CpD knockout cells based on mass spectrometry analysis, demonstrating that CpD is the only endogenous carboxypeptidase that cleaves antibody heavy chain C‐terminal lysine in CHO cells. Hence, our work showed for the first time that the cleavage of antibody heavy chain C‐terminal lysine is solely mediated by the carboxypeptidase D in CHO cells and our finding provides one solution to eliminating C‐terminal lysine heterogeneity for therapeutic antibody production by knocking out CpD gene expression. Biotechnol. Bioeng. 2016;113: 2100–2106.

A strategy to accelerate protein production from a pool of clones in Chinese hamster ovary cells for toxicology studies

In the biopharmaceutical industry, a clonally derived cell line is typically used to generate material for investigational new drug (IND)‐enabling toxicology studies. The same cell line is then used to generate material for clinical studies. If a pool of clones can be used to produce material for IND‐enabling toxicology studies (Pool for Tox (PFT) strategy) during the time a lead clone is being selected for clinical material production, the toxicology studies can be accelerated significantly (approximately 4 months at Genentech), leading to a potential acceleration of 4 months for the IND submission. We explored the feasibility of the PFT strategy with three antibodies—mAb1, mAb2, and mAb3—at the 2 L scale. For each antibody, two lead cell lines were identified that generated material with similar product quality to the material generated from the associated pool. For two antibody molecules, mAb1 and mAb2, the material generated by the lead cell lines from 2 L bioreactors was tested in an accelerated stability study and was shown to have stability comparable to the material generated by the associated pool. Additionally, we used this approach for two antibody molecules, mAb4 and mAb5, at Tox and GMP production. The materials from the Tox batch at 400 L scale and three GMP batches at 2000 L scale have comparable product quality attributes for both molecules. Our results demonstrate the feasibility of using a pool of clonally derived cell lines to generate material of similar product quality and stability for use in IND‐enabling toxicology studies as was derived from the final production clone, which enabled significant acceleration of timelines into clinical development.