Modeling kinetics of a large‐scale fed‐batch CHO cell culture by Markov chain Monte Carlo method

Markov chain Monte Carlo (MCMC) method was applied to model kinetics of a fed‐batch Chinese hamster ovary cell culture process in 5,000‐L bioreactors. The kinetic model consists of six differential equations, which describe dynamics of viable cell density and concentrations of glucose, glutamine, ammonia, lactate, and the antibody fusion protein B1 (B1). The kinetic model has 18 parameters, six of which were calculated from the cell culture data, whereas the other 12 were estimated from a training data set that comprised of seven cell culture runs using a MCMC method. The model was confirmed in two validation data sets that represented a perturbation of the cell culture condition. The agreement between the predicted and measured values of both validation data sets may indicate high reliability of the model estimates. The kinetic model uniquely incorporated the ammonia removal and the exponential function of B1 protein concentration. The model indicated that ammonia and lactate play critical roles in cell growth and that low concentrations of glucose (0.17 mM) and glutamine (0.09 mM) in the cell culture medium may help reduce ammonia and lactate production. The model demonstrated that 83% of the glucose consumed was used for cell maintenance during the late phase of the cell cultures, whereas the maintenance coefficient for glutamine was negligible. Finally, the kinetic model suggests that it is critical for B1 production to sustain a high number of viable cells. The MCMC methodology may be a useful tool for modeling kinetics of a fed‐batch mammalian cell culture process. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

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.     

Metabolic analysis of antibody producing CHO cells in fed‐batch production

Chinese hamster ovary (CHO) cells are commonly used for industrial production of recombinant proteins in fed batch or alternative production systems. Cells progress through multiple metabolic stages during fed‐batch antibody (mAb) production, including an exponential growth phase accompanied by lactate production, a low growth, or stationary phase when specific mAb production increases, and a decline when cell viability declines. Although media composition and cell lineage have been shown to impact growth and productivity, little is known about the metabolic changes at a molecular level. Better understanding of cellular metabolism will aid in identifying targets for genetic and metabolic engineering to optimize bioprocess and cell engineering. We studied a high expressing recombinant CHO cell line, designated high performer (HP), in fed‐batch productions using stable isotope tracers and biochemical methods to determine changes in central metabolism that accompany growth and mAb production. We also compared and contrasted results from HP to a high lactate producing cell line that exhibits poor growth and productivity, designated low performer (LP), to determine intrinsic metabolic profiles linked to their respective phenotypes. Our results reveal alternative metabolic and regulatory pathways for lactate and TCA metabolite production to those reported in the literature. The distribution of key media components into glycolysis, TCA cycle, lactate production, and biosynthetic pathways was shown to shift dramatically between exponential growth and stationary (production) phases. We determined that glutamine is both utilized more efficiently than glucose for anaplerotic replenishment and contributes more significantly to lactate production during the exponential phase. Cells shifted to glucose utilization in the TCA cycle as growth rate decreased. The magnitude of this metabolic switch is important for attaining high viable cell mass and antibody titers. We also found that phosphoenolpyruvate carboxykinase (PEPCK1) and pyruvate kinase (PK) are subject to differential regulation during exponential and stationary phases. The concomitant shifts in enzyme expression and metabolite utilization profiles shed light on the regulatory links between cell metabolism, media metabolites, and cell growth. Biotechnol. Bioeng. 2013; 110: 1735–1747. © 2013 Wiley Periodicals, Inc.     

Robust parameter estimation during logistic modeling of batch and fed‐batch culture kinetics

Methods for robust logistic modeling of batch and fed‐batch mammalian cell cultures are presented in this study. Linearized forms of the logistic growth, logistic decline, and generalized logistic equation were derived to obtain initial estimates of the parameters by linear least squares. These initial estimates facilitated subsequent determination of refined values by nonlinear optimization using three different algorithms. Data from BHK, CHO, and hybridoma cells in batch or fed‐batch cultures at volumes ranging from 100 mL–300 L were tested with the above approach and solution convergence was obtained for all three nonlinear optimization approaches for all data sets. This result, despite the sensitivity of logistic equations to parameter variation because of their exponential nature, demonstrated that robust estimation of logistic parameters was possible by this combination of linearization followed by nonlinear optimization. The approach is relatively simple and can be implemented in a spreadsheet to robustly model mammalian cell culture batch or fed‐batch data. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

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.     

Host cell protein dynamics in the supernatant of a mAb producing CHO cell line

The characterization of host cell protein (HCP) content during the production of therapeutic recombinant proteins is an important aspect in the drug development process. Despite this, key components of the HCP profile and how this changes with processing has not been fully investigated. Here we have investigated the supernatant HCP profile at different times throughout culture of a null and model GS-CHO monoclonal antibody producing mammalian cell line grown in fed-batch mode. Using 2D-PAGE and LC-MS/MS we identify a number of intracellular proteins (e.g., protein disulfide isomerise; elongation factor 2; calreticulin) that show a significant change in abundance relative to the general increase in HCP concentration observed with progression of culture. Those HCPs that showed a significant change in abundance across the culture above the general increase were dependent on the cell line examined. Further, our data suggests that the majority of HCPs in the supernatant of the cell lines investigated here arise through lysis or breakage of cells, associated with loss in viability, and are not present due to the secretion of protein material from within the cell. SELDI-TOF and principal components analysis were also investigated to enable rapid monitoring of changes in the HCP profile. SELDI-TOF analysis showed the same trends in the HCP profile as observed by 2D-PAGE analysis and highlighted biomarkers that could be used for process monitoring. These data further our understanding of the relationship between the HCP profile and cell viability and may ultimately enable a more directed development of purification strategies and the development of cell lines based upon their HCP profile.     

Principles and approach to developing mammalian cell culture media for high cell density perfusion process leveraging established fed‐batch media

Perfusion medium was successfully developed based on our fed‐batch platform basal and feed media. A systematic development approach was undertaken by first optimizing the ratios of fed‐batch basal and feed media followed by targeted removal of unnecessary and redundant components. With this reduction in components, the medium could then be further concentrated by 2× to increase medium depth. The medium osmolality was also optimized where we found ～360 mOsm/kg was desirable resulting in a residual culture osmolality of ～300 mOsm/kg for our cell lines. Further building on this, the amino acids Q, E, N, and D were rebalanced to reduce lactate and ammonium levels, and increase the cell‐specific productivity without compromising on cell viability while leaving viable cell density largely unaffected. Further modifications were also made by increasing certain important vitamin and lipid concentrations, while eliminating other unnecessary vitamins. Overall, an effective perfusion medium was developed with all components remaining in the formulation understood to be important and their concentrations increased to improve medium depth. The critical cell‐specific perfusion rate using this medium was then established for a cell line of interest to be 0.075 nL/cell‐day yielding 1.2 g/L‐day at steady state. This perfusion process was then successfully scaled up to a 100 L single‐use bioreactor with an ATF6 demonstrating similar performance as a 2 L bioreactor with an ATF2. Large volume handling challenges in our fed‐batch facility were overcome by developing a liquid medium version of the powder medium product contained in custom totes for plug‐and‐play use with the bioreactor. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:891–901, 2017     

Evaluation of different vector design strategies for the expression of recombinant monoclonal antibody in CHO cells

Monoclonal antibodies (mAbs) have emerged as the most promising category of recombinant proteins due to their high efficiency for the treatment of a wide range of human diseases. The complex nature of mAbs creates a great deal of challenges in both upstream and downstream manufacturing processes. Proportional expression and correct folding and assembly of the light chain and heavy chain are required for efficient production of the mAbs. In this regard, expression vector design has proven to have profound effects on the antibody expression level as well as its stability and quality. Here, we have explored the efficiency of different vector design strategies for the expression of a recombinant IgG1 antibody in Chinese hamster ovary (CHO) cells. The antibody expression level was analyzed in transient expression and stable cell pools followed by expression analysis on single-cell clones. While detectable amounts of antibody were observed in all three systems, dual-promoter single-vector system showed the highest expression level in transient and stable expression as well as the highest productivity among clonal cells. Our results here show the importance of vector design for successful production of whole mAbs in CHO cells.     

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.     

Scale-up and optimization of an acoustic filter for 200 L/day perfusion of a CHO cell culture

Acoustic cell retention devices have provided a practical alternative for up to 50 L/day perfusion cultures but further scale-up has been limited. A novel temperature-controlled and larger-scale acoustic separator was evaluated at up to 400 L/day for a 10(7) CHO cell/mL perfusion culture using a 100-L bioreactor that produced up to 34 g/day recombinant protein. The increased active volume of this scaled-up separator was divided into four parallel compartments for improved fluid dynamics. Operational settings of the acoustic separator were optimized and the limits of robust operations explored. The performance was not influenced over wide ranges of duty cycle stop and run times. The maximum performance of 96% separation efficiency at 200 L/day was obtained by setting the separator temperature to 35.1 degrees C, the recirculation rate to three times the harvest rate, and the power to 90 W. While there was no detectable effect on culture viability, viable cells were selectively retained, especially at 50 L/day, where there was a 5-fold higher nonviable washout efficiency. Overall, the new temperature-controlled and scaled-up separator design performed reliably in a way similar to smaller-scale acoustic separators. These results provide strong support for the feasibility of much greater scale-up of acoustic separations.     

Improving the efficiency of CHO cell line generation using glutamine synthetase gene knockout cells

Although Chinese hamster ovary (CHO) cells, with their unique characteristics, have become a major workhorse for the manufacture of therapeutic recombinant proteins, one of the major challenges in CHO cell line generation (CLG) is how to efficiently identify those rare, high‐producing clones among a large population of low‐ and non‐productive clones. It is not unusual that several hundred individual clones need to be screened for the identification of a commercial clonal cell line with acceptable productivity and growth profile making the cell line appropriate for commercial application. This inefficiency makes the process of CLG both time consuming and laborious. Currently, there are two main CHO expression systems, dihydrofolate reductase (DHFR)‐based methotrexate (MTX) selection and glutamine synthetase (GS)‐based methionine sulfoximine (MSX) selection, that have been in wide industrial use. Since selection of recombinant cell lines in the GS‐CHO system is based on the balance between the expression of the GS gene introduced by the expression plasmid and the addition of the GS inhibitor, L‐MSX, the expression of GS from the endogenous GS gene in parental CHOK1SV cells will likely interfere with the selection process. To study endogenous GS expression's potential impact on selection efficiency, GS‐knockout CHOK1SV cell lines were generated using the zinc finger nuclease (ZFN) technology designed to specifically target the endogenous CHO GS gene. The high efficiency (～2%) of bi‐allelic modification on the CHO GS gene supports the unique advantages of the ZFN technology, especially in CHO cells. GS enzyme function disruption was confirmed by the observation of glutamine‐dependent growth of all GS‐knockout cell lines. Full evaluation of the GS‐knockout cell lines in a standard industrial cell culture process was performed. Bulk culture productivity improved two‐ to three‐fold through the use of GS‐knockout cells as parent cells. The selection stringency was significantly increased, as indicated by the large reduction of non‐producing and low‐producing cells after 25 µM L‐MSX selection, and resulted in a six‐fold efficiency improvement in identifying similar numbers of high‐productive cell lines for a given recombinant monoclonal antibody. The potential impact of GS‐knockout cells on recombinant protein quality is also discussed. Biotechnol. Bioeng. 2012; 109:1007–1015. © 2011 Wiley Periodicals, Inc.     

Profiling of N‐glycosylation gene expression in CHO cell fed‐batch cultures

One of the goals of recombinant glycoprotein production is to achieve consistent glycosylation. Although many studies have examined the changes in the glycosylation quality of recombinant protein with culture, very little has been done to examine the underlying changes in glycosylation gene expression as a culture progresses. In this study, the expression of 24 genes involved in N‐glycosylation were examined using quantitative RT PCR to gain a better understanding of recombinant glycoprotein glycosylation during production processes. Profiling of the N‐glycosylation genes as well as concurrent analysis of glycoprotein quality was performed across the exponential, stationary and death phases of a fed‐batch culture of a CHO cell line producing recombinant human interferon‐γ (IFN‐γ). Of the 24 N‐glycosylation genes examined, 21 showed significant up‐ or down‐regulation of gene expression as the fed‐batch culture progressed from exponential, stationary and death phase. As the fed‐batch culture progressed, there was also an increase in less sialylated IFN‐γ glycoforms, leading to a 30% decrease in the molar ratio of sialic acid to recombinant IFN‐γ. This correlated with decreased expression of genes involved with CMP sialic acid synthesis coupled with increased expression of sialidases. Compared to batch culture, a low glutamine fed‐batch strategy appears to need a 0.5 mM glutamine threshold to maintain similar N‐glycosylation genes expression levels and to achieve comparable glycoprotein quality. This study demonstrates the use of quantitative real time PCR method to identify possible “bottlenecks” or “compromised” pathways in N‐glycosylation and subsequently allow for the development of strategies to improve glycosylation quality. Biotechnol. Bioeng. 2010;107: 516–528. © 2010 Wiley Periodicals, Inc.