Kinetic modeling as a tool to understand the influence of cell culture process parameters on the glycation of monoclonal antibody biotherapeutics

Glycation, the nonenzymatic reaction between the reducing sugar glucose and the primary amine residues on amino acid side chains, commonly occurs in the cell culture supernatant during production of therapeutic monoclonal antibodies (mAbs). While glycation has the potential to impact efficacy and pharmacokinetic properties for mAbs, the most common undesirable impact of glycation is on the distribution of charged species, often a release specification for commercial processes. Existing empirical approaches are usually insufficient to rationalize the effects of cell line and process changes on glycation. To address this gap, we developed a kinetic model for estimating mAb glycation levels during the cell culture process. The rate constant for glycation, including temperature and pH dependence, was estimated by fitting the kinetic model to time-course glycation data from bioreactors operated at different process settings that yielded a wide range of glycation values. The parameter values were further validated by independently estimating glycation rate constants using cell-free incubation studies at various temperatures. The model was applied to another mAb, by re-estimating the activation energy to account for effect of a glycation “hotspot”. The model was further utilized to study the role of temperature shift as an approach to reduce glycation levels in the manufacturing process for mAb2. While a downshift in temperature resulted in lowering of glycation levels for mAb2, the model helped elucidate that this effect was caused due to contribution from changes in glucose consumption, mAb secretion and temperature, instead of a direct impact of temperature alone on the kinetic rate of glycation.     

A study in glycation of a therapeutic recombinant humanized monoclonal antibody: where it is, how it got there, and how it affects charge-based behavior

The glycated form of a basic recombinant humanized monoclonal antibody (rhuMAb) was separated and quantitated by boronate affinity chromatography using optimized shielding reagents. Characterization on the isolated glycated material by peptide mapping analysis, using liquid chromatography-mass spectrometry (LC-MS) and tandem mass spectrometry (MS/MS) sequencing techniques, identified eight reactive lysine primary amine sites. The glycation reaction extent was similar among the various reactive sites, ranging from approximately 1 to 12%, and a single histidine residue separated the most and least reactive sites. Boronate chromatography run in a linear gradient mode separated monoglycated rhuMAb from higher order glycated species and indicated that the majority ( approximately 90%) of glycated rhuMAb is monoglycated. Low-level glycation on a heavy chain lysine located within a complementarity-determining region (CDR) did not significantly affect binding activity in potency measurements. The glycated forms also behaved as slightly more acidic than the nonglycated antibody in charge-based separation techniques, observable by capillary isoelectric focusing (cIEF) and ion exchange chromatography (IEC). The boronate column has significantly increased retention of aggregated rhuMAb material under separation conditions optimized for the monomer form. Recombinant protein glycation initially occurred during production in mammalian cell culture, where feed sugar and protein concentrations contribute to the total overall glycation on this antibody product.     

Advanced microscale bioreactor system: a representative scale-down model for bench-top bioreactors

In recent years, several automated scale-down bioreactor systems have been developed to increase efficiency in cell culture process development. ambr™ is an automated workstation that provides individual monitoring and control of culture dissolved oxygen and pH in single-use, stirred-tank bioreactors at a working volume of 10–15 mL. To evaluate the ambr™ system, we compared the performance of four recombinant Chinese hamster ovary cell lines in a fed-batch process in parallel ambr™, 2-L bench-top bioreactors, and shake flasks. Cultures in ambr™ matched 2-L bioreactors in controlling the environment (temperature, dissolved oxygen, and pH) and in culture performance (growth, viability, glucose, lactate, Na⁺, osmolality, titer, and product quality). However, cultures in shake flasks did not show comparable performance to the ambr™ and 2-L bioreactors.     

High-end pH-controlled delivery of glucose effectively suppresses lactate accumulation in CHO fed-batch cultures

A simple method for control of lactate accumulation in suspension cultures of Chinese hamster ovary (CHO) cells based on the culture's pH was developed. When glucose levels in culture reach a low level (generally below 1 mM) cells begin to take up lactic acid from the culture medium resulting in a rise in pH. A nutrient feeding method has been optimized which delivers a concentrated glucose solution triggered by rising pH. We have shown that this high-end pH-controlled delivery of glucose can dramatically reduce or eliminate the accumulation of lactate during the growth phase of a fed-batch CHO cell culture at both bench scale and large scale (2,500 L). This method has proven applicable to the majority of CHO cell lines producing monoclonal antibodies and other therapeutic proteins. Using this technology to enhance a 12-day fed-batch process that already incorporated very high initial cell densities and highly concentrated medium and feeds resulted in an approximate doubling of the final titers for eight cell lines. The increase in titer was due to additional cell growth and higher cell specific productivity.     

Continuous optical in-line glucose monitoring and control in CHO cultures contributes to enhanced metabolic efficiency while maintaining darbepoetin alfa product quality

Great efforts are directed towards improving productivity, consistency and quality of biopharmaceutical processes and products. One particular area is the development of new sensors for continuous monitoring of critical bioprocess parameters by using online or in-line monitoring systems. Recently, we developed a glucose biosensor applicable in single-use, in-line and long-term glucose monitoring in mammalian cell bioreactors. Now, we integrated this sensor in an automated glucose monitoring and feeding system capable of maintaining stable glucose levels, even at very low concentrations. We compared this fed-batch feedback system at both low (< 1 mM) and high (40 mM) glucose levels with traditional batch culture methods, focusing on glycosylation and glycation of the recombinant protein darbepoetin alfa (DPO) produced by a CHO cell line. We evaluated cell growth, metabolite and product concentration under different glucose feeding strategies and show that continuous feeding, even at low glucose levels, has no harmful effects on DPO quantity and quality. We conclude that our system is capable of tight glucose level control throughout extended bioprocesses and has the potential to improve performance where constant maintenance of glucose levels is critical.     

Comparison of a production process in a membrane-aerated stirred tank and up to 1000-L airlift bioreactors using BHK-21 cells and chemically defined protein-free medium

The applicability of a protein-free medium for the production of recombinant human interleukin-2 with baby hamster kidney cells in airlift bioreactors was investigated. For this purpose, a BHK-21 cell line, adapted to grow and produce in protein-free SMIF7 medium without forming spheroids in membrane-aerated bubble-free bioreactors, was used as the producer cell line. First, cultivation of the cells was established at a 20-L scale using an internal loop airlift bioreactor system. During the culturing process the medium formulation was optimized according to the specific requirements associated with cultivation of mammalian cells under protein-free conditions in a bubble-aerated system. The effects of the addition of an antifoam agent on growth, viability, productivity, metabolic rates, and release of lactate dehydrogenase were investigated. Although it was possible to establish cultivation and production at a 20-L scale without the use of antifoaming substances, the addition of 0.002% silicon-oil-based antifoaming reagent improved the cultivation system by completely preventing foam formation. This reduced the release of lactate dehydrogenase activity to the level found in bubble-free aerated stirred tank membrane bioreactors and led to a reduction in generation doubling times by about 5 h (17%). Using the optimized medium formulation, cells were cultivated at a 1000-L scale, resulting in a culture performance comparable to the 20-L airlift bioreactor. For comparison, cultivations with protein-containing SMIF7 medium were carried out at 20- and 1000-L scales. The application of protein supplements did not lead to a significant improvement in the cultivation conditions. The results were also compared with experiments performed in a bubble-free aerated stirred tank membrane bioreactor to evaluate the influence of bubbles on the investigated culture parameters. The data implied a higher metabolic activity of the cells in airlift bioreactors with a 150% higher glucose consumption rate. The results of this study clearly demonstrate the applicability of a protein-free chemically defined medium for the production of recombinant proteins with BHK cells in airlift bioreactors.     

Towards industrial usefulness - cryo-cell-banking of transgenic BY-2 cell cultures

Plants have been established as an useful production system for commercially relevant proteins. Plant cell cultures show certain advantages compared to field-grown plants. However, one critical drawback for the long-term use of recombinant plant cell cultures is the instability of cell cultures concerning genetic background and productivity when maintained by subculturing. The ability to store recombinant cell lines stably by cryopreservation allows to maintain an efficient and stable production system. In this work, we describe the development of a cryopreservation protocol for a transgenic BY-2 cell culture expressing human serum albumin. In 1.75-L stirred-tank bioreactors growth and production kinetics of the transgenic cell line were compared after cryopreservation to the hitherto performed maintenance by subculturing. Growth and productivity of the cryopreserved cell culture remained stable after freezing for one week. Here, we show that we developed an efficient method which allows the storage of transgenic plant cell cultures, an important requirement for industrial processes.     

Production of mouse granulocyte-macrophage colony-stimulating factor by gateway technology and transgenic rice cell culture

To establish a production platform for recombinant proteins in rice suspension cells, we first constructed a Gateway-compatible binary T-DNA destination vector. It provided a reliable and effective method for the rapid directional cloning of target genes into plant cells through Agrobacterium-mediated transformation. We used the approach to produce mouse granulocyte-macrophage colony-stimulating factor (mGM-CSF) in a rice suspension cell system. The promoter for the αAmy3 amylase gene, which is induced strongly by sugar depletion, drove the expression of mGM-CSF. The resulting recombinant protein was fused with the αAmy3 signal peptide and was secreted into the culture medium. The production of rice-derived mGM-CSF (rmGM-CSF) was scaled up successfully in a 2-L bioreactor, in which the highest yield of rmGM-CSF was 24.6 mg/L. Due to post-translational glycosylation, the molecular weight of rmGM-CSF was larger than that of recombinant mGM-CSF produced in Escherichia coli. The rmGM-CSF was bioactive and could stimulate the proliferation of a murine myeloblastic leukemia cell line, NSF-60.     

Structural Mechanism of Ring-opening Reaction of Glucose by Human Serum Albumin

Glucose reacts with proteins nonenzymatically under physiological conditions. Such glycation is exacerbated in diabetic patients with high levels of blood sugar and induces various complications. Human albumin serum (HSA) is the most abundant protein in plasma and is glycated by glucose. The glycation sites on HSA remain controversial among different studies. Here, we report two protein crystal structures of HSA in complex with either glucose or fructose. These crystal structures reveal the presence of linear forms of sugar for both monosaccharides. The linear form of glucose forms a covalent bond to Lys-195 of HSA, but this is not the case for fructose. Based on these structures, we propose a mechanism for glucose ring opening involving both residues Lys-195 and Lys-199. These results provide mechanistic insights to understand the glucose ring-opening reaction and the glycation of proteins by monosaccharides.     

Rapid monitoring of recombinant antibody production by mammalian cell cultures using fourier transform infrared spectroscopy and chemometrics

Fourier transform infrared (FT‐IR) spectroscopy combined with multivariate statistical analyses was investigated as a physicochemical tool for monitoring secreted recombinant antibody production in cultures of Chinese hamster ovary (CHO) and murine myeloma non‐secreting 0 (NS0) cell lines. Medium samples were taken during culture of CHO and NS0 cells lines, which included both antibody‐producing and non‐producing cell lines, and analyzed by FT‐IR spectroscopy. Principal components analysis (PCA) alone, and combined with discriminant function analysis (PC‐DFA), were applied to normalized FT‐IR spectroscopy datasets and showed a linear trend with respect to recombinant protein production. Loadings plots of the most significant spectral components showed a decrease in the C–O stretch from polysaccharides and an increase in the amide I band during culture, respectively, indicating a decrease in sugar concentration and an increase in protein concentration in the medium. Partial least squares regression (PLSR) analysis was used to predict antibody titers, and these regression models were able to predict antibody titers accurately with low error when compared to ELISA data. PLSR was also able to predict glucose and lactate amounts in the medium samples accurately. This work demonstrates that FT‐IR spectroscopy has great potential as a tool for monitoring cell cultures for recombinant protein production and offers a starting point for the application of spectroscopic techniques for the on‐line measurement of antibody production in industrial scale bioreactors. Biotechnol. Bioeng. 2010; 106: 432–442. © 2010 Wiley Periodicals, Inc.     

Large-scale transient transfection of serum-free suspension-growing HEK293 EBNA1 cells: peptone additives improve cell growth and transfection efficiency

Large-scale transient transfection of mammalian cells is a recent and powerful technology for the fast production of milligram amounts of recombinant proteins (r-proteins). As many r-proteins used for therapeutic and structural studies are naturally secreted or engineered to be secreted, a cost-effective serum-free culture medium that allows their efficient expression and purification is required. In an attempt to design such a serum-free medium, the effect of nine protein hydrolysates on cell proliferation, transfection efficiency, and volumetric productivity was evaluated using green fluorescent protein (GFP) and human placental secreted alkaline phosphate (SEAP) as reporter genes. The suspension growing, serum-free adapted HEK293SF-3F6 cell line was stably transfected with an EBNA1-expression vector to increase protein expression when using EBV oriP bearing plasmids. Compared to our standard serum-free medium, concomitant addition of the gelatin peptone N3 and removal of BSA slightly enhanced transfection efficiency and significantly increased volumetric productivity fourfold. Using the optimized medium formulation, transfection efficiencies between 40-60% were routinely obtained and SEAP production reached 18 mg/L(-1). To date, we have successfully produced and purified over fifteen r-proteins from 1-14-L bioreactors using this serum-free system. As examples, we describe the scale-up of two secreted his-tagged r-proteins Tie-2 and Neuropilin-1 extracellular domains (ED) in bioreactors. Each protein was successfully purified to >95% purity following a single immobilized metal affinity chromatography (IMAC) step. In contrast, purification of Tie-2 and Neuropilin-1 produced in serum-containing medium was much less efficient. Thus, the use of our new serum-free EBNA1 cell line with peptone-enriched serum-free medium significantly improves protein expression compared to peptone-less medium, and significantly increases their purification efficiency compared to serum-containing medium. This eliminates labor-intensive and expensive chromatographic steps, and allows for the simple, reliable, and extremely fast production of milligram amounts of r-proteins within 5 days posttransfection.     

Dynamic analysis of GS-NS0 cells producing a recombinant monoclonal antibody during fed-batch culture

In this study we have analyzed the dynamic covariation of the mammalian cell proteome with respect to functional phenotype during fed-batch culture of NS0 murine myeloma cells producing a recombinant IgG(4) monoclonal antibody. GS-NS0 cells were cultured in duplicate 10 L bioreactors (36.5 degrees C, 15% DOT, pH 7.0) for 335 h and supplemented with a continuous feed stream after 120 h. Cell-specific growth rate declined continuously after 72 h of culture. Cell-specific recombinant monoclonal antibody production rate (qP) varied sixfold through culture. Whilst qP correlated with relative recombinant heavy chain mRNA abundance up to 216 h, qP subsequently declined, independent of recombinant heavy chain or light chain mRNA abundance. GS-NS0 cultures were sampled at 48 h intervals between 24 and 264 h of culture for proteomic analyses. Total protein abundance and nascent polypeptide synthesis was determined by 2D PAGE of unlabeled proteins visualized by SYPRO Ruby and autoradiography of (35)S-labeled polypeptides, respectively. Covariation of nascent polypeptide synthesis and abundance with biomass-specific cell growth, glucose and glutamate consumption, lactate and Mab production rates were then examined using two partial least squares regression models. Most changes in polypeptide synthesis or abundance for proteins previously identified by mass spectrometry were positively correlated with biomass-specific growth rate. We conclude that the substantial transitions in cell physiology and qP that occur during culture utilize a relatively constant complement of the most abundant host cell machines that vary primarily with respect to induced changes in cell growth rate.     

Efficient long-term and high-yielded production of a recombinant proteoglycan in eukaryotic HEK293 cells using a membrane-based bioreactor

Standard culture systems of eukaryotic cells generally failed to deliver sufficient amounts of recombinant proteins without increasing the costs of production. We here showed that membrane-based bioreactors, initially developed for the production of monoclonal antibodies, can be very useful for the production using engineered HEK293 cells, of a recombinant proteoglycan called endocan, with achievement of high level expression and efficient long-term production. When compared to standard procedures, the growth in suspension and at high density of these cells in one bioreactor promoted a 60-fold increase of the concentration of the soluble recombinant endocan. These culture conditions did not affect cell viability, stable expression, recognition by specific monoclonal antibodies or electrophoretic profile of the recombinant endocan. Such an easy to scale up system to produce recombinant protein should open soon new opportunities to study structure and functions of endocan or any other glycosylated cell products newly investigated.     

A simplified polyethylenimine-mediated transfection process for large-scale and high-throughput applications

Transient gene expression in mammalian cells is a valuable alternative to stable cell lines for the rapid production of large amounts of recombinant proteins. While the establishment of stable cell lines takes 2-6 months, milligram amounts of protein can be obtained within a week following transfection. The polycation polyethylenimine (PEI) is one of the most utilized reagents for small- to large-scale transfections as it is simple to use and, when combined with optimized expression vectors and cell lines, provides high transfection efficiency and titers. As with most transfection reagents, PEI-mediated transfection involves the formation of nanoparticles (polyplexes) which are obtained by its mixing with plasmid DNA. A short incubation period that allows polyplexes to reach their optimal size is performed prior to their addition to the culture. As the quality of polyplexes directly impacts transfection efficiency and productivity, their formation complicates scalability and automation of the process, especially when performed in large-scale bioreactors or small-scale high-throughput formats. To avoid variations in transfection efficiency and productivity that arise from polyplexes formation step, we have optimized the conditions for their creation directly in the culture by the consecutive addition of DNA and PEI. This simplified approach is directly transferable from suspension cultures grown in 6-well plates to shaker flasks and 5-L WAVE bioreactors. As it minimizes the number of steps and does not require an incubation period for polyplex formation, it is also suitable for automation using static cultures in 96-well plates. This "direct" transfection method thus provides a robust platform for both high-throughput expression and large-scale production of recombinant proteins.     

Integrated strategy of pH-shift and glucose feeding for enhanced production of bioactive Antrodin C in submerged fermentation of Antrodia camphorata

Antrodin C is one of the most potent bioactive components produced by the medicinal mushroom Antrodia camphorata. However, almost all studies in this field have focused on the biological activity of Antrodin C and relatively rare information has been reported regarding the biosynthetic process of Antrodin C. In this study, the strategies of pH-shift and glucose feeding for enhanced production of Antrodin C in submerged fermentation of A. camphorata were successfully applied in stirred bioreactors. The critical parameters for pH-shift and glucose feeding were systematically investigated. On one hand, the optimal culture pH for cell growth was distinct with Antrodin C biosynthesis and the maximum Antrodin C production was obtained by maintaining the first-stage culture at initial pH 4.5 and adjusted to 6.0 at day 8. On the other hand, it was beneficial for the Antrodin C accumulation with the initial glucose concentration of 40 g/L and feeding glucose to keep the residual sugar above 10 g/L. The maximum Antrodin C production (1,549.06 mg/L) was about 2.1-fold higher than that of control in 15-L stirred bioreactors by taking advantage of the integrated strategy of pH-shift and glucose feeding. These results would be helpful for the design of a highly efficient Antrodin C biosynthesis process.     

Enhanced bioprocess control to advance the manufacture of mesenchymal stromal cell-derived extracellular vesicles in stirred-tank bioreactors

Extracellular vesicles (EVs) derived from mesenchymal stromal cells (MSCs) act as signaling mediators of cellular responses. However, despite representing a promising alternative to cell-based therapies, clinical translation of EVs is currently limited by their lack of scalability and standardized bioprocessing. Herein, we integrated scalable downstream processing protocols with standardized expansion of large numbers of viable cells in stirred-tank bioreactors to improve EV production. Higher EV yields were linked to EV isolation by tangential flow filtration followed by size exclusion chromatography, rendering 5 times higher number of EVs comparatively to density gradient ultracentrifugation protocols. Additionally, when compared to static culture, EV manufacture in bioreactors resulted in 2.2 higher yields. Highlighting the role of operating under optimal cell culture conditions to maximize the number of EVs secreted per cell, MSCs cultured at lower glucose concentration favored EV secretion. While offline measurements of metabolites concentration can be performed, in this work, Raman spectroscopy was also applied to continuously track glucose levels in stirred-tank bioreactors, contributing to streamline the selection of optimal EV collection timepoints. Importantly, MSC-derived EVs retained their quality attributes and were able to stimulate angiogenesis in vitro, therefore highlighting their promising therapeutic potential.     

Oxidative stress-alleviating strategies to improve recombinant protein production in CHO cells

Large scale biopharmaceutical production of biologics relies on the overexpression of foreign proteins by cells cultivated in stirred tank bioreactors. It is well recognized and documented fact that protein overexpression may impact host cell metabolism and that factors associated with large scale culture, such as the hydrodynamic forces and inhomogeneities within the bioreactors, may promote cellular stress. The metabolic adaptations required to support the high-level expression of recombinant proteins include increased energy production and improved secretory capacity, which, in turn, can lead to a rise of reactive oxygen species (ROS) generated through the respiration metabolism and the interaction with media components. Oxidative stress is defined as the imbalance between the production of free radicals and the antioxidant response within the cells. Accumulation of intracellular ROS can interfere with the cellular activities and exert cytotoxic effects via the alternation of cellular components. In this context, strategies aiming to alleviate oxidative stress generated during the culture have been developed to improve cell growth, productivity, and reduce product microheterogeneity. In this review, we present a summary of the different approaches used to decrease the oxidative stress in Chinese hamster ovary cells and highlight media development and cell engineering as the main pathways through which ROS levels may be kept under control.     

Early glycation products of endothelial plasma membrane proteins in experimental diabetes

The participation of glucose and two intermediates of glucose metabolism: glucose-6-phosphate (G6P) and glyceraldehyde-3-phosphate (Gald3P) to the formation of early glycation products was comparatively evaluated in the endothelial plasma membrane of streptozotocin-induced diabetic rats. Antibodies risen to a carrier protein reductively glycated by each of the sugars mentioned above were used to probe by immunoblotting the proteins of the lung microvascular endothelium plasmalemma purified from normal and diabetic rats. The amount of glycated endothelial plasma membrane proteins was below the limit of detection in normoglycemic animals but increased dramatically in diabetic animals for glucose and G6P. In contrast, no signal was found in diabetic rats for Gald3P, indicating that either the contribution of this phosphotriose to the glycation of intracellular proteins is negligible in vivo, or the Schiff base generated by this sugar transforms very rapidly into products of advanced glycation. Globally, the endothelial plasma membrane proteins bound on average 300 times more glucose than G6P proving that, in spite of its low in vitro potency as glycating agent, glucose represents the main contributor to the intracellular formation of early glycation products. The most abundant glycated proteins of the lung endothelial plasma membrane were separated by two dimensional electrophoresis and identified by mass spectrometry.     

A systematic approach for scale-down model development and characterization of commercial cell culture processes

The objective of process characterization is to demonstrate robustness of manufacturing processes by understanding the relationship between key operating parameters and final performance. Technical information from the characterization study is important for subsequent process validation, and this has become a regulatory expectation in recent years. Since performing the study at the manufacturing scale is not practically feasible, development of scale-down models that represent the performance of the commercial process is essential to achieve reliable process characterization. In this study, we describe a systematic approach to develop a bioreactor scale-down model and to characterize a cell culture process for recombinant protein production in CHO cells. First, a scale-down model using 2-L bioreactors was developed on the basis of the 2000-L commercial scale process. Profiles of cell growth, productivity, product quality, culture environments (pH, DO, pCO2), and level of metabolites (glucose, glutamine, lactate, ammonia) were compared between the two scales to qualify the scale-down model. The key operating parameters were then characterized in single-parameter ranging studies and an interaction study using this scale-down model. Appropriate operation ranges and acceptance criteria for certain key parameters were determined to ensure the success of process validation and the process performance consistency. The process worst-case condition was also identified through the interaction study.