Most biopharmaceutical

Transcription

1 B i op r o c e s s Technical Fed-Batch Cell Culture Process Optimization A Rationally Integrated Approach Zhou Jiang, Kurt Droms, Zhaohui Geng, Susan Casnocha, Zhihua Xiao, Steve Gorfien, and Scott J. Jacobia Most biopharmaceutical production platforms are based on fed-batch cell culture protocols, which can support high volumetric productivity while maintaining low operational complexity (1). The industry is interested in developing or refining high-titer cell culture processes to meet increasing market demands and reduce manufacturing costs (2). Although advancements in cell engineering have enabled development of highperforming recombinant cell lines (3 6), improvements in cell culture media and process parameter settings are required to realize the maximum production potentials of those cells (7 8). In a fed-batch process, a basal medium supports initial growth and production, and a feed medium prevents depletion of nutrients and sustains the production phase (9). Those media can contain different assortments of nutrients to accommodate the distinct metabolic requirements during different Pr o d u c t Fo c u s: Antibodies a n d other proteins Process Focus: Pr o d u c t i o n Wh o Sh o u l d Re a d: An a l y t i c a l a n d process development personnel Ke y w o r d s : Me d i a, supplements, CHO cells, design of experiments, titer Le v e l: Intermediate production phases. Process parameter settings including feeding strategy and control parameters define the chemical and physical environments suitable for cell growth and protein production. Optimization of a fedbatch process can be achieved by development efforts addressing one or more of three major elements: basal medium, feed medium, and process settings. Given the large sets of variables in these systems, establishing a cost- and time-efficient approach for process optimization is desired but challenging. Through a study aiming to upgrade a fed-batch process, we observed that basal and feed media have interrelated impacts on process outcomes (a pairing effect ). So we required a combined optimization of basal and feed media to fulfill our objective. Here we discuss a rationally integrated approach that best serves the practices of fed-batch cell culture process optimization. Materials and Methods Chinese Hamster Ovary Cells: We used a recombinant GS-CHO cell line (both the CHOK1SV host cell line and glutamine synthetase expression vector licensed from Lonza Biologics) expressing a monoclonal antibody as the model cell line in our study. Existing Fed-Batch Cell Culture Process: Development of the existing control fed-batch process has been detailed elsewhere (). Briefly, a chemically defined medium was chosen as the basal medium, and a chemically defined feed medium was developed through a multiround statistical design of experiment (DoE) study. The process was successfully applied to both NS and CHO cell cultures. Optimization of the Process: We conducted our optimization studies using either shake flasks (Corning) or Cellferm-Pro bioreactors (DASGIP BioTools). Cells were adapted over at least three passages into the test medium variants before evaluation in cell growth performance assays. Initial bioreactor culture volume was ml. We controlled ph at 7. ±. and dissolved oxygen (DO) at 3%. Culture conditions followed the existing control process except for our designed variables. We measured cell densities and viabilities using a Vi-Cell counter (Beckman Coulter) and measured concentrations of glucose, ammonia, and lactate with a BioProfile analyzer (Nova Biomedical). We determined monoclonal antibody titers using a POROS 2-µm protein A ID 4 BioProcess International (3) Ma r c h 212

2 Figure 1: Baseline performance of batch and fed-batch cell culture processes; both were seeded at 3 x vc/ml. The fed-batch culture was fed with a control feed at 1.6% volume per day starting from day 3, and the batch control culture was maintained without feeding. Terminal IgG titers are shown relative to the batch control condition. Viable Cell Density ( 6 cells/ml) Fed-Batch Batch Figure 3: Cell growth and IgG titers from the top media mixture and control medium; cells were seeded at 3 vc/ml and cultured in batch mode. Day 7 IgG titers are shown relative to the batch control condition. Viable Cell Density ( 6 cells/ml) Top Media Mixture Medium cartridge affinity column (Life Technologies) controlled by a Waters 269 Alliance system with 2998 photodiode array detector set at 2 nm (Waters), using a purified IgG standard to establish the standard curves in each measurement. Re s u lt s Baseline Performance of the Process: We assessed our existing control process using the model cell line to establish baseline performance. As Figure 1 shows, the fed-batch process reached a peak viable cell (vc) density of 19 6 cells/ml, and the batch process (run as a control without feeding) had a peak viable cell density of 7 6 cells/ml. The feed in this process demonstrated a high baseline performance by yielding an 8.-fold titer increase over the batch control process. The IgG titer from our fed-batch process reached the multigram per liter range, which is regarded in the industry as high for a platform process. Optimization Workflow: Figure 2 depicts our optimization workflow. This project included two major phases: Phase 1 dealt with basal medium development following a three-step DoE path, and phase 2 involved a feed DoE study followed by a combined feed and process optimization. We conducted basal medium optimization through three steps of DoE experiments. First, we used a Figure 2: Optimization work-flow chart; the project had two phases, each including multiple steps. Phase 1 focused on basal medium optimization, phase 2 on feed and process optimization. } Media Mixture DoE Two-Level Phase 1: Factorial DoE Basal Medium Optimization Central Composite DoE Two-Level Factorial Feed DoE Integrated Feed and Process Optimization } Phase 2: Feed and Process Optimization media mixture DoE study to identify a basal medium formulation as a starting point for medium optimization. Our second step was a two-level factorial DoE study testing the effects of multiple nutrient groups supplementing the basal medium. The final step was a central composite DoE to determine the optimal concentrations of functional nutrient groups identified in the previous step. The media mixture layout we designed using Design-Expert software (Stat-Ease), consisted of 1 unique mixtures of four chemically defined prototype formulations. We evaluated our media mixtures with a batch cell growth performance assay. A top media mixture was identified that outperformed the control basal medium by giving 8% higher peak cell densities and 2% higher IgG titers (Figure 3). In our two-level factorial DoE study, we selected five nutrient groups to evaluate how they affect protein titer when used as basal medium supplements at two concentrations (added or not) to the top media mixture. We designed a total of 16 basal medium variants with various combinations of those five nutrient groups and assessed them in a fedbatch cell growth performance assay using the existing control feed for all conditions. As Figure 4 (left) shows, the cell cultures exhibited a wide range of growth responses to supplementation of the nutrient groups. Multiple supplemented media supported higher peak cell densities than the control condition. However, their boosted cell growth did not translate to a gain in IgG titer; none of the medium variants improved IgG titer over the control (Figure 4, right). That was contradictory to the previous batch culture evaluation of media mixtures in which improved IgG titers were observed, suggesting that the feed may have been playing a dominant role in IgG production for this process. Furthermore, statistical analyses of the results revealed that two nutrient groups had a negative effect and one Ma r c h 212 (3) BioProcess International 41

3 Figure 4: Two-level factorial DoE experiment on cell growth and IgG titers; all conditions were seeded at 3 vc/ml and fed with the original control feed at 1.6% volume per day starting day 3; (left) cell growth curves; (right) IgG titers at harvest (shown relative to fed-batch control condition denoted by the red dotted line). Viable Cell Density ( 6 cells/ml) M1 M3 M M7 M9 M11 M13 M1 M2 M4 M6 M8 M M12 M14 M Medium Variants nutrient group had a positive effect on IgG titer (p <.). In a central composite DoE study, we regrouped select nutrient groups and tested them at five different concentrations encompassing a wider range than our two-level factorial study. We designed 1 medium variants for evaluation of three nutrient groups. All variants were tested in a fed-batch growth performance assay to which the original control feed was applied. As Figure shows, this round of optimization improved cell growth; however, that did not translate into increased IgG titer. Cell growth was largely improved through basal medium optimization. By contrast, IgG-specific productivity which characterizes average productivity per cell was drastically reduced (data not shown). So an increase in titer was not achieved. Optimally in a fed-batch cell culture process, the basal medium supports cells through their growth phase and thus plays a major role in cell growth, whereas the feed medium sustains cells through the production phase for a primary contribution of increasing IgG productivity. When basal medium optimization improved cell growth, we hypothesized that a corresponding feed optimization would be required to increase the IgG titer of our fed-batch process. Further, we hypothesized that process parameters might need to be altered to realize the full potential of our new medium and feed combination. Feed Optimization: In this project, we optimized feed by testing nutrient groups as supplements to the existing feed. We selected five nutrient groups for screening at two levels: high level (with supplements added back to the control feed) and low level (the control feed without supplementation). A total of 17 feed variants reflected different combinations of supplementing the nutrient groups. In the fed-batch cell growth performance assay, we seeded all conditions in the same basal medium (the top medium identified in phase 1), feeding each one with the designated feed variant. As Figure 6 shows, multiple test conditions outperformed the control fedbatch process with regard to IgG titer, with the top condition demonstrating a 1% increase. This improvement suggested that the fed-batch process may benefit from the pairing effect described above. The control feed was originally developed to specifically match the original basal medium, which gave a high baseline performance (11). After basal medium optimization, feed modification became necessary to better match the new basal medium for superior process Figure : Central composite DoE experiment cell growth and IgG titers; all conditions were seeded at the 3 vc/ml and fed with the original control feed at 1.6% volume per day starting day 3; (left) cell growth curves; (right) IgG titers at harvest (shown relative to fed-batch control condition denoted by the red dotted line). Viable Cell Density ( 6 cells/ml) C1 C3 C C7 C9 C11 C13 C1 C2 C4 C6 C8 C C12 C BioProcess International (3) March Medium Variants

4 outcome. We conducted statistical analyses and identified two nutrient groups with significant positive effects on IgG production (p <.). Our final study was an integrated feed and process optimization. We designed five feed variants to test different concentrations of nutrient groups identified as having a significant positive effect on protein titer in our previous experiment. Using a fed-batch growth performance assay, we tested these variants in conjunction with multiple process parameters: seeding density, feeding schedule, and temperature shift. We seeded all conditions in the same basal medium, feeding each condition with the designated variant under different process settings. As Figure 7 depicts, this round of integrated optimization further improved IgG titer, with the top condition 4% higher than the control fed-batch process. This titer improvement could be primarily linked to increased IgGspecific productivity (data not shown); the accompanying cell growth augmentation was only marginal. This study involved an integrated optimization combining both feed and process optimization in one step. Although feed development and process Figure 6: Cell growth and IgG titers in the two-level factorial feed optimization study; all conditions were seeded in the same basal medium at 3 vc/ml. Each condition was fed with the designated feed variant; (left) cell growth curves; (right) IgG titers at harvest (shown relative to fed-batch control condition denoted by the red dotted line). Viable Cell Density ( 6 cells/ml) F1 F3 F F7 F9 F11 F13 F1 F17 F2 F4 F6 F8 F F12 F14 F Feed Variants FROM SCRATCH TO BATCH GMP PRODUCTION OF BIOLOGICS CREATING TOMORROW S SOLUTIONS Just give us your protein sequence and we ll do the rest. Working closely with you, we ll put our process development skills and project management expertise at your service, providing you with a GMP batch of your product highly efficient, professionally and on time. Team up with the leading innovator in E. coli production technologies and learn about ESETEC, our unique E. coli secretion technology. Visit Wacker Biotech GmbH, Jena, Germany, Tel , info.biologics@wacker.com

5 Figure 7: Cell growth and IgG titers in the integrated feed and process optimization; all conditions were seeded in the same basal medium. Each condition was fed with designated feed variant under various process settings; (a) cell growth curves; (b) IgG titers at harvest (shown relative to fedbatch control condition denoted by the red dotted line). Viable Cell Density ( 6 cells/ml) Conditions. Fully integrated optimization is challenging because of the many experimental conditions required. optimization are usually addressed in separate studies, this integrated approach can be used to deliver superior results in a shortened period. Di s c u s s i o n Basal medium, feed medium, and process parameter settings are the three major factors for fed-batch cell culture process optimization. Performance can be improved by upgrading one or more of those three elements. In phase 1 of our study, extensive basal medium development efforts improved cell growth in a fed-batch process, but IgG titer did not increase because specific productivity decreased. Subsequent feed optimization in phase 2 promptly indentified a modified feed that better matched the new basal medium developed in phase 1 and outperformed the original fed-batch control process with regard to IgG titer by restoring specific productivity. The benefit of pairing basal and feed media supports the idea that the two Figure 8: Comparing top IgG titers achieved in each step (listed chronologically); steps 1 represent the control fed-batch process, twolevel factorial DoE, central composite DoE, two-level factorial feed DoE, and integrated feed/process development, respectively. Data are relative to the control fed-batch process (denoted by the red dotted line) Step have interrelated impacts on cell culture performance. An upgraded basal medium can induce notable changes in the growth and metabolism of cells and therefore may require an accordingly modified feed to accommodate the nutrient demands of those cells. For fedbatch process optimization, improving a single element may be insufficient to improve the overall process outcome and require development efforts on the other elements. Optimization of all three elements in our fed-batch process was necessary to realize its maximal protein production potential. As Figure 8 shows, protein titer increases were not seen in this study until basal and feed were optimized in tandem. All three elements can be optimized in different ways. The most straightforward, serial approach sequentially optimizes basal medium, feed medium, and process settings. However, that overlooks the nature of networked interactions among the three elements and thus may not guarantee an optimal outcome. An iterative optimization, in which sequential optimization of one or more elements is repeated until desired results are reached, can further propel a process toward its optimal point (4). However, that approach prolongs development timelines. As a more sophisticated strategy, a fully integrated approach with simultaneous optimization of all three elements is ideal for identifying the globally optimal condition. However, implementation of the fully integrated optimization is challenging because of the many experimental conditions required, which can be on the order of thousands and exceed current development capacity. Instead, we used a semiintegrated protocol. The basal medium and feed medium were optimized sequentially, followed by a final round of integrated optimization of feed and process settings. Our approach differs from a fully integrated optimization by involving sequential steps while taking advantage of the power of multiplexed integration. This is an example of rationally integrated optimization. Under that concept, integrated optimization can be rationally designed to meet requirements and deliver significantly improved process performance. 44 BioProcess International (3) Ma r c h 212

6 Th e Best o f Bo t h Wo r l d s Because the basal medium, feed medium, and process parameter settings have interrelated roles in a fed-batch process, optimization of all three elements may be required to maximize process outcomes. A fully integrated strategy with simultaneous optimization of all elements would allow for process optimization within a shorter timeline than a sequential approach requires. However, implementing a full integration can be challenging because of the required large set of experimental conditions. As an alternative, rationally integrated approaches can be designed and used to overcome those limitations and deliver desired results for fed-batch cell culture process development. Acknowledgments The authors thank Peggy Lio and Rickard Fike for their input as well as Jaime Goldfuss and Aaron Schrader for analytical support. References 1 Fike R. Nutrient Supplementation Strategies for Biopharmaceutical Production, Part 1: Identifying a Formulation. BioProcess Int. 7() 29: Birch JR, Racher AJ. Antibody Production. Adv. Drug Deliv. Rev. 8, 26: Wurm FM. Production of Recombinant Protein Therapeutics in Cultivated Mammalian Cells. Nat. Biotechnol. 22 (11) 24: Dinnis DM, James DC. Engineering Mammalian Cell Factories for Improved Recombinant Monoclonal Antibody Production: Lessons from Nature? Biotechnol. Bioeng. 91, 2: Barnes LM, Dickson AJ. Mammalian Cell Factories for Efficient and Stable Protein Expression. Curr. Opin. Biotechnol. 17, 26: Rita Costa A, et al. Guidelines to Cell Engineering for Monoclonal Antibody Production. Eur. J. Pharm. Biopharm. 74, 2: Gorfien S. Chapter : Cell Culture Media Development: Customization of Animal Origin-Free Components and Supplements. Cell Culture and Upstream Processing. Butler M, Ed. Garland Science Publishing: New York, NY, Oxford, UK, 27: Li F, et al. Cell Culture Processes for Monoclonal Antibody Production. MAbs 2() 2: Fike R. Nutrient Supplementation Strategies for Biopharmaceutical Production, Part 2: Feeding for Optimal Recombinant Protein Production. BioProcess Int. 7(11) 29: Ma N, et al. A Single Nutrient Feed Supports Both Chemically Defined NS and CHO Fed-Batch Processes: Improved Productivity and Lactate Metabolism. Biotechnol. Prog. 2() 29: Pacis E, et al. Systematic Approaches to Develop Chemically Defined Cell Culture Feed Media. BioPharm Int. 23(11) 2: Corresponding author Zhou Jiang is a staff scientist, Zhihua Xiao and Scott J. Jacobia are senior managers, and Steve Gorfien is senior director in bioproduction R&D at Life Technologies, 317 Staley Road, Grand Island, NY 1472; , fax ; zhou.jiang@lifetech.com; Kurt Droms and Susan Casnocha are associate research fellows, and Zhaohui Geng is senior manager of biotherapeutics R&D at Pfizer Corporation, 7 Chesterfield Parkway West, Chesterfield, MO Your partner in Hydrolysate innovation Proyield for Biopharma Cost effective productivity enhancement To order reprints of this article, contact Rhonda Brown (rhondab@ fosterprinting.com) Download a low-resolution PDF online at