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What Can Cell Culture Flocculation Offer for Antibody Purification Processes

What Can Cell Culture Flocculation Offer for Antibody Purification Processes

Editorial

2 Editorial What can culture offer for antibody purification processes

“The eventual goal of the application of flocculation in monoclonal antibody processing is to develop a separation alternative to , with equivalent separation efficiency, Pharm. Bioprocess. high process capacity, good facility fit and sound process economics.”

Keywords: antibody • flocculation • harvest • impurity removal • purification

Recent advances in cell culture processes solid content with wide particle distribution Yun (Kenneth) Kang have significantly increased monoclonal anti- and a high percentage of small particles fur- Author for correspondence: body (mAb) titers to levels as high as 30 g/l. ther complicate the harvest unit operation, BioProcess Sciences, Eli Lilly Not unexpectedly, these improvements have requiring significantly higher & Company, 450 East 29th Street, New York, NY 10016, USA resulted in a new set of starting conditions surface area which may exceed the existing [email protected] for , including: ele- train capacity. Harvest operations vated cell density levels (up to 108 cells/ml), have become extremely challenging, if not Dale L Ludwig BioProcess Sciences, Eli Lilly increased solid content (packed cell volume, impossible because of these issues. & Company, 450 East 29th Street, up to 40%) and increased soluble impurity Flocculation has been widely used for New York, NY 10016, USA levels such as host cell (HCP) and many years in the chemical and food indus- Paul Balderes high molecular weight species (HMW; up tries, as well as in . In BioProcess Sciences, Eli Lilly to 40%) [1–4] . New advances in mAb down- recent years, flocculation-based pretreatment & Company, 450 East 29th Street, stream processing are critically needed, in of cell cultures to circumvent both harvest New York, NY 10016, USA order to meet the significant challenges posed and purification issues experienced in mAb by increased cell culture productivity. production has been explored and imple- Purification productivity can potentially mented [2–4,10–14], and is in effect a strategy be improved in a number of ways: through with the potential to ‘kill two birds with one process intensification by increasing chro- stone’. matography column dimensions, operating Many flocculation agents or flocculants, 6 in multiple production cycles, utilizing high ranging from simple electrolytes to synthetic capacity or mixed-mode chromatographic (or polymers) have been resins or membrane adsorbers or by reduc- investigated. Flocculation is the agglomera- ing the number of necessary purification tion of particles (cells, cell debris or 2014 steps [5–8]. However, elevated levels of HCP in mammalian cell culture) caused by a bridg- and HMW in high cell density culture place ing effect induced by the flocculant. Floccu- greater demands on purification unit opera- lation agents are adsorbed to particles largely tions, often necessitating the use of novel or through electrostatic attraction although alternative technology to mitigate the higher additional interactive forces such as hydro- burden placed on downstream steps [1–4,9]. phobic interaction or hydrogen bonding may Additionally, increases in cell quantity, be involved [2,15–16]. Flocculated cell culture cell debris and colloids from high cell den- has a higher mean particle size compared sity culture pose significant challenges to the with untreated cell culture and increased harvest process, placing a greater burden on mean particle size has been observed to con- the and/or clarification filter sistently correlate with improved filterability. train. Culture suspensions containing high Notably, positively charged flocculants, such

10.4155/PBP.14.33 © 2014 Future Science Ltd Pharm. Bioprocess. (2014) 2(6), 483–485 ISSN 2048-9145 483 Editorial Kang, Ludwig & Balderes

as polyamines [12], calcium chloride/potassium phos- graphic resins, particularly A. Third, removal phate [14], chitosan [13], polydiallyldimethyl ammo- of impurities prior to Protein A could reduce the nium chloride [3,4] and stimulus responsive polymer number of chromatographic steps and enable a two- [2] have been shown to be successful in inducing floc- column purification platform, with greater flexibility culation, resulting in improved clarification efficiency, in the selection of the second chromatographic step. process yield and clearance of impurities during the The second chromatography column could potentially primary mAb recovery process from mammalian cell be developed primarily for viral clearance purposes. culture. Membrane chromatography suitable for high produc- It has been shown that flocculation of cell culture tivity or continuous processing might also be explored can enhance the removal of cells and cell debris via [5,19]. Therefore, introduction of flocculant into the centrifugation, or depth filtration and harvest process could result in a simplified and more increase filtration throughput or capacity[2, 13,17–18]. robust purification process and/or provide greater For example, chitosan used as a flocculant in mamma- process flexibility for mAb downstream processing, lian cell culture significantly improved centrifugation potentially paving the way for the implementation efficiency as indicated by reduced centrate , of a fully disposable and/or continuous purification resulting in a six- to seven-fold increase in the volumet- manufacturing process. ric throughput of the subsequent depth filtration step Finally, charged flocculants may serve as viral clear- [13] . In another case, depth filter capacity was increased ance agent through their ability to bind oppositely by more than eightfold when cell culture was floccu- charged viruses [10,17], thus providing an orthogo- lated with a smart polymer [2]. In each case, process nal viral removal step, again adding flexibility to the economics were improved due to reduction in filter manufacturing operation. costs and enhancement of process robustness, while In summary, flocculation may enable the develop- process yield and product quality were not adversely ment of a robust harvest process with the benefit of affected. removing potential obstacles to the downstream pro- cess. However, implementation of flocculation at com- mercial manufacturing scale should be assessed on a If flocculation is to be considered for use in “ case-by-case basis. The compatibility of flocculation to harvest operations, due diligence must be harvest unit operation, disk stack centrifugation, depth performed to verify its impact on downstream filtration or microfiltration, should first be evaluated chromatography operations. ” prior to implementation for an existing facility. Any cell culture, up to 2000 l, can be pretreated by floccu- Removal of process or product-related impurities lant directly in a and then clarified by depth such as HCP, host DNA and HMW is an additional filter trains, making it attractive for high titer and low benefit that flocculation may provide. Introduction of volume cell culture processes. When cell culture scale a smart polymer directly into a bioreactor was demon- is larger than 2000 l, a high-capacity depth filtration strated to result in reduced impurity levels in Protein device should be evaluated in order to ensure com- A eluate, meeting the requirements of drug substance patibility with flocculation. Due to the high packed and, thereby, reducing the impurity load to subsequent cell volume, alternatively, settlement of cells and cell purification steps[2] . Furthermore, a synergistic effect debris for high cell density culture can be evaluated on impurity removal was observed when flocculation to increase filtration capacity, and decrease filtration was combined with acid precipitation [2]. The combi- area. However, the behaviors of the flocculated nation of flocculation and acid precipitation may there- culture need to be studied to ensure that the operation fore be beneficial and should be explored if the target can be performed within a reasonable timeframe and antibody is stable in tested acidic conditions. without negatively impacting product quality. Novel Separation of soluble impurities from antibody strategies may also be investigated to recover the mAb product during harvest can reduce the overall impu- product from settled cell pellets if needed. rity load to downstream purification steps, which may If flocculation is to be considered for use in harvest have several benefits. First, a higher product/impurity operations, due diligence must be performed to verify ratio could permit increased load on subsequent chro- its impact on downstream chromatography operations. matographic steps, resulting in higher capacity chro- Due to potential flocculant toxicity, residual flocculant matography unit operations. Second, a higher purity levels in the drug substance should be assessed and harvested culture fluid with lower centrate turbidity acceptable clearance must be reached to ensure the and soluble impurity levels can potentially increase the safety of the drug product [2,20]. The obvious advan- number of operation cycles and lifetime of chromato- tage of flocculation using stimulus responsive polymer

484 Pharm. Bioprocess. (2014) 2(6) future science group What can cell culture flocculation offer for antibody purification processes Editorial and precipitation using simple acids is that there is process performance in current platform downstream little concern on the residual level [2,14,18]. processes. The eventual goal of the application of floccula- tion in mAb processing is to develop a separation unit Financial & competing interests disclosure operation alternative to chromatography, with equiva- The authors have no relevant affiliations or financial involve- lent separation efficiency, high process capacity, good ment with any organization or entity with a financial inter- facility fit and sound process economics. Shorter pro- est in or financial conflict with the subject matter or mate- cess development times and simpler scale-up proce- rials discussed in the manuscript. This includes employment, dures relative to a chromatography step could provide consultancies, honoraria, stock ownership or options, expert a in cases where mAbs or antibody-based mol- testimony, grants or patents received or pending or royalties. ecules such as bispecific antibodies produced in high No writing assistance was utilized in the production of this cell density culture demonstrate poor purification manuscript.

References 11 Parkkinen J, Rahola A, Von Bonsdorff L, Tolo H, Torma E. A modified caprylic acid method for manufacturing 1 Follstad BD, McCoy RE, Morris AE. WO2013006479A2 immunoglobulin G from human plasma with high yield and (2013). efficient virus clearance.Vox Sang. 90(2), 97–104 (2006). 2 Kang YK, Hamzik J, Felo M et al. Development of a novel 12 Peram T, McDonald P, Carter-Franklin J, Fahrner R. and efficient cell culture flocculation process using a stimulus Monoclonal antibody purification using cationic responsive polymer to streamline antibody purification polyelectrolytes: an alternative to column chromatography. processes. Biotechnol. Bioeng. 110(11), 2928–2937 (2013). Biotechnol. Prog. 26(5), 1322–1331 (2010). 3 McNerney TM, Petty K, Thomas A, Zhao X. 13 Riske F, Schroeder J, Belliveau J, Kang X, Kutzko J, WO2013090820A1 (2013). Menon MK. The use of chitosan as a flocculant in 4 Zhao X, Petty K, McNerney TM et al. Developing recovery mammalian cell culture dramatically improves clarification clarification processes for mammalian cell culture with high throughput without adversely impacting monoclonal density and high solid content. Presented at: 243rd ACS antibody recovery. J. Biotechnol. 128(4), 813–823 (2007). National Meeting and Exposition. San Diego, CA, USA, 14 Romero JK, Chrostowski J, De Vilmorin PG, Case JY. 25–29 March 2012. US2010/0145022A1 (2010). 5 Kang Y, Ng S, Lee J et al. Development of an alternative 15 Aunins JG, Wang D. Induced flocculation of animal cells monoclonal antibody polishing step. Biopharm. Int. 25(5), in culture. Biotechnol. Bioeng. 34(5), 629–638 34–46 (2012). (1989). 6 Kelley B. Very large scale monoclonal antibody purification: 16 Roush DJ, Lu Y. Advances in primary recovery: the case for conventional unit operations. Biotechnol. centrifugation and membrane technology. Biotechnol. Prog. Prog. 23(5), 995–1008 (2007). 24(3), 488–495 (2008). 7 Sengar T, Rathore A. Achieving process intensification by 17 Brodsky Y, Zhang C, Yigzaw Y, Vedantham G. Caprylic acid scheduling and debottlenecking biotech processes. Biopharm. precipitation method for impurity reduction: an alternative Int. 24(2), 44–53 (2011). to conventional chromatography for monoclonal antibody 8 Shukla AA, Hubbard B, Tressel T, Guhan S, Low D. purification. Biotechnol. Bioeng. 109(10), 2589–2598 (2012). Downstream processing of monoclonal antibodies- 18 Westoby M, Chrostowski J, De Vilmorin P, Smelko JP, application of platform approaches. J. Chromatogr. B Analyt. Romero JK. Effects of solution environment on mammalian Technol. Biomed. Life Sci. 848(1), 28–39 (2007). cell fermentation broth properties: enhanced impurity 9 Hove S, Cacace B, Felo M, Chefer K. Development of a removal and clarification performance. Biotechnol. Bioeng. robust clarification process for high density mammalian cell 108(1), 50–58 (2011). culture processes. Presented at: . Presented at: Recovery of 19 Zhou JX, Tressel T. Basic concepts in Q membrane Biological Products XIV. Lake Tahoe, CA, USA, 1–5 August chromatography for large-scale antibody production. 2010. Biotechnol. Prog. 22(2), 341–349 (2006). 10 Lebing W, Remington KM, Schreiner C, Paul HI. Properties 20 Fischer D, Li Y, Ahlemeyer B, Krieglstein J, Kissel T. In vitro of a new intravenous immunoglobulin (IGIV-C, 10%) cytotoxicity testing of polycations: influence of polymer produced by virus inactivation with caprylate and column structure on cell viability and hemolysis. Biomaterials 24(7), chromatography. Vox Sang. 84(3), 193–201 (2003). 1121–1131 (2003).

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