Foaming and media surfactant effects on the cultivation of animal cells in stirred and sparged bioreactors

Recent developments in high cell density and high productivity fed-batch animal cell cultures have placed a high demand on oxygenation and carbon dioxide removal in bioreactors. The high oxygen demand is often met by increasing agitation and sparging rates of air/O2 in the bioreactors. However, as we demonstrate in this study, an increase of gas sparging can result in cell damage at the sparger site due to high gas entrance velocities. Previous studies have showed that gas bubble breakup at the culture surface was primarily responsible for cell damage in sparged bioreactors. Such cell damage can be reduced by use of surfactants such as Pluronic F-68 in the culture. In our results, where NS0 cells were grown in a protein-free and cholesterol-free medium containing 0.5 g/L Pluronic F-68, high gas entrance velocity at the sparger site was observed as the second mechanism for cell damage. Experiments were performed in scaled-down spinners to model the effect of hydrodynamic force resulting from high gas velocities on antibody-producing NS0 cells. Cell growth and cell death were described by first-order kinetics. Cell death rate constant increased significantly from 0.04 to 0.18 day(-1) with increasing gas entrance velocity from 2.3 to 82.9 m/s at the sparger site. The critical gas entrance velocity for the NS0 cell line studied was found to be approximately 30 m/s; velocities greater than 30 m/s caused cell damage which resulted in reduced viability and consequently reduced antibody production. Observations from a second cholesterol-independent NS0 cell line confirmed the occurrence of cell damage due to high gas velocities. Increasing the concentration of Pluronic F-68 from 0.5 to 2 g/L had no additional protective effect on cell damage associated with high gas velocity at the sparger. The results of gas velocity analysis for cell damage have been applied in two case studies of large-scale antibody manufacturing. The first is a troubleshooting study for antibody production carried out in a 600 L bioreactor, and the second is the development of a gas sparger design for a large bioreactor scale (e.g., 10,000 L) for antibody manufacturing.

Section: Bubble Size and Gas-liquid Interfacementioning

confidence: 67%

NS0 cell damage by high gas velocity sparging in protein‐free and cholesterol‐free cultures

Zhu

Cuenca

Zhou

et al. 2008

“…To inhibit foam formation upon sparging due to the high protein content of the media, Antifoam C (AFC, a silicon-based substance used in cell culture) is frequently added to the culture medium (van der Pol et al, 1993;Zhang et al, 1992). To determine whether AFC has a deleterious effect on ES cells, J1 cells were cultured in the presence of different concentrations of AFC, and cell viability was monitored via an MTT assay.…”

Section: Es Cell Vitality Is Not Affected By Antifoam Cmentioning

confidence: 99%

Differentiation and lineage selection of mouse embryonic stem cells in a stirred bench scale bioreactor with automated process control

Schroeder

Niebruegge

Werner

et al. 2005

164

138

It is well established that embryonic stem (ES) cells can differentiate into functional cardiomyocytes in vitro. ES-derived cardiomyocytes could be used for pharmaceutical and therapeutic applications, provided that they can be generated in sufficient quantity and with sufficient purity. To enable large-scale culture of ES-derived cells, we have developed a robust and scalable bioprocess that allows direct embryoid body (EB) formation in a fully controlled, stirred 2 L bioreactor following inoculation with a single cell suspension of mouse ES cells. Utilizing a pitched-blade-turbine, parameters for optimal cell expansion as well as efficient ES cell differentiation were established. Optimization of stirring conditions resulted in the generation of high-density suspension cultures containing 12.5 x 10(6) cells/mL after 9 days of differentiation. Approximately 30%-40% of the EBs formed in this process vigorously contracted, indicating robust cardiomyogenic induction. An ES cell clone carrying a recombinant DNA molecule comprised of the cardiomyocyte-restricted alpha myosin heavy chain (alphaMHC) promoter and a neomycin resistance gene was used to establish the utility of this bioprocess to efficiently generate ES-derived cardiomyocytes. The genetically engineered ES cells were cultured directly in the stirred bioreactor for 9 days, followed by antibiotic treatment for another 9 days. The protocol resulted in the generation of essentially pure cardiomyocyte cultures, with a total yield of 1.28 x 10(9) cells in a single 2 L bioreactor run. This study thus provides an important step towards the large-scale generation of ES-derived cells for therapeutic and industrial applications.

“…Cell death can result from numerous insults present in the bioreactors including mechanical agitation, nutritional depletion, waste byproduct accumulation, hypoxia, and viral insult (Franek, 1995;Goswami et al, 1999;Kunas and Papoutsakis, 1990;Mastrangelo et al, 2000a,b;Mercille and Massie, 1994;Shimizu et al, 1995;Simpson et al, 1997;Zanghi et al, 1999;Zhang et al, 1992). Cell death occurs in two general forms: necrosis and apoptosis.…”

Section: Introductionmentioning

confidence: 97%

Inhibiting apoptosis in mammalian cell culture using the caspase inhibitor XIAP and deletion mutants

Sauerwald

Betenbaugh

Oyler

2002

Lower yields and poorer quality of biopharmaceutical products result from cell death in bioreactors. Such cell death may occur from necrosis but is more commonly associated with apoptosis. During the process of programmed cell death or apoptosis, caspases become activated and cause a cascade of events that eventually destroy the cell. XIAP is the most potent caspase inhibitor encoded in the mammalian genome. The effectiveness of XIAP and its deletion mutants was examined in two cell lines commonly utilized in commercial bioreactors: Chinese hamster ovary (CHO) and 293 human embryonic kidney (293 HEK) cells. CHO cells undergo apoptosis as a result of various insults, including Sindbis virus infection and serum deprivation. In this study, we demonstrate that 293 HEK cells undergo apoptosis during Sindbis virus infection and exposure to the toxins, etoposide and cisplatin. Two deletion mutants of XIAP were created; one containing three tandem baculovirus iap repeat (BIR) domains and the other containing only the C-terminal RING domain, lacking the BIRs. Viability studies were performed for cells expressing each mutant and the wild-type protein on transiently transfected cells, as stable pools, or as stable clonal cell populations after induction of apoptosis by serum deprivation, Sindbis virus infection, etoposide, and cisplatin treatment. Expression of the wild-type XIAP inhibited apoptosis significantly; however, the XIAP mutant containing the three BIRs provided equivalent or improved levels of apoptosis inhibition in all cases. Expression of the RING domain offered no protection and was pro-apoptotic in transient expression experiments. With the aid of an N-terminal YFP fusion to each protein, distribution within the cell was visualized, and the wild-type and mutants showed differing intracellular accumulation patterns. While the wild-type XIAP protein accumulated primarily in aggregates in the cytosol, the RING mutant was enriched in the nucleus. In contrast, the deletion mutant containing the three BIRs was distributed evenly throughout the cytosol. Thus, protein engineering of the XIAP protein can be used to alter the intracellular distribution pattern and improve the ability of this caspase inhibitor to protect against apoptosis for two mammalian cell lines.