Small-scale perfusion mimic cultures in the ambr250 HT bioreactor system

被引:0
|
作者
Rapala, Srikanth
Barton, Abiageal [1 ,3 ]
Harcum, Sarah W. [1 ,2 ]
机构
[1] Clemson Univ, Dept Chem & Biomol Engn, Clemson, SC 29634 USA
[2] Clemson Univ, Dept Bioengn, 301 Rhodes Res Ctr, Clemson, SC 29634 USA
[3] IGM Biosci Inc, Mountain View, CA 94043 USA
基金
美国国家科学基金会;
关键词
Chinese hamster ovary cells; Centrifugation; Gravity settling; DO stress; CHO-CELL CULTURE; ELEVATED PCO(2); DOWN MODEL; CARBON-DIOXIDE; PERFORMANCE; OSMOLALITY; HYBRIDOMA; PLATFORM; BATCH;
D O I
10.1016/j.bej.2024.109332
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Perfusion cell cultures generate higher viable cell densities (VCD) and volumetric productivity compared to fedbatch cultures. However, due to the limited availability of small-scale perfusion models, perfusion systems are seldom used to produce licensed biotherapeutics. This study evaluated two small-scale perfusion mimic protocols to bridge the research-to-production gap. Shake flasks and the ambr250 HT were used to compare centrifugation and in situ gravity settling protocols. The centrifugation protocol achieved a peak VCD >50 million cells/mL and is well-suited to media formulation and feeding strategy comparisons. The in situ gravity settling protocol achieved -20 million cells/mL and is well-suited to cell productivity and stability studies. The cell retention steps resulted in temporary DO and pH changes but did not affect the overall culture's health. Further, both protocols were able to recover from an imposed long-duration DO stress, although the centrifugation protocol cultures had higher cell specific oxygen consumption rates indicative of higher culture stress. Both protocols sustained the cultures for 39 days with stable cell specific productivities (-27 pg/cell & sdot;day). Overall, this study demonstrated the feasibility of two economic small-scale perfusion mimic protocols in a standard small-scale bioreactor system, which could be translated to other multi-unit small-scale bioreactor systems.
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页数:13
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