Development of a scalable process for high-yield lentiviral vector production by transient transfection of HEK293 suspension cultures

被引:112
作者
Ansorge, Sven [1 ,2 ]
Lanthier, Stephane [1 ]
Transfiguracion, Julia [1 ]
Durocher, Yves [1 ]
Henry, Olivier [2 ]
Kamen, Amine [1 ]
机构
[1] Natl Res Council Canada, Biotechnol Res Inst, Montreal, PQ H4P 2R2, Canada
[2] Ecole Polytech, Montreal, PQ H3C 3A7, Canada
关键词
gene therapy; HEK293; lentiviral vectors; scalable production; suspension culture; LARGE-SCALE PRODUCTION; PACKAGING CELL-LINE; SERUM-FREE PRODUCTION; MODELING RETROVIRUS PRODUCTION; RECOMBINANT PROTEIN-PRODUCTION; OF-THE-ART; HIGH-TITER; GENE-THERAPY; IN-VIVO; SODIUM-BUTYRATE;
D O I
10.1002/jgm.1370
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
Background Lentiviral vectors (LV) offer several advantages over other gene delivery vectors. Their potential for the integration and long-term expression of therapeutic genes renders them an interesting tool for gene and cell therapy interventions. However, large-scale LV production remains an important challenge for the translation of LV-based therapeutic strategies to the clinic. The development of robust processes for mass production of LV is needed. Methods A suspension-grown HEK293 cell line was exploited for the production of green fluorescent protein-expressing LV by transient polyethylenimine (PEI)-based transfection with LV-encoding plasmid constructs. Using third-generation packaging plasmids (Gag/Pol, Rev), a vesicular stomatitis virus G envelope and a self-inactivating transfer vector, we employed strategies to increase volumetric and specific productivity. Functional LV titers were determined using a flow cytometry-based gene transfer assay. Results A combination of the most promising conditions (increase in cell density, medium selection, reduction of PEI-DNA complexes per cell addition, of sodium butyrate) resulted in significantly increased LV titers of more than 150-fold compared to non-optimized small-scale conditions, reaching infectious titers of approximately 10(8) transducing units/ml. These conditions are readily scalable and were validated in 3-liter scale perfusion cultures. Conclusions Our process produces LV in suspension cultures and is consequently easily scalable, industrially viable and generated more than 10(11) total functional LV particles in a single bioreactor run. This process will allow the production of LV by transient transfection in sufficiently large quantities for phase I clinical trials at the 10-20-liter bioreactor scale. Copyright (C) 2009 John Wiley & Sons, Ltd.
引用
收藏
页码:868 / 876
页数:9
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