Bioreactor scale up and protein product quality characterization of piggyBac transposon derived CHO pools. (7th March 2017)

• Record Type: Journal Article
• Authors: Rajendra, Yashas; Balasubramanian, Sowmya; Peery, Robert B.; Swartling, James R.; McCracken, Neil A.; Norris, Dawn L.; Frye, Christopher C.; Barnard, Gavin C.
• Is Part Of: Biotechnology progress. Volume 33:Number 2(2017)
• Page Start: 534
• Page End: 540
• Publication Date: 2017-03-07
• Subjects: piggyBac -- transposon -- CHO pools -- antibody -- bioreactor; Biotechnology -- Periodicals; Food industry and trade -- Periodicals; Bioengineering -- Periodicals; 660.6
• DOI: 10.1002/btpr.2447
• Languages: English
• ISSNs: 8756-7938

Abstract

Abstract : Chinese hamster ovary (CHO) cells remain the most popular host for the production of biopharmaceutical drugs, particularly monoclonal antibodies (mAbs), bispecific antibodies, and Fc‐fusion proteins. Creating and characterizing the stable CHO clonally‐derived cell lines (CDCLs) needed to manufacture these therapeutic proteins is a lengthy and laborious process. Therefore, CHO pools have increasingly been used to rapidly produce protein to support and enable preclinical drug development. We recently described the generation of CHO pools yielding mAb titers as high as 7.6 g/L in a 16 day bioprocess using piggyBac transposon‐mediated gene integration. In this study, we wanted to understand why the piggyBac pool titers were significantly higher (2–10 fold) than the control CHO pools. Higher titers were the result of a combination of increased average gene copy number, significantly higher messenger RNA levels and the homogeneity (i.e. less diverse population distribution) of the piggyBac pools, relative to the control pools. In order to validate the use of piggyBac pools to support preclinical drug development, we then performed an in‐depth product quality analysis of purified protein. The product quality of protein obtained from the piggyBac pools was very similar to the product quality profile of protein obtained from the control pools. Finally, we demonstrated the scalability of these pools from shake flasks to 36L bioreactors. Overall, these results suggest that gram quantities of therapeutic protein can be rapidly obtained from piggyBac CHO pools without significantly changing product quality attributes. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:534–540, 2017