Justification of continuous packed-bed reactor for retroviral vector production from amphotropic Psi CRIP murine producer cell

Citation
Sh. Kang et al., Justification of continuous packed-bed reactor for retroviral vector production from amphotropic Psi CRIP murine producer cell, CYTOTECHNOL, 34(1-2), 2000, pp. 151-158
Citations number
27
Categorie Soggetti
Biotecnology & Applied Microbiology
Journal title
CYTOTECHNOLOGY
ISSN journal
09209069 → ACNP
Volume
34
Issue
1-2
Year of publication
2000
Pages
151 - 158
Database
ISI
SICI code
0920-9069(200010)34:1-2<151:JOCPRF>2.0.ZU;2-W
Abstract
To indentify a plausible large-scale production system for retroviral vecto r, three culture systems, i.e., batch culture with medium exchange, microca rrier culture, and packed-bed reactor culture were compared. In batch cultu res with medium exchange, high cell concentrations were maintained for abou t a month, and the harvested retroviral titer remained constant. In microca rrier cultures, although cell growth was rapid, the retroviral titer was un expectedly low, suggesting that the low titer was due either to serious dam age to the retroviral vector or to a reduction in the production rate of re troviral vector, caused by mechanical shear forces. Although the retroviral titer (maximum titer, 1.56 x 10(6)) in the packed-bed reactor was a little bit lower than that obtained in the batch culture with medium exchange (ma ximum titer, 1.91 x 10(6)), continuous production made it possible to incre ase the cumulative titer up to 16-fold of that from the batch culture with medium exchange. Moreover, as the packed-bed reactor system requires less l abor and shows excellent volumetric productivity in comparison to batch cul tures with medium exchanges, it will be an appropriate production system fo r retroviral vector in large quantities.