Gas transfer characteristics of a novel membrane bioreactor.

Abstract:

:We show the design features of a membrane bioreactor based on pulsatile flow across dimpled membranes. Results show an enhanced mass transfer of air of at least five-fold magnitude as compared with flat membranes. An increased working volume form 20 mL to 120 mL reduced the k(L)A at a given Reynolds number because of axial mixing of fluid from the deoxygenated end chamber. The bioreactor was used to supply air to a hybridoma mammalian cell line, and the calculated oxygen uptake showed that high-density cultures could be maintained in a 20 mL, single-dimpled cultures could be maintained in a 20 mL, single-dimpled membrane system. Indirect aeration of a 2 L continuous stirred tank reactor, by a double-membrane system, showed that air could be supplied to mammalian cells at cell densities of approximately 4 x 10(6) /mL.

journal_name

Biotechnol Bioeng

authors

Beeton S,Millward HR,Bellhouse BJ,Nicholson AM,Jenkins N,Knowles CJ

doi

10.1002/bit.260381016

subject

Has Abstract

pub_date

1991-12-05 00:00:00

pages

1233-8

issue

10

eissn

0006-3592

issn

1097-0290

journal_volume

38

pub_type

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