High density cell culture systems offer the advantage of production of
bio-pharmaceuticals in compact bioreactors with high volumetric produ
ction rates; however, these systems are difficult to design and operat
e. First of all, the cells have to be retained in the bioreactor by ph
ysical means during perfusion. The design of the cell retention is the
key to performance of high density cell culture systems. Oxygenation
and media design are also important for maximizing the cell number. In
high density perfusion reactors, variable cell density, and hence the
metabolic demand, require constant adjustment of perfusion rates. The
use of cell specific perfusion rate (CSPR) control provides a constan
t environment to the cells resulting in consistent production. On-line
measurement of cell density and metabolic activities can be used for
the estimation of cell densities and the control of CSPR. Issues relat
ed to mass transfer and mixing become more important at high cell dens
ities. Due to the difference in mass transfer coefficients for oxygen
and CO2, a significant accumulation of dissolved COP is experienced wi
th silicone tubing aeration. Also, mixing is observed to decrease at h
igh densities. Base addition, if not properly done, could result in lo
calized cell lysis and poor culture performance. Non-uniform mixing in
reactors promotes the heterogeneity of the culture. Cell aggregation
results in segregation of the cells within different mixing zones. Thi
s paper discusses these issues and makes recommendations for further d
evelopment of high density cell culture bioreactors.