Jl. Moreira et al., INFLUENCE OF POWER INPUT AND AERATION METHOD ON MASS-TRANSFER IN A LABORATORY-ANIMAL CELL-CULTURE VESSEL, Journal of chemical technology and biotechnology, 62(2), 1995, pp. 118-131
Large-scale animal cell operation is costly both in terms of facilitie
s and consumables. Hence developmental studies with animal cells norma
lly start at laboratory scale, often using small stirred tanks. In ord
er to better optimise cell performance, it is necessary to know the ph
ysical conditions under which the cells are grown. In this study a lab
oratory-scale vessel (2 dm(3) working volume) with two large-bladed pa
ddle impellers was characterised hydrodynamically. Three different aer
ation methods (surface, sparging and membrane aeration) were investiga
ted and compared. Power input and oxygen transfer rates to culture med
ium were determined as a function of agitation and gas flow rates. Non
dimensional correlations were established for each case, which can be
useful for scale-up purposes. The results obtained indicate that power
input is quite dependent on the vessel accessories: for the same agit
ation rate, the maximum power is required for the membrane structure a
nd the minimum for surface aeration, with the addition of the sparger
leading to an intermediate situation. Predictions found in the literat
ure can be used for simple vessels, but may not be applicable when acc
essories are added to the vessel structure; in such cases, the use of
experimental relationships are required. Oxygen transfer rate was depe
ndent on the aeration method and working conditions (agitation and gas
flow rates), particularly for sparger aeration. Membrane aeration gav
e larger oxygen transfer but higher gas pressure and flow rates were r
equired. Surface aeration was the least effective method, nevertheless
requiring gas flow rates similar to those used for membrane aeration.
The aeration method of choice depends upon the culture and work speci
ficities: surface aeration is limited to small cell concentrations and
low oxygen consumption rates. For higher cell concentrations and oxyg
en consumption rates, both membrane and sparger aeration methods can b
e applied: the use of the sparger is limited to cells that are not aff
ected by the presence of bubbles or the addition of surfactants, where
as the membrane aeration basket should not be used when a hydrodynamic
ally controlled stirred tank is required.