F. Unterluggauer et al., STABLE, CONTINUOUS LARGE-SCALE PRODUCTION OF HUMAN MONOCLONAL HIV-1 ANTIBODY USING A COMPUTER-CONTROLLED PILOT-PLANT, BioTechniques, 16(1), 1994, pp. 140
A completely automated pilot plant used for fermentation has been empl
oyed with direct digital control (DDC) technology for monitoring and r
egulating growth of human cells. A human hybridoma cell line (3D6) pro
ducing anti-human immunodeficiency virus (HIV)-1 antibodies was used a
s a model for large-scale production (300-liter airlift fermentor) in
continuous culture. Parameters controlled were pH, dissolved oxygen, t
emperature and the flow rate of four gases used in the process. A cont
rol strategy was implemented to achieve constant fluid velocity and mi
xing by maintaining the rate of gas flow at a constant level. Another
advantage of this approach was that the total gas flow required for op
timal fluid circulation was reduced from 1 volume gas/volume fermenter
/hour (vvh) to 0.3 vvh. Use of a low flow rate eliminated the serious
problems of foaming, which contributed significantly to cell destructi
on, shorter filter-life and other considerations. Dilution rate was op
timized at laboratory scale for maximum productivity, which results in
relatively low viability. At a dilution rate of 0.0076 h(-1), a total
cell density of 6-7 x 10(5) cells/ml with a viability of approximatel
y 75% was maintained during long-term continuous cultivation. growth c
onditions resulted in a product titer stabilized in the range of 35 mu
g IgG/ml. Batchwise purification was achieved with a recovery of more
than 50% and a final purification of active monoclonal antibody repre
senting about 99% product. Results from isoelectric focusing and Weste
rn blotting demonstrated batch-to-batch consistency of the purified hu
man monoclonal antibody to HIV-1 during the continuous growth process.
This approach using DDC has broad applicability for the production of
high-quality biologics for use in medicine, agriculture and other dis
ciplines.