Monoclonal IgA was produced under serum free conditions by a murine hy
bridoma cell line (ZAC3) in a hollow fibre, a continuous stirred tank
and a fluidized bed reactor. Differences in the antibody adsorption to
DEAE chromatography matrices, an essential step in downstream process
ing, were related to the production systems. Chromatography on hydroxy
apatite was used to separate monomeric, dimeric and polymeric IgA. Thi
s method was successfully applied to IgA produced by all three reactor
configurations. The binding of dimeric and polymeric IgA to antigen w
as tested by ELISA. Using 2-dimensional SDS-PAGE analysis, dimeric IgA
from the three sources was shown to be identical with respect to isoe
lectric points of alpha, kappa and J-chain but showed marked differenc
es in purity. Finally the efficiency of the three bioprocesses was ass
essed by comparing the product yields after purification. This include
d the reactor specific production rates, media and time requirements a
nd time consumption for the production of 1 g purified dimeric IgA.