Production of immunoglobulin A in different reactor configurations.

A murine hybridoma line (Zac3), secreting an IgA monoclonal antibody, was cultivated in different systems: a BALB/c mouse, a T-flask, a stirred-tank bioreactor and a hollow fiber reactor. These systems were characterized in terms of cell metabolism and performances for IgA production. Cultures in T-flask and batch bioreactor were found to be glutamine-limited. Ammonia and lactate were produced in significant amounts. IgA productivity was found to be constant and growth associated. Final IgA concentration was similar in both systems. In fed-batch cultures, supplemented with glutamine and glucose, maximum viable cell concentration was increased by 60% and final IgA concentration by 155%. The hollow fiber reactor was able to produce very large amounts of IgA at very high concentrations, similar to the value found in ascites fluid. The productivity ofZac3 is similar to the values reported for IgG-producing cell lines.

Transcytosis of the polymeric Ig receptor requires phosphorylation of serine 664 in the absence but not the presence of dimeric IgA.

MDCK cells expressing the polymeric immunoglobulin (poly-Ig) receptor, cocultured with IgA-producing hybridoma cells, transported dimeric IgA (dIgA) from the basolateral into the lumenal compartment, where it was recovered as secretory component-dIgA complexes. The tail of the receptor was phosphorylated on serines 664 and 726. Each serine was mutated to alanine. Appearance of A726 receptor at the basolateral surface was reduced approximately 5-fold. This was accompanied by a approximately 5-fold reduction in dIgA transcytosis. Basolateral delivery of receptor was not affected by mutation A664, and in the absence of dIgA, the receptor accumulated in recycling basolateral endosomes. In coculture, however, dIgA transcytosis by A664 receptor was normal. Thus, entry of receptor into the transcytotic pathway requires Ser-664 phosphorylation only in the absence of dIgA.