A baseline process for the production, recovery, and purification of bacterial influenza vaccine candidates.

The current commercial system for influenza vaccine production depends on the culture of virus in embryonated eggs--a strategy that is both costly and poorly scalable. Consequently, a sudden pandemic event with a demand for millions of vaccine doses in a short time could readily overwhelm the available world production capacity. In this communication, we present a process that uses Escherichia coli for scalable production of recombinant vaccine candidates against influenza. A monomeric and a dimeric fragment of hemagglutinin of the influenza A H1N1/2009 virus were successfully expressed in a BL21 (DE3) pLysS variety of C41 E. coli. We present results from batch processes where induction is made with isopropyl thiogalactoside and from fed-batch experiments where expression is induced using lactose/glucose pulses. Concentrations in the range of 1.188-0.605 g/L of recombinant protein were observed in 2-L stirred tank bioreactors. The genetic construct included an N-terminal histidine tag sequence that facilitated recovery, purification, and proper refolding of the vaccine candidate by affinity chromatography in columns loaded with Ni(+2) . The proteins produced by this strategy selectively and specifically recognizes antibodies from patients diagnosed as positive to influenza A H1N1/2009. Overall protein recovery yields between 30.0 and 34.7% were typically observed. Based on these yields, a production of 4.6 × 10(3) doses L(-3) day(-1) is feasible.

A biopharmaceutical plant on a chip: continuous micro-devices for the production of monoclonal antibodies.

We report a proof-of-principle for the use of micro-devices as continuous bioreactors for the production of monoclonal antibodies. We culture CHO cells on the surface of PMMA "zigzag" channels textured with semi-spherical cavities coated with fibronectin, observing steady-state productivities 100 times higher than those observed in full scale systems.