Modeling the Residence Time Distribution of Integrated Continuous Bioprocesses.

In response to the biopharmaceutical industry advancing from traditional batch operation to continuous operation, the Food and Drug Administration (FDA) has published a draft for continuous integrated biomanufacturing. This draft outlines the most important rules for establishing continuous integration. One of these rules is a thorough understanding of mass flows in the process.

Truly continuous low pH viral inactivation for biopharmaceutical process integration.

Continuous virus inactivation (VI) has received little attention in the efforts to realize fully continuous biomanufacturing in the future. Implementation of continuous VI must assure a specific minimum incubation time, typically 60 min. To guarantee the minimum incubation time, we implemented a packed bed continuous viral inactivation reactor (CVIR) with narrow residence time distribution (RTD) for low pH incubation.

A narrow residence time incubation reactor for continuous virus inactivation based on packed beds.

A narrow residence time distribution (RTD) is highly desirable for continuous processes where a strict incubation time must be ensured, such as continuous virus inactivation. A narrow RTD also results in faster startup and shut down phases and limits the broadening of potential disturbances in continuous processes. A packed bed reactor with non-porous inert beads was developed to achieve narrow RTDs.

Continuous Solvent/Detergent Virus Inactivation Using a Packed-Bed Reactor.

Continuous virus inactivation (VI) remains one of the missing pieces while the biopharma industry moves toward continuous manufacturing. The challenges of adapting VI to the continuous operation are two-fold: 1) achieving fluid homogeneity and 2) a narrow residence time distribution (RTD) for fluid incubation. To address these challenges, a dynamic active in-line mixer and a packed-bed continuous virus inactivation reactor (CVIR) are implemented, which act as a narrow RTD incubation chamber.

Continuous precipitation of IgG from CHO cell culture supernatant in a tubular reactor.

We successfully transferred a two-stage batch precipitation-based antibody capture step to continuous mode using continuous tubular reactors. The precipitation process solely employs a cheap mineral salt (CaCl2 ) and an organic solvent (ethanol) and could replace the costly protein A capture step in the purification of recombinant antibodies from cell culture supernatant. The time from startup untill attaining steady state conditions was reached in less than 15 minutes and both reactors were operated for several hours at steady state without manual intervention, delivering antibody at a constant yield and purity.

Economics of recombinant antibody production processes at various scales: Industry-standard compared to continuous precipitation.

Standard industry processes for recombinant antibody production employ protein A affinity chromatography in combination with other chromatography steps and ultra-/diafiltration. This study compares a generic antibody production process with a recently developed purification process based on a series of selective precipitation steps. The new process makes two of the usual three chromatographic steps obsolete and can be performed in a continuous fashion.