No abstract

Perfusion operation mode remains the preferred platform for production of labile biopharmaceuticals (e.g., blood factors) and is also being increasingly adopted for production of stable products (e.g., monoclonal antibodies). Regardless of the product, process development typically aims at maximizing production capacity. In this work, we investigated the impact of perfusion cultivation conditions on process productivity for production of human factor VIII (FVIII). Recombinant CHO cells were cultivated in bioreactors coupled to inclined settlers and the effects of reducing the temperature to 31 C with or without valeric acid (VA) supplementation were evaluated. Increases in cell specific productivity (q p ) up to 2.4-fold (FVIII concentration) and up to 3.0-fold (FVIII biological activity) were obtained at 31 C with VA compared to the control at 37 C. Biological activity is the most important quality attribute for FVIII and was positively affected by mild hypothermia in combination with the chemical inducer. The low temperature conditions resulted in enhanced product transcript levels, suggesting that the higher q p is related to the increased mRNA levels. Furthermore, a high-producer subclone was evaluated under the perfusion conditions optimized for the parental clone (31 C with VA), yielding increases in q p of 6-fold and 15-fold compared to the parental clone cultivated under the same condition and at 37 C, respectively. The proposed perfusion strategy enables increased product formation without increasing production costs, being potentially applicable to perfusion production of other CHO-derived biopharmaceuticals. To the best of our knowledge, this is the first report showing the benefits of perfusion combining mild hypothermia with VA supplementation. K E Y W O R D SCHO perfusion cultivation, mild hypothermia, productivity, recombinant factor VIII, valeric acid

In the present work Computational Fluid Dynamics (CFD) was used to study the flow field and particle dynamics in an internal spin-filter (SF) bioreactor system. Evidence of a radial exchange flow through the filter mesh was detected, with a magnitude up to 130-fold higher than the perfusion flow, thus significantly contributing to radial drag. The exchange flow magnitude was significantly influenced by the filter rotation rate, but not by the perfusion flow, within the ranges evaluated. Previous reports had only given indirect evidences of this exchange flow phenomenon in spin-filters, but the current simulations were able to quantify and explain it. Flow pattern inside the spinfilter bioreactor resembled a typical Taylor-Couette flow, with vortices being formed in the annular gap and eventually penetrating the internal volume of the filter, thus being the probable reason for the significant exchange flow observed. The simulations also showed that cells become depleted in the vicinity of the mesh due to lateral particle migration. Cell concentration near the filter was approximately 50% of the bulk concentration, explaining why cell separation achieved in SFs is not solely due to size exclusion. The results presented indicate the power of CFD techniques to study and better understand spin-filter systems, aiming at the establishment of effective design, operation and scale-up criteria.

In the present work, the main fluid flow features inside a rotating cylindrical filtration (RCF) system used as external cell retention device for animal cell perfusion processes were investigated using particle image velocimetry (PIV). The motivation behind this work was to provide experimental fluid dynamic data for such turbulent flow using a high-permeability filter, given the lack of information about this system in the literature. The results shown herein gave evidence that, at the boundary between the filter mesh and the fluid, a slip velocity condition in the tangential direction does exist, which had not been reported in the literature so far. In the RCF system tested, this accounted for a fluid velocity 10% lower than that of the filter tip, which could be important for the cake formation kinetics during filtration. Evidence confirming the existence of Taylor vortices under conditions of turbulent flow and high permeability, typical of animal cell perfusion RCF systems, was obtained. Second-order turbulence statistics were successfully calculated. The radial behavior of the second-order turbulent moments revealed that turbulence in this system is highly anisotropic, which is relevant for performing numerical simulations of this system.