Tag: <span>single-use bioreactor</span>

Stirred tank single-use bioreactors (SUBs) have been widely adopted for production of biopharmaceuticals such as monoclonal antibodies in mammalian cell culture. However, they are seldom used for commercial production of biologics with microbial fermentation. SUBs offer time-saving advantages because they do not require significant downtime for cleaning and sterilization, so finding a SUB that can perform well with high cell density microbial fermentation processes has the potential to increase the number of production runs. Therefore, for this study, a His-tagged protease inhibitor was chosen as a model protein to demonstrate that the Sartorius Biostat STRĀ® MO, a SUB recently developed for microbial fermentation, is suited for recombinant protein production by high cell density Escherichia coli fermentation processes.

At 50 L scale, the SUB achieved good process control and allowed an oxygen uptake rate (OUR) of up to 240 mmoles/L/h. The fermentation runs produced up to 5.8 g/L of the soluble recombinant protein and a dry cell weight of >60 g/L at the end of fermentation. Additionally, the SUB showed a similar fermentation profile when compared with data from parallel runs in 15 L sterilise-in-place (SIP) vessels using identical media and process parameters. This study indicates that with a minimum investment of capital resources, stirred tank SUBs could be used in pilot-scale manufacturing with high cell density microbial fermentations to potentially shorten the timelines and costs of advancing therapeutic proteins to clinic.

Manufacturing

A perfusion approach at N-1, where cells stay in the exponential growth phase throughout the entire culture duration, is becoming more common as a strategy for process intensification. This is because the higher cell densities it generates allows manufacturers to skip seed stages and reduce process transfer time through multiple bioreactor sizes, thus providing more cost-effective biologics production in smaller facilities. However, this N-1 perfusion approach requires optimization. In this article, we describe the development and proof-of-concept studies with single-use rocking motion perfusion bioreactors in which we have achieved a ten-fold increase in viable cell count in N-1 seed stage, compared to the fed-batch control process, in just 6ā€“8 days. We also mention in detail how we inoculated a 50 L bioreactor production run using this intensified seed train and show comparable growth kinetics and yield with a control process, also at 50 L scale. Using this intensification approach in the future will help our manufacturing facility, the Biopharma Division of Intas Pharmaceuticals Ltd., reach 4000 L production-scale volumes with fewer process transfer steps, and without changing the feeding strategy or production bioreactors of our biologicsā€™ portfolio.

Manufacturing

Process characterization using qualified scale-down models (SDM) offers time and resource-saving advantages to companies developing biotherapeutics. Current approaches with glass benchtop bioreactors as SDMs have demonstrated the ability to predict process performance and product quality, but are throughput- limited by infrastructure that requires significant operational input, as well as large volumes of media and reagents. In this article, the Sartorius Stedim Biotech ambrĀ®250 high-throughput, single-use mini bioreactor system will be discussed for its suitability as an SDM for process characterization.

Biologics Production

In the past 20 years, mammalian cell lines have been utilized to produce many viral veterinary vaccines. Cell lines such as baby hamster kidney (BHK)-21, Vero, and Madin Darby canine kidney (MDCK) are widely used because they help facilitate shorter manufacturing lead times and tighter process controls. As compared to other biotech products, viral vaccine manufacturing processes present some specific constraints linked to the cell substrates used. With the global veterinary vaccine market value predicted to be almost $7 billion per year by 2021[2], to remain competitively priced as well as profitable, bioprocess scientists are under pressure to develop methods for faster and more cost-efficient cell culture production. This has led to a shift from the use of expensive, two-dimensional T-flask and roller bottles to single-use, stirred tank bioreactors with microcarriers, or the adaptation of attachment-dependent cell lines such as BHK-21 for suspension culture. This requires time-consuming optimization and scale-up development experiments, which are real drawbacks. However, utilizing automated, single-use mini bioreactors as a scale-down model can enable more efficient use of time and optimization of media, feed, and culture conditions to de-risk upstream process development. In this article, single-use, mini bioreactors are evaluated to determine if they are geometrically comparable to benchtop bioreactors (both glass and single-use vessels) and pilot-scale, single-use bioreactors for effectively modelling mammalian cell culture at 2 L and 50 L scale…

Biologics Production