June 5, 2019
Cell and gene therapies as well as wider industry desire for cost efficiency will shape bioprocessing tech innovation, say experts.
Biopharma interest in cell and gene therapies is increasing. Products like Kymriah, Luxturna and Yescarta are the tip of an R&D iceberg according to PhRMA, which says around 300 such treatments are in development.
The trend has been well received, with various groups suggesting it will yield treatments for untreatable conditions (see here, here and here, for examples). Investors have also welcomed the surge in R&D, citing the revenue potential of cell and gene therapies.
Technology innovation
But for cell and gene therapies to fulfill their potential industry needs to address some manufacturing challenges according to Clive Glover, director of strategy at Pall Biotech.
“Alternative therapy types such as cell and gene therapy which have different needs compared to recombinant protein and monoclonal antibody (mAb) production which has driven this field for the past 20 years.
“For example, viral vectors manufacturing is generally done in adherent format and requires transient transfection. Standard stirred tank reactors are not well suited to this particularly at large scale, so we seek to optimize the process and overcome scalability challenges,” Glover told us.
Vector capacity
Viral vectors are hollow viruses that can carry genetic material. Cell and gene therapy developers use them to insert genes into cells.
Making vectors is time consuming and costly. In addition, as the Alliance of Advanced Biomedical Engineering (AABM) pointed out, there are not enough production facilities to satisfy biopharma demand.
Tech limitations – particularly the fact stirred tank bioreactors (STR) are not suitable for the culturing of adherent cells – are also a constraint according to Glover, who says Pall’s R&D team has taken this need into account.
“High quality viral vector production is best done using transient transfection in adherent systems. Pall’s iCELLis fixed-bed bioreactor provides up to 500 m2 of surface area in a very small footprint.
“While it is difficult to translate adherent production to suspension production, 500 m2 is roughly equivalent to 1,500 L of suspension culture, almost the same as the largest single-use STR. When you combine this scalability with the quality of virus coming from these bioreactors, they provide a compelling method to scale up viral vector production.”
Future bioreactors
Joe Capone, global product manager at Pall, also believes the growing cell and gene therapy sector will be a major influence on bioreactor design.
“In ten years from now the continuing efforts in cell line and process development, process development will be further realized. Productivity will be maximized to drive down costs, which will help to drive further evolution for all biotech equipment towards continuous processing.”
But cell and gene therapies are not be the only influence. The separate needs of monoclonal antibody (MAb) developers will also drive development of new technology says Capone.