Advanced Centre for Biochemical Engineering, Department of Biochemical Engineering, University College London, London, UK.
Cell Culture and Fermentation Sciences, Biopharmaceutical Development, AstraZeneca, Cambridge, UK.
Biotechnol Bioeng. 2024 Jun;121(6):1774-1788. doi: 10.1002/bit.28685. Epub 2024 Mar 3.
The biopharmaceutical industry is replacing fed-batch with perfusion processes to take advantage of reduced capital and operational costs due to the operation at high cell densities (HCD) and improved productivities. HCDs are achieved by cell retention and continuous medium exchange, which is often based on the cell-specific perfusion rate (CSPR). To obtain a cost-productive process the perfusion rate must be determined for each process individually. However, determining optimal operating conditions remain labor-intensive and time-consuming experiments, as investigations are performed in lab-scale perfusion bioreactors. Small-scale models such as microwell plates (MWPs) provide an option for screening multiple perfusion rates in parallel in a semi-perfusion mimic. This study investigated two perfusion rate strategies applied to the MWP platform operated in semi-perfusion. The CSPR-based perfusion rate strategy aimed to maintain multiple CSPR values throughout the cultivation and was compared to a cultivation with a perfusion rate of 1 RV d. The cellular performance was investigated with the dual aim (i) to achieve HCD, when inoculating at conventional and HCDs, and (ii) to maintain HCDs, when applying an additional manual cell bleed. With both perfusion rate strategies viable cell concentrations up to 50 × 10 cells mL were achieved and comparable results for key metabolites and antibody product titers were obtained. Furthermore, the combined application of cell bleed and CSPR-based medium exchange was successfully shown with similar results for growth, metabolites, and productivities, respectively, while reducing the medium consumption by up to 50% for HCD cultivations.
生物制药行业正在用灌流工艺取代分批培养,以利用高细胞密度(HCD)带来的降低资本和运营成本的优势,并提高生产效率。通过细胞截留和连续介质交换来实现 HCD,而这通常基于细胞特异性灌流率(CSPR)。为了获得具有成本效益的工艺,必须针对每个工艺单独确定灌流率。然而,确定最佳操作条件仍然是劳动密集型和耗时的实验,因为研究是在实验室规模的灌流生物反应器中进行的。微井板(MWP)等小尺寸模型为在半灌流模拟中并行筛选多个灌流率提供了一种选择。本研究考察了两种灌流率策略在半灌流模式下的 MWP 平台上的应用。基于 CSPR 的灌流率策略旨在在整个培养过程中维持多个 CSPR 值,并与灌流率为 1 RV d 的培养进行了比较。通过双重目的研究了细胞性能:(i)在常规和 HCD 接种时达到 HCD,以及(ii)在应用额外的手动细胞排空时维持 HCD。通过这两种灌流率策略,均可实现高达 50×10⁶细胞/mL 的活细胞浓度,并获得了关键代谢物和抗体产物滴度的可比结果。此外,通过细胞排空和基于 CSPR 的培养基交换的联合应用,分别成功地展示了相似的生长、代谢物和生产力结果,同时使 HCD 培养的培养基消耗减少了高达 50%。