Departament d'Enginyeria Química, Escola d'Enginyeria, Universitat Autònoma de Barcelona, 08193 Bellaterra (Cerdanyola del Vallès), Barcelona, Spain.
J Biotechnol. 2012 Jan;157(1):214-22. doi: 10.1016/j.jbiotec.2011.11.007. Epub 2011 Nov 20.
The culture of HEK-293S cells in a stirred tank bioreactor for adenoviral vectors production for gene therapy is studied. Process monitoring using oxygen uptake rate (OUR) was performed. The OUR was determined on-line by the dynamic method, providing good information of the process evolution. OUR enabled cell activity monitoring, facilitating as well the determination of the feeding rate in perfusion cultures and when to infect the culture. Batch cultures were used to validate the monitoring methodology. A cell density of 10×10(5)cell/mL was infected, producing 1.3×10(9) infectious viral particles/mL (IVP/mL). To increase cell density values maintaining cell specific productivity, perfusion cultures, based on tangential flow filtration, were studied. In this case, OUR measurements were used to optimize the dynamic culture medium feeding strategy, addressed to avoid any potential nutrient limitation. Furthermore, the infection protocol was defined in order to optimize the use of the viral inoculum, minimizing the uncontrolled release of particles through the filter unit mesh. All these developments enabled an infection at 78×10(5)cell/mL with the consequent production of 44×10(9)IVP/mL, representing a cell specific productivity 4.3 times higher than for the batch culture.
研究了在搅拌罐生物反应器中培养 HEK-293S 细胞以生产用于基因治疗的腺病毒载体的过程。使用耗氧速率 (OUR) 进行了过程监测。OUR 通过动态方法在线确定,提供了过程演变的良好信息。OUR 能够监测细胞活性,还便于确定灌注培养中的进料率以及何时感染培养物。分批培养用于验证监测方法。以 10×10(5)个细胞/mL 的细胞密度感染,产生 1.3×10(9)个感染性病毒颗粒/mL(IVP/mL)。为了提高细胞密度值,同时保持细胞特异性产率,研究了基于切向流过滤的灌注培养。在这种情况下,OUR 测量用于优化动态培养基进料策略,以避免任何潜在的营养限制。此外,还定义了感染方案,以优化病毒接种物的使用,最大程度地减少通过过滤单元网格的颗粒失控释放。所有这些开发都能够以 78×10(5)个细胞/mL 的感染,从而产生 44×10(9)个 IVP/mL,比分批培养的细胞特异性产率高 4.3 倍。