Zhang Ye, Stobbe Per, Silvander Christian Orrego, Chotteau Véronique
School of Biotechnology, Dept. Industrial Biotechnology/Bioprocess Design, Cell Technology Group (CETEG), Royal Institute of Technology, KTH, SE-10691 Stockholm, Sweden.
PerfuseCell, Malmmosevej 19C, DK-2840 Holte, Denmark.
J Biotechnol. 2015 Nov 10;213:28-41. doi: 10.1016/j.jbiotec.2015.07.006. Epub 2015 Jul 23.
Recombinant Chinese Hamster Ovary (CHO) cells producing IgG monoclonal antibody were cultivated in a novel perfusion culture system CellTank, integrating the bioreactor and the cell retention function. In this system, the cells were harbored in a non-woven polyester matrix perfused by the culture medium and immersed in a reservoir. Although adapted to suspension, the CHO cells stayed entrapped in the matrix. The cell-free medium was efficiently circulated from the reservoir into- and through the matrix by a centrifugal pump placed at the bottom of the bioreactor resulting in highly homogenous concentrations of the nutrients and metabolites in the whole system as confirmed by measurements from different sampling locations. A real-time biomass sensor using the dielectric properties of living cells was used to measure the cell density. The performances of the CellTank were studied in three perfusion runs. A very high cell density measured as 200 pF/cm (where 1 pF/cm is equivalent to 1 × 10(6)viable cells/mL) was achieved at a perfusion rate of 10 reactor volumes per day (RV/day) in the first run. In the second run, the effect of cell growth arrest by hypothermia at temperatures lowered gradually from 37 °C to 29 °C was studied during 13 days at cell densities above 100 pF/cm. Finally a production run was performed at high cell densities, where a temperature shift to 31 °C was applied at cell density 100 pF/cm during a production period of 14 days in minimized feeding conditions. The IgG concentrations were comparable in the matrix and in the harvest line in all the runs, indicating no retention of the product of interest. The cell specific productivity was comparable or higher than in Erlenmeyer flask batch culture. During the production run, the final harvested IgG production was 35 times higher in the CellTank compared to a repeated batch culture in the same vessel volume during the same time period.
表达重组IgG单克隆抗体的中国仓鼠卵巢(CHO)细胞,在一种整合了生物反应器和细胞截留功能的新型灌注培养系统CellTank中进行培养。在该系统中,细胞被容纳在由培养基灌注并浸于储液池中的聚酯无纺布基质中。尽管CHO细胞已适应悬浮培养,但它们仍滞留在基质中。无细胞培养基通过置于生物反应器底部的离心泵,有效地从储液池循环进入并通过基质,不同采样点的测量结果证实,整个系统中营养物质和代谢产物的浓度高度均匀。使用基于活细胞介电特性的实时生物量传感器来测量细胞密度。在三次灌注运行中研究了CellTank的性能。在第一次运行中,以每天10个反应器体积(RV/天)的灌注速率,实现了非常高的细胞密度,测量值为200 pF/cm(其中1 pF/cm相当于1×10⁶活细胞/mL)。在第二次运行中,研究了在13天内,细胞密度高于100 pF/cm时,温度从37℃逐渐降至29℃对细胞生长停滞的影响。最后,在高细胞密度下进行了一次生产运行,在最小化补料条件下,在14天的生产期内,当细胞密度达到100 pF/cm时,将温度升至31℃。在所有运行中,基质和收获管线中的IgG浓度相当,表明目标产物没有截留。细胞比生产率与锥形瓶分批培养相当或更高。在生产运行期间,与相同容器体积在同一时间段内的重复分批培养相比,CellTank中最终收获的IgG产量高出35倍。