Takamatsu H, Hamamoto K, Ishimaru K, Yokoyama S, Tokashiki M
Biotechnology Research Laboratories, Teijin Limited, Tokyo, Japan.
Appl Microbiol Biotechnol. 1996 May;45(4):454-7. doi: 10.1007/BF00578455.
A high-cell-density perfusion culture process, using a novel centrifuge, was developed. The centrifuge has spiral multiple settling zones to separate cells from culture medium. Because of the multiple zones, the separation area can be efficiently increased without enlarging the diameter of the centrifuge. The centrifuge used in this study had a separation capacity of 2600 ml culture medium min -1 at 100 g of the centrifugal force. A new cell separation and withdrawal method was also developed. The cells separated in the centrifuge can be withdrawn easily from the centrifuge with no cell clogging by feeding a liquid carrier such as a perfluorocarbon into the centrifuge and pushing the cells out with the liquid carrier. By this culture process, monoclonal antibodies were produced with mouse-human hybridoma X87X at a cell density of about 8 x 10(6) cells ml -1 for 25 days. This centrifuge culture shows promise as a large-scale perfusion culture process. (Himmelfarb et al. 1969; Feder and Tolbert 1983) usually have the problem of filter clogging, and perfusion culture processes with gravitational cell settling (Tokashiki and Arai 1989) are limited in scale-up because of low separation efficiency. Recently centrifugal separation of cells from culture medium has been used for perfusion culture processes (Hamamoto et al. 1989; Tokashiki et al. 1990; Apelman 1992; Jäger 1992). This process essentially has a high separation efficiency and can avoid further operational problems, such as filter clogging, by the type of filtration. To investigate the scale-up feasibility of the centrifuge culture system, we have developed a new type of centrifuge with four layers of spiral cell-settling zones to increase the separation area, and a novel cell separation and withdrawal method using a perfluorocarbon.
开发了一种使用新型离心机的高细胞密度灌注培养工艺。该离心机具有螺旋形的多个沉降区,用于从培养基中分离细胞。由于有多个区域,无需增大离心机直径就能有效增加分离面积。本研究中使用的离心机在100g离心力下的分离能力为每分钟2600ml培养基。还开发了一种新的细胞分离和取出方法。通过向离心机中加入全氟化碳等液体载体,并利用液体载体将细胞推出,可轻松地从离心机中取出在离心机中分离出的细胞,且不会出现细胞堵塞现象。通过这种培养工艺,用人鼠杂交瘤X87X以约8×10⁶个细胞/ml的细胞密度培养了25天来生产单克隆抗体。这种离心机培养作为一种大规模灌注培养工艺显示出了前景。(希默法布等人,1969年;费德和托尔伯特,1983年)通常存在过滤器堵塞的问题,而利用重力使细胞沉降的灌注培养工艺(户刈木和新井,1989年)由于分离效率低,在扩大规模方面受到限制。最近,从培养基中离心分离细胞已用于灌注培养工艺(滨本等人,1989年;户刈木等人,1990年;阿佩尔曼,1992年;耶格尔,1992年)。该工艺本质上具有较高的分离效率,并且通过过滤类型可以避免诸如过滤器堵塞等进一步的操作问题。为了研究离心机培养系统扩大规模的可行性,我们开发了一种新型离心机,其具有四层螺旋形细胞沉降区以增加分离面积,以及一种使用全氟化碳的新型细胞分离和取出方法。