Dalm Marcella C F, Cuijten Suzanne M R, van Grunsven Wout M J, Tramper Johannes, Martens Dirk E
Department of Agrotechnology and Food Sciences, Food and Bioprocess Engineering Group, Wageningen University, Bomenweg 2, 6703 HD Wageningen, The Netherlands.
Biotechnol Bioeng. 2004 Dec 5;88(5):547-57. doi: 10.1002/bit.20287.
For the development of optimal perfusion processes the effect of the feed and bleed rate on cell growth in a perfusion bioreactor was studied. The viable-cell density, viability, growth, death, and lysis rate and cell-cycle distribution of a hybridoma cell line producing an IgG1 were studied over a range of specific feed and bleed rates. It was found that the feed and bleed rates applied in the different cultures could be divided into two regions based on the viable-cell density and cell-cycle distribution. The cultures in the first region, low feed rates (0.5 and 1.0 d(-1)) combined with low bleed rates (0.05 and 0.10 d(-1)), were nutrient-limited, as an increase in the feed rate resulted in an increase in the viable-cell density. The cultures in the second region, high feed and bleed rates, were nonnutrient-limited. In this region the viable-cell density decreased more or less linearly with an increase in the bleed rate and was independent of the feed rate. This suggests that the cells were limited by a cell-related factor. Comparison of Trypan-blue dye-exclusion measurements and lactate-dehydrogenase activity measurements revealed that cell lysis was not negligible in this bioreactor set-up. Therefore, lactate-dehydrogenase activity measurements were essential to measure the death rate accurately. The specific growth rate was nearly constant for all tested conditions. The viability increased with an increase of the bleed rate and was independent of the feed rate. Furthermore, the specific productivity of monoclonal antibody was constant under all tested conditions. For the optimal design of a perfusion process it should first be established whether viability is an important parameter. If not, a bleed rate as low as possible should be chosen. If low viabilities are to be avoided, the bleed rate chosen should be higher, with the value depending on the desired viability. Next, the feed rate should be set at such a rate that the cells are just in the nonnutrient-limited region.
为了开发最佳灌注工艺,研究了灌注生物反应器中进料和出料速率对细胞生长的影响。在一系列特定的进料和出料速率范围内,研究了产生IgG1的杂交瘤细胞系的活细胞密度、活力、生长、死亡、裂解速率以及细胞周期分布。结果发现,根据活细胞密度和细胞周期分布,不同培养物中应用的进料和出料速率可分为两个区域。第一个区域的培养物,低进料速率(0.5和1.0 d(-1))与低出料速率(0.05和0.10 d(-1))相结合,是营养限制型的,因为进料速率的增加导致活细胞密度增加。第二个区域的培养物,高进料和出料速率,是非营养限制型的。在这个区域,活细胞密度随着出料速率的增加或多或少呈线性下降,并且与进料速率无关。这表明细胞受到与细胞相关的因素限制。台盼蓝染料排除测量和乳酸脱氢酶活性测量的比较表明,在这种生物反应器设置中细胞裂解不可忽略。因此,乳酸脱氢酶活性测量对于准确测量死亡率至关重要。在所有测试条件下,比生长速率几乎恒定。活力随着出料速率的增加而增加,并且与进料速率无关。此外,单克隆抗体的比生产率在所有测试条件下都是恒定的。对于灌注工艺的优化设计,首先应确定活力是否是一个重要参数。如果不是,应选择尽可能低的出料速率。如果要避免低活力,则应选择较高的出料速率,其值取决于所需的活力。接下来,进料速率应设置为使细胞刚好处于非营养限制区域的速率。