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首页> 外文期刊>Enzyme and Microbial Technology >Bioreactor operation for transgenic Nicotiana tabacum cell cultures and continuous production of recombinant human granu10cyte-macrophage co10ny-stimulating factor by perfusion culture
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Bioreactor operation for transgenic Nicotiana tabacum cell cultures and continuous production of recombinant human granu10cyte-macrophage co10ny-stimulating factor by perfusion culture

机译:转基因烟草细胞培养的生物反应器操作和通过灌流培养法连续生产重组人粒巨噬细胞共刺激因子

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The production of hGM-CSF was investigated in both a flask and a 5-1 bioreactor,using transgenic Nicotiana tabacum suspension cells.While the maximum cell density and secreted hGM-CSF in the flask were 15.4 g 1~(-1)and 6.5 mug 1~(-1),respectively,those in the bioreactor were 15.6 g 1~(-1)and 7.6 jxg I~(-1).No detectable growth inhibition,shorter production of hGM-CSF and reduced cell viability in the batch bioreactor were observed under the specific conditions used compared with the flask culture.To improve the productivity,a perfusion culture was carried out in the bioreactor,with three different perfusion rates(0.5,1.0 and 2.0 day~(-1)).In all cases,the hGM-CSF in the medium was significantly increased during the overall culture period(16 days),with maximum values 3.0-,9.4-and 6.0-fold higher than those obtained in the batch cultures,respectively,even though the intracellular hGM-CSF content was not significantly varied by the perfusion rate.In terms of the total amount of hGM-CSF secreted,205.5,1073.2 and 1246.3 fig accumulated in the perfusate within 16 days at the perfusion rates of 0.5,1.0 and 2.0 day~(-1),respectively.It was concluded that the beneficial effect of perfusion on the production of hGM-CSF originated from the reduced proteolytic degradation due to the 10wer protease activity caused by the perfusion.Additionally,the cell growth and physio10gy in the perfusion culture were somewhat negatively affected by the increased perfusion rate,although the dry cell density steadily increased,and as a result,19.4,22.4 and 22.9gl~(-1)of maximum cells were obtained with perfusion rates of 0.5,1.0 and 2.0day~(-1),respectively.This work highlighted the importance of proteolytic degradation in plant cell cultures for the production of secretory proteins and the feasibility of perfusion strategies for the continuous production of foreign proteins by the prevention of protein 10ss due to proteolytic enzymes.
机译:使用转基因烟草悬浮细胞在烧瓶和5-1生物反应器中研究了hGM-CSF的产生,而烧瓶中最大细胞密度和分泌的hGM-CSF分别为15.4 g 1〜(-1)和6.5马克杯1〜(-1)的生物反应器分别为15.6 g 1〜(-1)和7.6 jxg I〜(-1)。没有可检测到的生长抑制作用,hGM-CSF的产生更短且细胞活力降低。在特定条件下与烧瓶培养相比,观察到了间歇式生物反应器。为提高生产率,在生物反应器中进行了灌注培养,三种灌注速率分别为(0.5、1.0和2.0天〜(-1))。在所有情况下,培养基中的hGM-CSF在整个培养期间(16天)均显着增加,即使分别在细胞内,其最大值也分别比分批培养的高3.0-,9.4-和6.0-倍hGM-CSF含量随灌注速度变化不明显。灌注时间分别为0.5、1.0和2.0天〜(-1)时,灌注液中分别有205.5、1073.2和1246.3个无花果堆积。结论是灌注对hGM-CSF产生的有益作用灌注引起的蛋白水解降解降低是由于灌注引起的10wer蛋白酶活性降低。此外,灌注速率的提高对灌注培养中的细胞生长和生理特性产生了一定的负面影响,尽管干细胞密度稳定地增加了,结果分别以0.5、1.0和2.0day〜(-1)的灌注速率获得了最大细胞的19.4、22.4和22.9gl〜(-1)。这项工作突显了蛋白水解降解在植物细胞培养物中对生产的重要性。蛋白质的合成以及通过预防由于蛋白水解酶引起的蛋白质10ss来连续生产外源蛋白质的灌注策略的可行性。

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