首页> 外文期刊>Vaccine >Establishment of a mink enteritis vaccine production process in stirred-tank reactor and Wave Bioreactor microcarrier culture in 1-10 L scale
【24h】

Establishment of a mink enteritis vaccine production process in stirred-tank reactor and Wave Bioreactor microcarrier culture in 1-10 L scale

机译:在1-10 L规模的搅拌罐反应器和Wave Bioreactor微载体培养中建立水貂肠炎疫苗生产工艺

获取原文
获取原文并翻译 | 示例
           

摘要

A scale-up and process optimization scheme for the growth of adherent embryonic feline lung fibroblasts (E-FL) on microcarriers and the propagation of a mink enteritis virus (MEV) strain for the production of an inactivated vaccine is shown. Stirred-tank cultivations are compared with results obtained from Wave Bioreactors. Transfer from a roller bottle-based production process into large-scale microcarrier culture with starting concentrations of 2g/L Cytodex 1 microcarriers and 2.0 x 10(5)cells/mL was successful. A maximum cell yield of 1.2 x 10(6)cells/mL was obtained in stirred-tank microcarrier batch culture while cell numbers in the Wave Bioreactor could not be determined accurately due to the fast sedimentation of microcarriers under non-rocking conditions required for sampling. Detailed off-line analysis was carried out to understand the behaviour of the virus-host cell system in both cultivation systems. Metabolic profiles for glucose, lactate, glutamine, and ammonium showed slight differences for both systems. E-FL cell growth was on the same level in stirred-tank and Wave Bioreactor with a higher volumetric cell yield compared to roller bottles. Propagation of MEV, which can only replicate efficiently in mitotic cells, was characterized in the Wave Bioreactor using a multiple harvest strategy. Maximum virus titres of 10(6.6) to 10(6.8) TCID(50)/mL were obtained, which corresponds to an increase in virus yield by a factor of about 10 compared to cultivations in roller bottles. As a consequence, a single Wave Bioreactor cultivation of appropriate scale can replace hundreds of roller bottles. Thus, the Wave Bioreactor proved to be a suitable system for large-scale production of an inactivated MEV vaccine.
机译:显示了用于在微载体上生长粘附的胚胎猫科动物肺成纤维细胞(E-FL)以及用于生产灭活疫苗的水貂肠炎病毒(MEV)菌株繁殖的按比例放大和工艺优化方案。将搅拌罐培养与从Wave Bioreactors获得的结果进行比较。成功地从基于滚瓶的生产工艺转移到大规模微载体培养,起始浓度为2g / L Cytodex 1微载体和2.0 x 10(5)细胞/ mL。在搅拌罐式微载体分批培养中获得的最大细胞产量为1.2 x 10(6)个细胞/ mL,但由于微载体在采样所需的非摇摆条件下快速沉降,因此无法准确确定Wave Bioreactor中的细胞数。进行了详细的离线分析,以了解两种培养系统中病毒宿主细胞系统的行为。葡萄糖,乳酸,谷氨酰胺和铵的代谢曲线在两个系统中均显示出细微差别。与滚瓶相比,搅拌罐和Wave Bioreactor中E-FL细胞的生长处于相同水平,细胞体积的产量更高。在Wave生物反应器中,使用多重收获策略对只能在有丝分裂细胞中有效复制的MEV的繁殖进行了表征。获得的最大病毒滴度为10(6.6)至10(6.8)TCID(50)/ mL,与在滚瓶中培养相比,这相当于病毒产量增加了约10倍。结果,适当规模的单个Wave Bioreactor培养可以替代数百个滚瓶。因此,Wave生物反应器被证明是用于大规模生产灭活的MEV疫苗的合适系统。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号