Conceição M M, Tonso A, Freitas C B, Pereira C A
Laboratório de Imunologia Viral, Instituto Butantan, Av. Vital Brasil 1500, 05503-900 São Paulo, Brazil.
Vaccine. 2007 Nov 7;25(45):7785-95. doi: 10.1016/j.vaccine.2007.08.048. Epub 2007 Sep 14.
Viral antigens can be obtained from infected mammalian cells cultivated on microcarriers. We have worked out parameters for the production of bovine parainfluenza 3 (PI-3) virus by Mandin-Darby Bovine Kidney (MDBK) cells cultivated on Cytodex 1 microcarriers (MCs) in spinners flasks and bioreactor using fetal bovine serum (FBS) supplemented Eagle minimal essential medium (Eagle-MEM). Medium renewal during the cell culture was shown to be crucial for optimal MCs loading (>90% MCs with confluent cell monolayers) and cell growth (2.5 x 10(6)cells/mL and a micro(x) (h(-1)) 0.05). Since cell cultures performed with lower amount of MCs (1g/L), showed good performances in terms of cell loading, we designed batch experiments with a lower concentration of MCs in view of optimizing the cell growth and virus production. Studies of cell growth with lower concentrations of MCs (0.85 g/L) showed that an increase in the initial cell seeding (from 7 to 40 cells/MC) led to a different kinetic of initial cell growth but to comparable final cell concentrations ((8-10)x10(5)cells/mL at 120 h) and cell loading (210-270 cells/MC). Upon infection with PI-3 virus, cultures showed a decrease in cell growth and MC loading directly related to the multiplicity of infection (moi) used for virus infection. Infected cultures showed also a higher consumption of glucose and production of lactate. The PI-3 virus and PI-3 antigen production among the cultures was not significantly different and attained values ranging from, respectively, 7-9 log(10) TCID(50)/mL and 1.5-2.2 OD. The kinetics of PI-3 virus production showed a sharp increase during the first 24h and those of PI-3 antigen increased after 24h. The differential kinetics of PI-3 virus and PI-3 antigen can be explained by the virus sensitivity to temperature. In view of establishing a protocol of virus production and based on the previous experiments, MDBK cell cultures performed under medium perfusion in a bioreactor of 1.2L were infected and the PI-3 virus production in 12L attained 12 log(10) TCID(50). Other than establishing a protocol for PI-3 production in MDBK cell cultures on Cytodex 1, the experiments are proposed as a basis for approaching the development of a virus production protocol in mammalian cells cultivated on microcarriers in bioreactors.
病毒抗原可从在微载体上培养的受感染哺乳动物细胞中获得。我们已经确定了在转瓶和生物反应器中,使用补充有胎牛血清(FBS)的伊格尔最低必需培养基(伊格尔 - MEM),在Cytodex 1微载体(MCs)上培养的曼氏 - 达比牛肾(MDBK)细胞生产牛副流感3型(PI - 3)病毒的参数。细胞培养过程中的培养基更新对于实现最佳的MCs负载(>90%的MCs带有汇合的细胞单层)和细胞生长(2.5×10⁶个细胞/mL以及μ(h⁻¹)0.05)至关重要。由于使用较低量的MCs(1g/L)进行的细胞培养在细胞负载方面表现良好,我们设计了较低MCs浓度的批次实验,以优化细胞生长和病毒生产。对较低浓度MCs(0.85g/L)的细胞生长研究表明,初始细胞接种量的增加(从7个细胞/MC增加到40个细胞/MC)导致初始细胞生长动力学不同,但最终细胞浓度相当(120小时时为(8 - 10)×10⁵个细胞/mL)且细胞负载相当(210 - 270个细胞/MC)。用PI - 3病毒感染后,培养物显示细胞生长和MCs负载下降,这与用于病毒感染的感染复数(moi)直接相关。受感染的培养物还显示葡萄糖消耗增加和乳酸产生增加。各培养物中PI - 3病毒和PI - 3抗原的产量没有显著差异,分别达到7 - 9 log₁₀ TCID₅₀/mL和1.5 - 2.2 OD。PI - 3病毒生产的动力学在最初24小时内急剧增加,而PI - 3抗原的动力学在24小时后增加。PI - 3病毒和PI - 3抗原的不同动力学可以通过病毒对温度的敏感性来解释。鉴于建立病毒生产方案,并基于先前的实验,在1.2L生物反应器中进行培养基灌注培养的MDBK细胞培养物被感染,12L中的PI - 3病毒产量达到12 log₁₀ TCID₅₀。除了建立在Cytodex 1上的MDBK细胞培养物中PI - 3生产的方案外,这些实验被提议作为在生物反应器中微载体上培养的哺乳动物细胞中开发病毒生产方案的基础。