A method for large-scale production of rotavirus vaccine using bioreactor
A bioreactor and rotavirus technology, applied to biochemical equipment and methods, viruses, microorganisms, etc., can solve the problems of low virus virulence titer, low rotavirus adsorption and infection, and improve production and quality Effect
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Embodiment 1
[0041] Embodiment 1: the preparation of rotavirus liquid
[0042] 1) Recovery and passage of Vero cells: After the cryopreservation tube containing the working seeds of Vero cells (the cells are from ATCC, the working seeds of the cells are self-made) is taken out from the liquid nitrogen, it is quickly put into a 40°C water bath to thaw, and then placed in the Take out the cell suspension in the ultra-clean bench, add it to the cell culture bottle, add the cell growth solution, and put it into the CO2 incubator for cultivation; after the cells grow into a single layer, digest the adherent cells and make a uniform cell suspension solution, according to the seeding ratio of 1:4, inoculated in the cell bottle, added the cell production solution, put it into the CO2 incubator to continue culturing, after two passages, inoculated the cells in the 10-layer cell factory, and After adding cell growth medium, culture;
[0043] 2) Cell collection and inoculation bioreactor: When the c...
Embodiment 2
[0050] 75L bioreactor cultivates the method for rotavirus vaccine, and preparation method is shown in embodiment 1, and wherein step 4) described bioreactor enters liquid, and the perfusion velocity of changing liquid also has effect to bioreactor production rotavirus Certain effects are shown in Table 1.
[0051] Table 1:
[0052] serial number Bioreactor feed Perfusion velocity during fluid change (WV / D) Titer (lgCCID50 / ml) Antigen content (ug / ml) 1 M199 culture medium with 0.5ug / ml trypsin 8 7.5 2.3 2 M199 culture medium with 0.5ug / ml trypsin 6 7.3 2.2 3 M199 culture medium with 0.5ug / ml trypsin 5 7.0 2.0 4 M199 culture medium with 0.5ug / ml trypsin 9 6.7 1.5 5 M199 medium with 0.2% bovine serum 8 3.5 0.5
[0053] Conclusion: As shown in Table 1, compared with Group 1 and Group 5, Group 5 is only the cell growth solution in which the serum concentration in the culture solution has been reduced to 0.2% as the ...
Embodiment 3
[0055] 75L bioreactor cultivates the method for rotavirus vaccine, and preparation method is the same as shown in embodiment 1, wherein step 5) described virus seed is activated and bioreactor controls the condition of the bioreactor when cell infection 24 hours after liquid change As shown in table 2
[0056] Table 2:
[0057]
[0058] Conclusion: As shown in Table 2, the virus titer of the rotavirus pooling solution harvested by groups 1-3 reaches 7.0lgCCID 50 / ml or more, the antigen content reaches more than 2.0ug / ml, which meets the requirements of large-scale production, wherein the titer and antigen content of the rotavirus pooled liquid of group 1 (i.e. embodiment 1) are optimal. And group 4, the harvest liquid of group 5 harvest, the virus titer of harvest liquid is lower, and antigen content is also lower, therefore, the control condition of the bioreactor described in step 5) is: temperature 35.0~36.0 ℃, pH The value is 7.2-7.5, the dissolved oxygen is 15%-35%,...
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