A novel scale-up strategy for cultivation of BHK-21 cells based on similar hydrodynamic environments in the bioreactors

被引:5
作者
Teng, Xiaonuo [1 ]
Li, Chao [1 ]
Yi, Xiaoping [1 ]
Zhuang, Yingping [1 ]
机构
[1] East China Univ Sci & Technol, State Key Lab Bioreactor Engn, Shanghai 200237, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
BHK-21; cells; Bioreactor; Computational fluid dynamics; Hydrodynamic characteristics; Scale-up; FLUID-DYNAMICS; RABIES VACCINE; MASS-TRANSFER; CELL;
D O I
10.1186/s40643-021-00393-3
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The scale-up of animal cell cultivation is important but remains complex and challenging. In the present study, we propose a novel scale-up strategy for baby hamster Syrian kidney-21 (BHK-21) cell cultivation based on similar hydrodynamic environments. The hydrodynamic characteristics of the different scale bioreactors were determined by computational fluid dynamics (CFD) and further correlated with the agitation speed. The optimal hydrodynamic environment for cell cultivation and vaccine production was determined from the cultivation experiments of BHK-21 cells in 5-L laboratory-scale bioreactors equipped with different impellers at various agitation speeds. BHK-21 cell cultivation was scaled up from 5-L to 42-, 350-, and 1000-L bioreactors by adjusting the agitation speed to make the hydrodynamic features similar to those in the 5-L bioreactor, especially for the shear rate in the impeller zone (gamma(imp)) and energy dissipation rate in the tank bulk zone (epsilon(tan)). The maximum cell density and cell aggregation rate in these scaled-up bioreactors were in the range of 4.6 x 10(6) similar to 4.8 x 10(6) cells/mL and 16 similar to 20%, which are comparable to or even better than those observed in the 5-L bioreactor (maximum cell density 4.8 x 10(6) cells/mL, cell aggregation rate 21%). The maximum virus titer of 10(8.0) LD50/mL achieved in the 1000-L bioreactor was close to 10(8.3) LD50/mL that obtained in the 5-L bioreactor. Hence, the scale-up strategy proposed in this study is feasible and can efficiently facilitate the scale-up processes of animal cell cultivation.
引用
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页数:13
相关论文
共 27 条
[1]   Using computational fluid dynamics (CFD) modeling to understand murine embryonic stem cell aggregate size and pluripotency distributions in stirred suspension bioreactors [J].
Borys, Breanna S. ;
Le, An ;
Roberts, Erin L. ;
Dang, Tiffany ;
Rohani, Leili ;
Hsu, Charlie Yu-Ming ;
Wyma, Alexander A. ;
Rancourt, Derrick E. ;
Gates, Ian D. ;
Kallos, Michael S. .
JOURNAL OF BIOTECHNOLOGY, 2019, 304 :16-27
[2]   Scale-up of embryonic stem cell aggregate stirred suspension bioreactor culture enabled by computational fluid dynamics modeling [J].
Borys, Breanna S. ;
Roberts, Erin L. ;
Le, An ;
Kallos, Michael S. .
BIOCHEMICAL ENGINEERING JOURNAL, 2018, 133 :157-167
[3]   Rabies Virus [J].
Brunker, Kirstyn ;
Mollentze, Nardus .
TRENDS IN MICROBIOLOGY, 2018, 26 (10) :886-887
[4]  
Cai Y., 2015, J APPL VIROL, V4, P4, DOI [10.21092/jav.v4i1.34, DOI 10.21092/JAV.V4I1.34]
[5]   Determination of the average shear rate in a stirred and aerated tank bioreactor [J].
Campesi, Alexandre ;
Cerri, Marcel O. ;
Hokka, Carlos O. ;
Badino, Alberto C. .
BIOPROCESS AND BIOSYSTEMS ENGINEERING, 2009, 32 (02) :241-248
[6]   Scale-up of aerated bioreactors: CFD validation and application to the enzyme production by Trichoderma reesei [J].
Cappello, Vincenzo ;
Plais, Cecile ;
Vial, Christophe ;
Augier, Frederic .
CHEMICAL ENGINEERING SCIENCE, 2021, 229
[7]   Bioreactor scale-up and oxygen transfer rate in microbial processes: An overview [J].
Garcia-Ochoa, Felix ;
Gomez, Emilio .
BIOTECHNOLOGY ADVANCES, 2009, 27 (02) :153-176
[8]   Scale-up agitation criteria for Trichoderma reesei fermentation [J].
Hardy, Nicolas ;
Augier, Frederic ;
Nienow, Alvin W. ;
Beal, Catherine ;
Ben Chaabane, Fadhel .
CHEMICAL ENGINEERING SCIENCE, 2017, 172 :158-168
[9]   From industrial fermentor to CFD-guided downscaling: what have we learned? [J].
Haringa, Cees ;
Mudde, Robert F. ;
Noorman, Henk J. .
BIOCHEMICAL ENGINEERING JOURNAL, 2018, 140 :57-71
[10]   A systematic mass-transfer modeling approach for mammalian cell culture bioreactor scale-up [J].
He, Chuan ;
Ye, Pei ;
Wang, Haibin ;
Liu, Xiao ;
Li, Feng .
BIOCHEMICAL ENGINEERING JOURNAL, 2019, 141 :173-181