Evaluating shear in perfusion rotary lobe pump using nanoparticle aggregates and computational fluid dynamics

被引:3
作者
Amer, Momen [1 ]
Vaca, Alex [2 ]
Bowden, Marshall [3 ]
机构
[1] Biogen, Cell Culture Dev, 5000 Davis Dr, Res Triangle Pk, NC 27709 USA
[2] Biogen, Gene Therapy Cell Culture, Cambridge, MA 02142 USA
[3] Biogen, Drug Subst Pilot Dev, 5000 Davis Dr, Res Triangle Pk, NC 27709 USA
关键词
Cell Culture; Perfusion; Rotary lobe pump; Computational fluid dynamics; Shear; HYDRODYNAMIC DAMAGE; CHO-CELLS; FLOW; CULTURES; STRESS;
D O I
10.1007/s00449-022-02757-1
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
Perfusion cell culture technology has gained a lot of interest in recent years in the biopharmaceutical industry. One common application is N-1 perfusion which is used to intensify fed batch production processes and increase facility output. Upon running our perfusion process for the first time at manufacturing scale, unexpected cell damage was observed. Reducing the recirculation pump speed resulted in improvements in cell viability which implied the impact of pump shear stress on cell viability. In this study, we used polymethyl methacrylate (PMMA) nanoparticles to determine the shear stress inside two different sized rotary lobe pumps used in N-1 perfusion. The results were used to validate a computational fluid dynamics (CFD) model to predict the maximum shear under different operating conditions of the pump. The CFD model identified the radial and mesh clearance zones as regions that experience the maximum shear stress inside the pump. The model was then used to evaluate the impact of different geometry modifications in the pump lobes, and it predicted a 17% reduction in the maximum shear stress by increasing the mesh and radial clearances by 0.08 mm and 0.13 mm, respectively. The study indicates that CFD can be a useful tool to predict shear stress inside rotary pumps. The results can be used to optimize the pump operating conditions or even customize the pump geometry to save time and cost of process scaling to manufacturing without compromising the preset operating conditions or critical scale-up parameters.
引用
收藏
页码:1477 / 1488
页数:12
相关论文
共 42 条
[1]   Using CFD simulations and statistical analysis to correlate oxygen mass transfer coefficient to both geometrical parameters and operating conditions in a stirred-tank bioreactor [J].
Amer, Momen ;
Feng, Yu ;
Ramsey, Joshua D. .
BIOTECHNOLOGY PROGRESS, 2019, 35 (03)
[2]  
[Anonymous], ANSYS Inc., 2024, ANSYS Software Documentation, ANSYS Inc., Canonsburg, PA, accessed Nov. 8
[3]  
[Anonymous], 2010, REL 11 0 ANSYS CFX S
[4]  
[Anonymous], 2002, ALFA LAVAL PUMP HDB
[5]  
Babnik S., 2020, BIOMEDICAL J SCI TEC, V3, P20732, DOI DOI 10.26717/BJSTR.2020.27.004494
[6]   Perfusion mammalian cell culture for recombinant protein manufacturing - A critical review [J].
Bielser, Jean-Marc ;
Wolf, Moritz ;
Souquet, Jonathan ;
Broly, Herve ;
Morbidelli, Massimo .
BIOTECHNOLOGY ADVANCES, 2018, 36 (04) :1328-1340
[7]   Hydrodynamic damage to animal cells [J].
Chisti, Y .
CRITICAL REVIEWS IN BIOTECHNOLOGY, 2001, 21 (02) :67-110
[8]   Application of CFD to Analyze the Hydrodynamic Behaviour of a Bioreactor with a Double Impeller [J].
Ebrahimi, Mohammadreza ;
Tamer, Melih ;
Villegas, Ricardo Martinez ;
Chiappetta, Andrew ;
Ein-Mozaffari, Farhad .
PROCESSES, 2019, 7 (10)
[9]   Prediction of Agglomerate Type during Scale-Up of a Batch Crystallization Using Computational Fluid Dynamics Models [J].
Falk, Richard F. ;
Marziano, Ivan ;
Kougoulos, Terry ;
Girard, Kevin P. .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2011, 15 (06) :1297-1304
[10]   Modelling of mass transfer in gas-liquid stirred tanks agitated by Rushton turbine and CD-6 impeller: A scale-up study [J].
Gimbun, J. ;
Rielly, C. D. ;
Nagy, Z. K. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (4A) :437-451