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利用计算流体动力学(CFD)模型来理解搅拌悬浮生物反应器中鼠胚胎干细胞聚集体大小和多能性分布。

Using computational fluid dynamics (CFD) modeling to understand murine embryonic stem cell aggregate size and pluripotency distributions in stirred suspension bioreactors.

机构信息

Pharmaceutical Production Research Facility, Schulich School of Engineering, University of Calgary, 2500 University Dr. NW, Calgary, AB, T2N 1N4, Canada; Biomedical Engineering Graduate Program, University of Calgary, 2500 University Dr. NW, Calgary, AB, T2N 1N4, Canada.

Pharmaceutical Production Research Facility, Schulich School of Engineering, University of Calgary, 2500 University Dr. NW, Calgary, AB, T2N 1N4, Canada; Department of Chemical and Petroleum Engineering, Schulich School of Engineering, University of Calgary, 2500 University Dr. NW, Calgary, AB, T2N 1N4, Canada.

出版信息

J Biotechnol. 2019 Oct 10;304:16-27. doi: 10.1016/j.jbiotec.2019.08.002. Epub 2019 Aug 5.

Abstract

Computational fluid dynamics (CFD) modeling can be applied to understand hydrodynamics in stirred suspension bioreactors, which can in turn affect cell viability, proliferation, pluripotency and differentiation. In this study, we developed a CFD model to determine the effects of average shear rates and turbulent eddies on the formation and growth of murine embryonic stem cell aggregates. We found a correlation between average eddy size and aggregate size, which depended on bioreactor agitation rates. By relating these computational and biological variables, CFD modeling can predict optimal agitation rates to grow embryonic stem cell aggregates in stirred suspension bioreactors. To examine the effect of hydrodynamics on pluripotency, mESCs cultured in bioreactors under various agitation rates were tested for SSEA-1, Sox-2, and Nanog expression. Cells maintained a minimum of 95% positive expression with no change in the intensity distribution pattern between the different bioreactor conditions. This indicates that the average level of pluripotency marker expression is independent of changes in the hydrodynamic profile and resulting aggregate size distribution. The findings here can be further extended to other cell types that grow as aggregates in stirred suspension bioreactors and offer important insights necessary to realize cell therapies.

摘要

计算流体动力学 (CFD) 建模可用于理解搅拌悬浮生物反应器中的流体动力学,这反过来又会影响细胞活力、增殖、多能性和分化。在这项研究中,我们开发了一种 CFD 模型来确定平均剪切率和湍流涡对鼠胚胎干细胞聚集体形成和生长的影响。我们发现平均涡尺寸与聚集体尺寸之间存在相关性,这取决于生物反应器的搅拌速度。通过将这些计算和生物学变量联系起来,CFD 建模可以预测在搅拌悬浮生物反应器中生长胚胎干细胞聚集体的最佳搅拌速度。为了研究流体动力学对多能性的影响,在不同搅拌速度下在生物反应器中培养的 mESCs 被检测到 SSEA-1、Sox-2 和 Nanog 的表达。细胞保持至少 95%的阳性表达,不同生物反应器条件之间的强度分布模式没有变化。这表明多能性标志物表达的平均水平与流体动力学特征的变化和由此产生的聚集体尺寸分布无关。这里的发现可以进一步扩展到其他以搅拌悬浮生物反应器中的聚集体形式生长的细胞类型,并为实现细胞治疗提供必要的重要见解。

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