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搅拌系统中源自球体的小细胞外囊泡生产的可扩展性。

Scalability of spheroid-derived small extracellular vesicles production in stirred systems.

作者信息

Dauphin Thibaud, de Beaurepaire Laurence, Salama Apolline, Pruvost Quentin, Claire Clémentine, Haurogné Karine, Sourice Sophie, Dupont Aurélien, Bach Jean-Marie, Hervé Julie, Olmos Eric, Bosch Steffi, Lieubeau Blandine, Mosser Mathilde

机构信息

Oniris VetAgroBio, INRAE, IECM, Nantes, France.

Oniris VetAgroBio, B-FHIT, Nantes, France.

出版信息

Front Bioeng Biotechnol. 2025 Apr 29;13:1516482. doi: 10.3389/fbioe.2025.1516482. eCollection 2025.

Abstract

INTRODUCTION

Small extracellular vesicle (sEV)-based therapies have gained widespread interest, but challenges persist to ensure standardization and high-scale production. Implementing upstream processes in a chemically defined media in stirred-tank bioreactors (STBr) is mandatory to closely control the cell environment, and to scale-up production, but it remains a significant challenge for anchorage-dependent cells.

METHODS

We used a human β cell line, grown as monolayer or in suspension as spheroid in stirred systems. We assessed the consequences of culturing these cells in 3D with, or without fetal bovine serum in a chemically defined medium, for cell growth, viability and metabolism. We next explored how different scale-up strategies might influence cell and spheroid formation in spinner flask, with the aim to transfer the process in instrumented Ambr®250 STBr. Lastly, we analyzed and characterized sEV production in monolayer, spinner flask and STBr.

RESULTS AND DISCUSSION

Generation of spheroids in a chemically defined medium allowed the culture of highly viable cells in suspension in stirred systems. Spheroid size depended on the system's volumetric power input (P/V), and maintaining this parameter constant during scale-up proved to be the optimal strategy for standardizing the process. However, transferring the spinner flask (SpF) process to the Ambr®250 STBr at constant P/V modified spheroid size, due to important geometric differences and impeller design. Compared to a monolayer reference process, sEV yield decreased two-fold in SpF, but increased two-fold in STBr. Additionally, a lower expression of the CD63 tetraspanin was observed in sEV produced in both stirred systems, suggesting a reduced release of exosomes compared to ectosomes. This study addresses the main issues encountered in spheroid culture scale-up in stirred systems, rather conducive for the production of ectosomes.

摘要

引言

基于小细胞外囊泡(sEV)的疗法已引起广泛关注,但要确保标准化和大规模生产仍面临挑战。在搅拌罐生物反应器(STBr)中使用化学成分明确的培养基实施上游工艺对于严格控制细胞环境和扩大生产规模至关重要,但对于贴壁依赖性细胞而言,这仍然是一项重大挑战。

方法

我们使用了一种人β细胞系,其在搅拌系统中以单层或作为球体悬浮生长。我们评估了在化学成分明确的培养基中,无论有无胎牛血清,将这些细胞进行三维培养对细胞生长、活力和代谢的影响。接下来,我们探讨了不同的扩大培养策略如何影响转瓶中的细胞和球体形成,目的是将该工艺转移到配备仪器的安瓿®250 STBr中。最后,我们分析并表征了单层、转瓶和STBr中的sEV产量。

结果与讨论

在化学成分明确的培养基中生成球体能够在搅拌系统中悬浮培养高活力细胞。球体大小取决于系统的体积功率输入(P/V),并且在扩大培养过程中保持该参数恒定被证明是使该工艺标准化的最佳策略。然而,由于重要的几何差异和叶轮设计,在恒定P/V下将转瓶(SpF)工艺转移到安瓿®250 STBr会改变球体大小。与单层参考工艺相比,SpF中的sEV产量降低了两倍,但在STBr中增加了两倍。此外,在两个搅拌系统中产生的sEV中观察到CD63四跨膜蛋白的表达较低,这表明与外泌体相比,外小体的释放减少。本研究解决了搅拌系统中球体培养扩大规模时遇到的主要问题,相当有利于外小体的生产。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/0ba0/12069995/c1314a704835/fbioe-13-1516482-g001.jpg

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