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垂直轮系统中无血清条件下基于微载体的人骨髓间充质干细胞扩增的生物反应器参数

Bioreactor Parameters for Microcarrier-Based Human MSC Expansion under Xeno-Free Conditions in a Vertical-Wheel System.

作者信息

Lembong Josephine, Kirian Robert, Takacs Joseph D, Olsen Timothy R, Lock Lye Theng, Rowley Jon A, Ahsan Tabassum

机构信息

RoosterBio, Inc., 5295 Westview Drive, Suite 275, Frederick, MD 21703, USA.

出版信息

Bioengineering (Basel). 2020 Jul 8;7(3):73. doi: 10.3390/bioengineering7030073.

Abstract

Human mesenchymal stem/stromal cells (hMSCs) have been investigated and proven to be a well-tolerated, safe therapy for a variety of indications, as shown by over 900 registered hMSC-based clinical trials. To meet the commercial demand for clinical manufacturing of hMSCs, production requires a scale that can achieve a lot size of ~100B cells, which requires innovative manufacturing technologies such as 3D bioreactors. A robust suspension bioreactor process that can be scaled-up to the relevant scale is therefore crucial. In this study, we developed a fed-batch, microcarrier-based bioreactor process, which enhances media productivity and drives a cost-effective and less labor-intensive hMSC expansion process. We determined parameter settings for various stages of the culture: inoculation, bioreactor culture, and harvest. Addition of a bioreactor feed, using a fed-batch approach, was necessary to replenish the mitogenic factors that were depleted from the media within the first 3 days of culture. Our study resulted in an optimized hMSC culture protocol that consistently achieved hMSC densities between 2 × 10-6 × 10 cells/mL within 5 days with no media exchange, maintaining the final cell population doubling level (PDL) at 16-20. Using multiple hMSC donors, we showed that this process was robust and yielded hMSCs that maintained expansion, phenotypic characteristic, and functional properties. The developed process in a vertical-wheel suspension bioreactor can be scaled to the levels needed to meet commercial demand of hMSCs.

摘要

人类间充质干/基质细胞(hMSCs)已得到研究,并被证明是一种耐受性良好、安全的治疗方法,可用于多种适应症,900多项已注册的基于hMSCs的临床试验表明了这一点。为了满足hMSCs临床生产的商业需求,生产规模需要达到约100B个细胞的批量,这就需要创新的制造技术,如3D生物反应器。因此,一种能够扩大到相关规模的强大的悬浮生物反应器工艺至关重要。在本研究中,我们开发了一种基于微载体的分批补料生物反应器工艺,该工艺提高了培养基的生产率,并推动了一种经济高效且劳动强度较低的hMSCs扩增过程。我们确定了培养各个阶段的参数设置:接种、生物反应器培养和收获。采用分批补料方法添加生物反应器进料对于补充在培养的前3天内从培养基中耗尽的促有丝分裂因子是必要的。我们的研究得出了一种优化的hMSCs培养方案,该方案在5天内无需更换培养基即可始终实现2×10 - 6×10个细胞/mL的hMSCs密度,将最终细胞群体倍增水平(PDL)维持在16 - 20。使用多个hMSCs供体,我们表明该工艺是稳健的,并且产生的hMSCs保持了扩增能力、表型特征和功能特性。在垂直轮悬浮生物反应器中开发的工艺可以扩大到满足hMSCs商业需求所需的水平。

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