Scalable, High-Density Expansion of Human Mesenchymal Stem Cells on Microcarriers Using the Bach Impeller in Stirred-Tank Reactors.

IF 3.5 2区 生物学 Q2 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Tom A Wyrobnik,Laia Miranda,Alan Lam,Steve Oh,Andrea Ducci,Martina Micheletti
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Abstract

This paper describes the results of process developmental experiments to achieve higher cell densities in the manufacturing of hMSCs using the novel Bach impeller in a stirred-tank bioreactor. Engineering experiments have previously shown that the Bach impeller represents an efficient mixing device that suspends particles in fluids at low power inputs. To assess the impeller during biological experiments, the growth performance of Wharton Jelly (WJ)-hMSCs in a 1 L STR equipped with the Bach impeller was evaluated at a variety of culture conditions. The cells attached to Cytodex 1 microcarriers at a concentration of 5.6 g/L and were cultured for 5-7 days. The growth phase was carried out at varying impeller speeds N $N$  = 75, 115, and 150 rpm. Cell growth was additionally evaluated at a microcarrier concentration of 11.2 g/L Cytodex 1. Here, a maximum cell density of up to 1.7 × 106 cells/mL and cell viability > 90% was achieved within 5 culture days, which is amongst the highest cell densities ever attained for a hMSC batch culture. Critical cell quality attributes of the WJ-hMSCs were assessed upon completion of the growth phase, that is, FACS to identify stem cell surface markers, tri-lineage differentiation, and capacity of the cells to form colonies. In addition, informed by the previously described engineering characterization, the 1 L process at N $N$  = 75 rpm was scaled up to the 5 L scale, where WJ-hMSCs were again confirmed to have retained the relevant cell quality attributes. The reported findings are important to determine the design space to which scale-ups to even larger tank sizes can adhere.
在搅拌槽反应器中使用巴赫叶轮在微载体上可扩展、高密度地扩增人间充质干细胞。
本文描述了在搅拌槽生物反应器中使用新型巴赫叶轮制造hMSCs以获得更高细胞密度的工艺开发实验结果。先前的工程实验表明,巴赫叶轮是一种高效的混合装置,可以在低功率输入下悬浮流体中的颗粒。为了在生物实验中对叶轮进行评估,我们在配备巴赫叶轮的1 L STR中评估了沃顿果冻(WJ)-hMSCs在各种培养条件下的生长性能。细胞附着于浓度为5.6 g/L的Cytodex 1微载体上,培养5-7天。生长阶段在不同的叶轮转速N$ N$ = 75、115和150 rpm下进行。在微载体浓度为11.2 g/L Cytodex 1时,进一步评估细胞生长情况。在这里,最大细胞密度高达1.7 × 106个细胞/mL,细胞存活率在5天内达到bbb90 %,这是hMSC批量培养所达到的最高细胞密度之一。WJ-hMSCs的关键细胞质量属性在生长阶段完成时进行评估,即通过FACS识别干细胞表面标记物、三系分化和细胞形成集落的能力。此外,根据之前描述的工程特性,在N$ N$ = 75 rpm下的1 L工艺被扩大到5 L的规模,其中WJ-hMSCs再次被证实保留了相关的细胞质量属性。报告的发现对于确定设计空间具有重要意义,可以将其扩展到更大的储罐尺寸。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Biotechnology and Bioengineering
Biotechnology and Bioengineering 工程技术-生物工程与应用微生物
CiteScore
7.90
自引率
5.30%
发文量
280
审稿时长
2.1 months
期刊介绍: Biotechnology & Bioengineering publishes Perspectives, Articles, Reviews, Mini-Reviews, and Communications to the Editor that embrace all aspects of biotechnology. These include: -Enzyme systems and their applications, including enzyme reactors, purification, and applied aspects of protein engineering -Animal-cell biotechnology, including media development -Applied aspects of cellular physiology, metabolism, and energetics -Biocatalysis and applied enzymology, including enzyme reactors, protein engineering, and nanobiotechnology -Biothermodynamics -Biofuels, including biomass and renewable resource engineering -Biomaterials, including delivery systems and materials for tissue engineering -Bioprocess engineering, including kinetics and modeling of biological systems, transport phenomena in bioreactors, bioreactor design, monitoring, and control -Biosensors and instrumentation -Computational and systems biology, including bioinformatics and genomic/proteomic studies -Environmental biotechnology, including biofilms, algal systems, and bioremediation -Metabolic and cellular engineering -Plant-cell biotechnology -Spectroscopic and other analytical techniques for biotechnological applications -Synthetic biology -Tissue engineering, stem-cell bioengineering, regenerative medicine, gene therapy and delivery systems The editors will consider papers for publication based on novelty, their immediate or future impact on biotechnological processes, and their contribution to the advancement of biochemical engineering science. Submission of papers dealing with routine aspects of bioprocessing, description of established equipment, and routine applications of established methodologies (e.g., control strategies, modeling, experimental methods) is discouraged. Theoretical papers will be judged based on the novelty of the approach and their potential impact, or on their novel capability to predict and elucidate experimental observations.
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