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2012
DOI: 10.5301/ijao.5000077
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Microcarrier-based Expansion Process for hMSCs with High Vitality and Undifferentiated Characteristics

Abstract: For cell therapy, a high biomass of human mesenchymal stem cells (hMSCs) is required for clinical applications, such as in the form of encapsulated implants. An easy and reproducible microcarrier-based stirred tank reactor cultivation process for hMSCs in 1.68 L scale is described. To avoid medium changes, studies comparing high-glucose DMEM (DMEM-HG) with low-glucose EMEM were performed showing that high-glucose medium has positive effects on cell proliferation and that cell differentiability remains. Studies… Show more

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Cited by 44 publications
(44 citation statements)
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“…At the end of the cultivation, a cell density of around 50 000 cells per cm 2 growth surface, a total cells number up to 4 · 10 8 cells per L of production volume, an expansion factor of 7.2 and a cell yield after harvest of over 95 % was determined. Quality control of the harvested hMSC-TERT showed high viabilities and differentiability [60].…”
Section: Expansion Of Hmscs In Dynamic Systemsnew Conceptsmentioning
confidence: 99%
“…At the end of the cultivation, a cell density of around 50 000 cells per cm 2 growth surface, a total cells number up to 4 · 10 8 cells per L of production volume, an expansion factor of 7.2 and a cell yield after harvest of over 95 % was determined. Quality control of the harvested hMSC-TERT showed high viabilities and differentiability [60].…”
Section: Expansion Of Hmscs In Dynamic Systemsnew Conceptsmentioning
confidence: 99%
“…For example for hMSC-TERT ATMP production, it is not only important to efficiently detach cells, but also to keep them viable (and undifferentiated). This gets challenging when production takes places in dynamic systems (stirred tank reactors (Cierpka et al, 2013;Elseberg et al, 2012), fixed bed-systems (Weber et al, 2010a;2010b;2010c) and the harvested cells are further processed (e.g., beadto-bead transfer, cell encapsulation (Freimark et al, 2010). Trypsin is unsuitable for hMSC-TERT detachment out of dynamic systems and for detachment of further processed cells.…”
Section: Discussionmentioning
confidence: 99%
“…Microcarriers 2-5 mm in diameter are often used for FBR processes, whereas those used in fluidized bed reactors are typically 1 mm in diameter and those used in STRs are generally 100-300 µm in diameter [80]. Glass has been used as a cell culture growth surface for decades [81], and low-density microcarriers with a copolymer plastic core and a high-silica glass coating were used for the expansion of hMSC-TERT in serum-containing medium [51,82]. These results are based on a microcarrier choice for the hMSC-TERT cell line resulting in strong proliferation and a good yield of detached cells for glass and polystyrene microcarriers [36].…”
Section: Microcarrier Choicementioning
confidence: 99%
“…Initial seeding densities of 1-3 × 10 4 cells/cm 2 are nearly independent from the available growth surface area. The inoculation strategy is often based on intermittent agitation or flow depending on the system [50,51].…”
Section: Cell Expansion In Bioreactorsmentioning
confidence: 99%
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