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The manufacturing of viable and functional β‐cell spheroids is required for diabetes cell therapy and drug testing. Mesenchymal stromal/stem cells (MSCs) are known to improve β‐cell viability and functionality. We therefore investigated the aggregation behavior of three different β‐cell lines (rat insulinoma‐1 cell line [INS‐1], mouse insulinoma‐6 cell line [MIN6], and a cell line formed by the electrofusion of primary human pancreatic islets and PANC‐1 cells [1.1B4]), two MSC types, and mixtures of β‐cells and MSCs under different conditions. We screened several static systems to produce uniform β‐cell and MSC spheroids, finding cell‐repellent plates the most suitable. The three different β‐cell lines differed in their aggregation behavior, spheroid size, and growth in the same static environment. We found no major differences in spheroid formation between primary MSCs and an immortalized MSC line, although both differed with regard to the aggregation behavior of the β‐cell lines. All spheroids showed a reduced viability due to mass transfer limitations under static conditions. We therefore investigated three dynamic systems (shaking multi‐well plates, spinner flasks, and shaking flasks). In shaking flasks, there were no β‐cell‐line‐dependent differences in aggregation behavior, resulting in uniform and highly viable spheroids. We found that the aggregation behavior of the β‐cell lines changed in a static coculture with MSCs. The β‐cell/MSC coculture conditions must be refined to avoid a rapid segregation into distinct populations under dynamic conditions. [ABSTRACT FROM AUTHOR]

The great properties of human mesenchymal stromal cells (hMSCs) make these cells an important tool in regenerative medicine. Because of the limitations of hMSCs derived from the bone marrow during isolation and expansion, hMSCs derived from the umbilical cord stroma are a great alternative to overcome these issues. For a large expansion of these cells, we performed a process transfer from static culture to a dynamic system. For this reason, a microcarrier selection out of five microcarrier types was made to achieve a suitable growth surface for the cells. The growth characteristics and metabolite consumption and production were used to compare the cells growth in 12-well plate and spinner flask. The goal to determine relevant process parameters to transfer the expansion process into a stirred tank bioreactor was achieved. [ABSTRACT FROM AUTHOR]