Protein-free media for cardiac differentiation of hPSCs in 2000 mL suspension culture.

BACKGROUND: Commonly used media for the differentiation of human pluripotent stem cells into cardiomyocytes (hPSC-CMs) contain high concentrations of proteins, in particular albumin, which is prone to quality variations and presents a substantial cost factor, hampering the clinical translation of in vitro-generated cardiomyocytes for heart repair. To overcome these limitations, we have developed chemically defined, entirely protein-free media based on RPMI, supplemented with L-ascorbic acid 2-phosphate (AA-2P) and either the non-ionic surfactant Pluronic F-68 or a specific polyvinyl alcohol (PVA). METHODS AND RESULTS: Both media compositions enable the efficient, directed differentiation of embryonic and induced hPSCs, matching the cell yields and cardiomyocyte purity ranging from 85 to 99% achieved with the widely used protein-based CDM3 medium. The protein-free differentiation approach was readily up-scaled to a 2000 mL process scale in a fully controlled stirred tank bioreactor in suspension culture, producing > 1.3 × 109 cardiomyocytes in a single process run. Transcriptome analysis, flow cytometry, electrophysiology, and contractile force measurements revealed that the mass-produced cardiomyocytes differentiated in protein-free medium exhibit the expected ventricular-like properties equivalent to the well-established characteristics of CDM3-control cells. CONCLUSIONS: This study promotes the robustness and upscaling of the cardiomyogenic differentiation process, substantially reduces media costs, and provides an important step toward the clinical translation of hPSC-CMs for heart regeneration.

Standardized production of hPSC-derived cardiomyocyte aggregates in stirred spinner flasks.

A promising cell-therapy approach for heart failure aims at differentiating human pluripotent stem cells (hPSCs) into functional cardiomyocytes (CMs) in vitro to replace the disease-induced loss of patients' heart muscle cells in vivo. But many challenges remain for the routine clinical application of hPSC-derived CMs (hPSC-CMs), including good manufacturing practice (GMP)-compliant production strategies. This protocol describes the efficient generation of hPSC-CM aggregates in suspension culture, emphasizing process simplicity, robustness and GMP compliance. The strategy promotes clinical translation and other applications that require large numbers of CMs. Using a simple spinner-flask platform, this protocol is applicable to a broad range of users with general experience in handling hPSCs without extensive know-how in biotechnology. hPSCs are expanded in monolayer to generate the required cell numbers for process inoculation in suspension culture, followed by stirring-controlled formation of cell-only aggregates at a 300-ml scale. After 48 h at checkpoint (CP) 0, chemically defined cardiac differentiation is induced by WNT-pathway modulation through use of the glycogen-synthase kinase-3 inhibitor CHIR99021 (WNT agonist), which is replaced 24 h later by the chemical WNT-pathway inhibitor IWP-2. The exact application of the described process parameters is important to ensure process efficiency and robustness. After 10 d of differentiation (CP I), the production of ≥100 × 106 CMs is expected. Moreover, to 'uncouple' cell production from downstream applications, continuous maintenance of CM aggregates for up to 35 d in culture (CP II) is demonstrated without a reduction in CM content, supporting downstream logistics while potentially overcoming the requirement for cryopreservation.

Matrix-free human pluripotent stem cell manufacturing by seed train approach and intermediate cryopreservation.

BACKGROUND: Human pluripotent stem cells (hPSCs) have an enormous therapeutic potential, but large quantities of cells will need to be supplied by reliable, economically viable production processes. The suspension culture (three-dimensional; 3D) of hPSCs in stirred tank bioreactors (STBRs) has enormous potential for fuelling these cell demands. In this study, the efficient long-term matrix-free suspension culture of hPSC aggregates is shown. METHODS AND RESULTS: STBR-controlled, chemical aggregate dissociation and optimized passage duration of 3 or 4 days promotes exponential hPSC proliferation, process efficiency and upscaling by a seed train approach. Intermediate high-density cryopreservation of suspension-derived hPSCs followed by direct STBR inoculation enabled complete omission of matrix-dependent 2D (two-dimensional) culture. Optimized 3D cultivation over 8 passages (32 days) cumulatively yielded ≈4.7 × 1015 cells, while maintaining hPSCs' pluripotency, differentiation potential and karyotype stability. Gene expression profiling reveals novel insights into the adaption of hPSCs to continuous 3D culture compared to conventional 2D controls. CONCLUSIONS: Together, an entirely matrix-free, highly efficient, flexible and automation-friendly hPSC expansion strategy is demonstrated, facilitating the development of good manufacturing practice-compliant closed-system manufacturing in large scale.

Process control and in silico modeling strategies for enabling high density culture of human pluripotent stem cells in stirred tank bioreactors.

The routine therapeutic and industrial applications of human pluripotent stem cells (hPSCs) require their constant mass supply by robust, efficient, and economically viable bioprocesses. Our protocol describes the fully controlled expansion of hPSCs in stirred tank bioreactors (STBRs) enabling cell densities of 35 × 106 cells/mL while reducing culture medium consumption by 75%. This is achieved by in silico process modeling and computable upscaling. We provide a detailed blueprint for systematic process development of hPSCs and their progenies. For complete details on the use and execution of this protocol, please refer to Manstein et al. (2021).

High density bioprocessing of human pluripotent stem cells by metabolic control and in silico modeling.

To harness the full potential of human pluripotent stem cells (hPSCs) we combined instrumented stirred tank bioreactor (STBR) technology with the power of in silico process modeling to overcome substantial, hPSC-specific hurdles toward their mass production. Perfused suspension culture (3D) of matrix-free hPSC aggregates in STBRs was applied to identify and control process-limiting parameters including pH, dissolved oxygen, glucose and lactate levels, and the obviation of osmolality peaks provoked by high density culture. Media supplements promoted single cell-based process inoculation and hydrodynamic aggregate size control. Wet lab-derived process characteristics enabled predictive in silico modeling as a new rational for hPSC cultivation. Consequently, hPSC line-independent maintenance of exponential cell proliferation was achieved. The strategy yielded 70-fold cell expansion in 7 days achieving an unmatched density of 35 × 106 cells/mL equivalent to 5.25 billion hPSC in 150 mL scale while pluripotency, differentiation potential, and karyotype stability was maintained. In parallel, media requirements were reduced by 75% demonstrating the outstanding increase in efficiency. Minimal input to our in silico model accurately predicts all main process parameters; combined with calculation-controlled hPSC aggregation kinetics, linear process upscaling is also enabled and demonstrated for up to 500 mL scale in an independent bioreactor system. Thus, by merging applied stem cell research with recent knowhow from industrial cell fermentation, a new level of hPSC bioprocessing is revealed fueling their automated production for industrial and therapeutic applications.