Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes

The potential of human mesenchymal stem cells (hMSCs) for allogeneic cell therapies has created a large amount of interest. However, this presupposes the availability of efficient scale-up procedures. Promising results have been reported for stirred bioreactors that operate with microcarriers. Recen...

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Main Authors: Valentin Jossen, Cedric Schirmer, Dolman Mostafa Sindi, Regine Eibl, Matthias Kraume, Ralf Pörtner, Dieter Eibl
Format: Article
Language:English
Published: Wiley 2016-01-01
Series:Stem Cells International
Online Access:http://dx.doi.org/10.1155/2016/4760414
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author Valentin Jossen
Cedric Schirmer
Dolman Mostafa Sindi
Regine Eibl
Matthias Kraume
Ralf Pörtner
Dieter Eibl
author_facet Valentin Jossen
Cedric Schirmer
Dolman Mostafa Sindi
Regine Eibl
Matthias Kraume
Ralf Pörtner
Dieter Eibl
author_sort Valentin Jossen
collection DOAJ
description The potential of human mesenchymal stem cells (hMSCs) for allogeneic cell therapies has created a large amount of interest. However, this presupposes the availability of efficient scale-up procedures. Promising results have been reported for stirred bioreactors that operate with microcarriers. Recent publications focusing on microcarrier-based stirred bioreactors have demonstrated the successful use of Computational Fluid Dynamics (CFD) and suspension criteria (NS1u, NS1) for rapidly scaling up hMSC expansions from mL- to pilot scale. Nevertheless, one obstacle may be the formation of large microcarrier-cell-aggregates, which may result in mass transfer limitations and inhomogeneous distributions of stem cells in the culture broth. The dependence of microcarrier-cell-aggregate formation on impeller speed and shear stress levels was investigated for human adipose derived stromal/stem cells (hASCs) at the spinner scale by recording the Sauter mean diameter (d32) versus time. Cultivation at the suspension criteria provided d32 values between 0.2 and 0.7 mm, the highest cell densities (1.25 × 106 cells mL−1 hASCs), and the highest expansion factors (117.0 ± 4.7 on day 7), while maintaining the expression of specific surface markers. Furthermore, suitability of the suspension criterion NS1u was investigated for scaling up microcarrier-based processes in wave-mixed bioreactors for the first time.
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spelling doaj-art-842d9c2787bf43e4ab5b5f8943a168c82025-02-03T01:30:29ZengWileyStem Cells International1687-966X1687-96782016-01-01201610.1155/2016/47604144760414Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production ProcessesValentin Jossen0Cedric Schirmer1Dolman Mostafa Sindi2Regine Eibl3Matthias Kraume4Ralf Pörtner5Dieter Eibl6Institute of Chemistry and Biotechnology, Zurich University of Applied Sciences, Campus Grüental, 8820 Wädenswil, SwitzerlandInstitute of Chemistry and Biotechnology, Zurich University of Applied Sciences, Campus Grüental, 8820 Wädenswil, SwitzerlandInstitute of Chemistry and Biotechnology, Zurich University of Applied Sciences, Campus Grüental, 8820 Wädenswil, SwitzerlandInstitute of Chemistry and Biotechnology, Zurich University of Applied Sciences, Campus Grüental, 8820 Wädenswil, SwitzerlandDepartment of Process Engineering, Chair of Chemical and Process Engineering, Technical University of Berlin, Strasse des 17.Juni 135, 10623 Berlin, GermanyDepartment of Bioprocess and Biosystems Engineering, Technical University of Hamburg, Denickestrasse 1, 21073 Hamburg, GermanyInstitute of Chemistry and Biotechnology, Zurich University of Applied Sciences, Campus Grüental, 8820 Wädenswil, SwitzerlandThe potential of human mesenchymal stem cells (hMSCs) for allogeneic cell therapies has created a large amount of interest. However, this presupposes the availability of efficient scale-up procedures. Promising results have been reported for stirred bioreactors that operate with microcarriers. Recent publications focusing on microcarrier-based stirred bioreactors have demonstrated the successful use of Computational Fluid Dynamics (CFD) and suspension criteria (NS1u, NS1) for rapidly scaling up hMSC expansions from mL- to pilot scale. Nevertheless, one obstacle may be the formation of large microcarrier-cell-aggregates, which may result in mass transfer limitations and inhomogeneous distributions of stem cells in the culture broth. The dependence of microcarrier-cell-aggregate formation on impeller speed and shear stress levels was investigated for human adipose derived stromal/stem cells (hASCs) at the spinner scale by recording the Sauter mean diameter (d32) versus time. Cultivation at the suspension criteria provided d32 values between 0.2 and 0.7 mm, the highest cell densities (1.25 × 106 cells mL−1 hASCs), and the highest expansion factors (117.0 ± 4.7 on day 7), while maintaining the expression of specific surface markers. Furthermore, suitability of the suspension criterion NS1u was investigated for scaling up microcarrier-based processes in wave-mixed bioreactors for the first time.http://dx.doi.org/10.1155/2016/4760414
spellingShingle Valentin Jossen
Cedric Schirmer
Dolman Mostafa Sindi
Regine Eibl
Matthias Kraume
Ralf Pörtner
Dieter Eibl
Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
Stem Cells International
title Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
title_full Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
title_fullStr Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
title_full_unstemmed Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
title_short Theoretical and Practical Issues That Are Relevant When Scaling Up hMSC Microcarrier Production Processes
title_sort theoretical and practical issues that are relevant when scaling up hmsc microcarrier production processes
url http://dx.doi.org/10.1155/2016/4760414
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