2016
DOI: 10.1016/j.procbio.2016.05.010
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Multiphase mixing characteristics in a microcarrier-based stirred tank bioreactor suitable for human mesenchymal stem cell expansion

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Cited by 28 publications
(18 citation statements)
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“…These have a controlled power input, ensuring the homogeneous mixing of suspension cells and anchorage-dependent adherent cells growing on microcarriers. However, dynamic cultivation systems are a double-edged sword because the homogeneity of cell growth comes at the expense of high shear stress [56,57]. Adherent cell lines can be shielded from shear forces by using porous carriers, and macroporous carriers are advantageous despite mass transfer limitations.…”
Section: Bioreactor Selectionmentioning
confidence: 99%
“…These have a controlled power input, ensuring the homogeneous mixing of suspension cells and anchorage-dependent adherent cells growing on microcarriers. However, dynamic cultivation systems are a double-edged sword because the homogeneity of cell growth comes at the expense of high shear stress [56,57]. Adherent cell lines can be shielded from shear forces by using porous carriers, and macroporous carriers are advantageous despite mass transfer limitations.…”
Section: Bioreactor Selectionmentioning
confidence: 99%
“…Three-phase systems, such as aerated microcarrier-based stirred-tank cultures, show the complex effects of the working volume, carrier concentration and aeration on the power input. Understanding the mixing characteristics of such a system is required to optimize hMSC cultivation [55]. Similarly, for hollow fiber or FBR systems, the flow rate must be defined according to the cell line, microcarrier and system volume [43].…”
Section: Cell Expansion In Bioreactorsmentioning
confidence: 99%
“…During cultivation, the stirrer speed was increased from 55 to 75 rpm and minimal aggregate formation was observed [46]. The mixing characteristics of this three-phase system showed a certain degree of inhomogeneity, but this was beneficial because the cells were allowed rest phases of low shear stress [55].…”
Section: Stirred Tank Reactormentioning
confidence: 99%
“…One of the approaches to address this issue is to optimize configuration and geometry of stirred bioreactors and their impellers for maximum media mixing and minimum hydrodynamic shear stress. Numerous studies (Cioffi et al, ; Dusting, Sheridan, & Hourigan, ; Grein et al, ; Odeleye, Marsh, Osborne, Lye, & Micheletti, ; Santiago, de Campos Giordano, & Suazo, ; Sucosky, Osorio, Brown, & Neitzel, ) made improvements to a certain degree, yet they cannot overcome the fundamental limits imposed by the finite diffusion rate of gases and nutrients and the hydrodynamics. Another approach is to locally shield cells from the hydrodynamic shear stress.…”
Section: Introductionmentioning
confidence: 99%
“…Numerous studies (Cioffi et al, 2008;Dusting, Sheridan, & Hourigan, 2006;Grein et al, 2016;Odeleye, Marsh, Osborne, Lye, & Micheletti, 2014;Santiago, de Campos Giordano, & Suazo, 2011;Sucosky, Osorio, Brown, & Neitzel, 2004) made improvements to a certain degree, yet they cannot overcome the fundamental limits imposed by the finite diffusion rate of gases and nutrients and the hydrodynamics. Another approach is to locally shield cells from the hydrodynamic shear stress.…”
mentioning
confidence: 99%