1999
DOI: 10.1016/s0168-1656(99)00129-7
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Experimental and theoretical considerations on oxygen supply for animal cell growth in fixed-bed reactors

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Cited by 81 publications
(52 citation statements)
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“…In addition to scaffold-based approaches, 3D MSC expansion can also occur in suspension [38,83] and within spheroids [40]. 3D MSC expansion has been paired with dynamic stimulation because cell viability is restricted to 100-200 mm from the surface because of diffusive nutrient transport limitations when cultured statically [84]. Bioreactors are devices that facilitate the development of biological and/or biochemical processes through closely monitored and user-controlled operating parameters such as pH, temperature, nutrient supply, and waste removal [85].…”
Section: D Expansionmentioning
confidence: 99%
“…In addition to scaffold-based approaches, 3D MSC expansion can also occur in suspension [38,83] and within spheroids [40]. 3D MSC expansion has been paired with dynamic stimulation because cell viability is restricted to 100-200 mm from the surface because of diffusive nutrient transport limitations when cultured statically [84]. Bioreactors are devices that facilitate the development of biological and/or biochemical processes through closely monitored and user-controlled operating parameters such as pH, temperature, nutrient supply, and waste removal [85].…”
Section: D Expansionmentioning
confidence: 99%
“…Direct axial perfusion of 3D porous constructs with medium in axial-flow packed bed bioreactors (aPBBs) uses convection to enhance oxygen and nutrients transport to cells internal to the construct [24][25][26][27]. However, at low axial superficial velocity the dissolved oxygen and nutrients concentrations may steeply decrease towards the end of the construct leading to poor cell nourishment and causing the formation of a necrotic end zone [28,29]. Cell perfusion at high axial superficial velocity to keep cells viable and differentiated anywhere in the construct may cause cell wash-out [30].…”
Section: Introductionmentioning
confidence: 99%
“…Nevertheless, the fixed-bed bioreactor presents some drawbacks, such as a difficult monitoring of the cell concentration in the fixed-bed during the process and the presence of cell concentration gradients (Fassnacht et al 1999;Warnock et al 2005). The homogeneity of the cell concentration in the fixed-bed during the whole process is very important to reach the best yield of the bioreactor (Sadettin et al 2005;Nienow 2006).…”
Section: Introductionmentioning
confidence: 99%
“…A mathematical model of this fixed-bed bioreactor can be used to improve the control of the bioreactor and can contribute to the efficiency definition of the operating conditions leading to the homogeneity of the cell concentration in the fixed-bed. The gradients of the cell and the extracellular species concentrations inside a single carrier have been considered in several models developed in previous works (Tramper 1995;Fassnacht et al 1999;Pörtner et al 2005). The extrapolation from a single carrier to a stacking of carriers is seldom reported in the literature.…”
Section: Introductionmentioning
confidence: 99%