2008
DOI: 10.1021/bp070324s
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Expansion of Human Neural Precursor Cells in Large‐Scale Bioreactors for the Treatment of Neurodegenerative Disorders

Abstract: The transplantation of in vitro expanded human neural precursor cells (hNPCs) represents a potential new treatment alternative for individuals suffering from incurable neurodegenerative disorders such as Parkinson's disease (PD) and Huntington's disease (HD). However, in order for cell restorative therapy to have widespread therapeutic significance, it will be necessary to generate unlimited quantities of clinical grade hNPCs in a standardized method. We report here that we have developed a serum‐free medium a… Show more

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Cited by 46 publications
(64 citation statements)
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“…For clinical applications, more robust and costeffective cell expansion technologies will be required. In this aspect, expansion methods such as automated bioreactors and rotary culture machines hold promise for generating iPS cell derivatives in bulk [28][29][30][31].…”
Section: Discussionmentioning
confidence: 99%
“…For clinical applications, more robust and costeffective cell expansion technologies will be required. In this aspect, expansion methods such as automated bioreactors and rotary culture machines hold promise for generating iPS cell derivatives in bulk [28][29][30][31].…”
Section: Discussionmentioning
confidence: 99%
“…In smaller vessels, surface aeration as the main mode of oxygen supply is typically sufficient and commonly used due to its simplicity. However, as culture volumes increase and cell densities increase, the surface area to volume ratios decrease and surface aeration may no longer be sufficient to ensure oxygen transport to the cells (Gilbertson et al, 2006;Baghbaderani et al, 2008). Options to increase oxygen transport include increasing agitation rate of the impeller, sparging, or medium additives such as Perfluorocarbons (PFCs) which increase oxygen solubility within the liquid medium.…”
Section: Nutrient and Oxygen Uptakementioning
confidence: 99%
“…There have been thorough reviews elsewhere which have described several approaches to experimentally determine k L a (Garcia-Ochoa & Gomez., 2009). One example that we have used, described by Baghbaderani et al (2008), is as follows. Briefly, the assumption is made that at some point in time the reactor reaches steady state during which any oxygen entering the medium would be immediately consumed by the cells (that is, C O2 equals zero in the medium).…”
Section: Nutrient and Oxygen Uptakementioning
confidence: 99%
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“…High-throughput cell culture experiments at a more economical scale could then be performed for culture optimisation (Kostov et al 2001) and allow for factorial experimental design. While substantial research has been completed in the area of scaled-up production (Baghbaderani et al 2008;Fernandes-Platzgummer et al 2011;Garcia-Ochoa and Gomez 2009;Gilbertson et al 2006;Park et al 2010;Youn et al 2005;Yu et al 2009) to increase cell cultures to clinically meaningful numbers such as the estimated 1 billion cells per patient required for stem cell therapy (Docherty et al 2007), there has been little development in scaling down mammalian cell bioreactor systems. Many scaled-down bioreactors in the literature have been developed to culture Escherichia coli (bacteria) or Saccharomyces cerevisiae (yeast).…”
Section: Small-scale Bioreactorsmentioning
confidence: 99%