Optimal medium use for continuous high density perfusion processes

Büntemeyer H, Wallerius C, Lehmann J (1992)
Cytotechnology 9(1-3): 59-67.

Zeitschriftenaufsatz | Veröffentlicht | Englisch
 
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Büntemeyer, HeinoUniBi; Wallerius, Claus; Lehmann, Jürgen
Abstract / Bemerkung
For maintenance of high cell density in continuous perfusion processes not only feeding with substrates but also removal of inhibitors and toxic waste products are of special interest. High perfusion rates cause large volumes of product containing medium which have to be processed in product isolation. In order to minimize these volumes concentrated feed solutions of optimized medium are used. On the other hand, such media may cause high concentrations of toxic or inhibitory metabolites which can negatively influence cell growth and product formation. Especially, if the spent medium (or special parts of it) is used again after product isolation, the removal or even better the control of inhibitor production is of highest importance. We have developed a continuous fermentation concept and system (continuous medium cycle bioreactor, (MCB) in which both limitation and inhibition effects can be generated to identify special substances as limiting or inhibitory components. With the results from those experiments it was possible to lower the total perfusion rate during serum-free perfusion cultures of hybridoma cells and to obtain an optimal substrate utilization. The advantages for decreasing the production costs (for media, special supplements and product isolation) are obvious. The other aim of this study was to identify secreted metabolic waste products as inhibitor or toxic metabolite.
Stichworte
inhibition; re-use; hybridoma growth; toxic metabolites; medium use
Erscheinungsjahr
1992
Zeitschriftentitel
Cytotechnology
Band
9
Ausgabe
1-3
Seite(n)
59-67
ISSN
0920-9069
eISSN
1573-0778
Page URI
https://pub.uni-bielefeld.de/record/1782368

Zitieren

Büntemeyer H, Wallerius C, Lehmann J. Optimal medium use for continuous high density perfusion processes. Cytotechnology. 1992;9(1-3):59-67.
Büntemeyer, H., Wallerius, C., & Lehmann, J. (1992). Optimal medium use for continuous high density perfusion processes. Cytotechnology, 9(1-3), 59-67. https://doi.org/10.1007/BF02521732
Büntemeyer, Heino, Wallerius, Claus, and Lehmann, Jürgen. 1992. “Optimal medium use for continuous high density perfusion processes”. Cytotechnology 9 (1-3): 59-67.
Büntemeyer, H., Wallerius, C., and Lehmann, J. (1992). Optimal medium use for continuous high density perfusion processes. Cytotechnology 9, 59-67.
Büntemeyer, H., Wallerius, C., & Lehmann, J., 1992. Optimal medium use for continuous high density perfusion processes. Cytotechnology, 9(1-3), p 59-67.
H. Büntemeyer, C. Wallerius, and J. Lehmann, “Optimal medium use for continuous high density perfusion processes”, Cytotechnology, vol. 9, 1992, pp. 59-67.
Büntemeyer, H., Wallerius, C., Lehmann, J.: Optimal medium use for continuous high density perfusion processes. Cytotechnology. 9, 59-67 (1992).
Büntemeyer, Heino, Wallerius, Claus, and Lehmann, Jürgen. “Optimal medium use for continuous high density perfusion processes”. Cytotechnology 9.1-3 (1992): 59-67.
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9 Zitationen in Europe PMC

Daten bereitgestellt von Europe PubMed Central.

A novel control scheme for inducing angiostatin-human IgG fusion protein production using recombinant CHO cells in a oscillating bioreactor.
Wang IK, Hsieh SY, Chang KM, Wang YC, Chu A, Shaw SY, Ou JJ, Ho L., J. Biotechnol. 121(3), 2006
PMID: 16162365
Achievement of high cell density and high antibody productivity by a controlled-fed perfusion bioreactor process.
Yang JD, Angelillo Y, Chaudhry M, Goldenberg C, Goldenberg DM., Biotechnol. Bioeng. 69(1), 2000
PMID: 10820333
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Shirai Y, Yamaguchi M, Kobayashi A, Nishi A, Nakamura H, Murakami H., Cytotechnology 14(2), 1994
PMID: 7765240
Growth and interferon-gamma production in batch culture of CHO cells.
Leelavatcharamas V, Emery AN, al-Rubeai M., Cytotechnology 15(1-3), 1994
PMID: 7765954
Catabolic control of hybridoma cells by glucose and glutamine limited fed batch cultures.
Ljunggren J, Haggstrom L., Biotechnol. Bioeng. 44(7), 1994
PMID: 18618848

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