Homogenisation and oxygen transfer rates in large agitated and sparged animal cell bioreactors: Some implications for growth and production |
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Authors: | Alvin W Nienow Christian Langheinrich Neil C Stevenson A Nicholas Emery Timothy M Clayton Nigel K H Slater |
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Institution: | (1) BBSRC Centre for Biochemical Engineering, The University of Birmingham, Birmingham, UK;(2) Glaxo Wellcome, Beckenham, Kent, UK;(3) The Dept of Chemical Engineering, Aston University, Birmingham, UK |
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Abstract: | Because of concern for cell damage, very low agitation energy inputs have been used in industrial animal cell bioreactors, typical values being two orders of magnitude less than those found in bacterial fermentations. Aeration rates are also very small. As a result, such bioreactors might be both poorly mixed and also unable to provide the higher oxygen up-take rates demanded by more intensive operation. This paper reports experimental studies both of K
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a and of mixing (via pH measurements) in bioreactors up to 8 m3 at Wellcome and of scaled down models of such reactors at Birmingham. Alongside these physical measurements, sensitivity of certain cell lines to continuously controlled dO2 has been studied and the oxygen up-take rates measured in representative growth conditions. An analysis of characteristic times and mixing theory, together with other recent work showing that more vigorous agitation and aeration can be used especially in the presence of Pluronic F-68, indicates ways of improving their performance. pH gradients offer a special challenge. |
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Keywords: | cell culture mixing time oxygen demand oxygen transfer pH and dO2 sensitivity scale-up |
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