Experimental and theoretical considerations on oxygen supply for animal cell growth in fixed-bed reactors

被引:54
作者
Fassnacht, D [1 ]
Pörtner, R [1 ]
机构
[1] Tech Univ Hamburg Harburg, D-21071 Hamburg, Germany
关键词
fixed-bed; reaction-diffusion model; hybridoma; oxygen limitation; hyperoxia;
D O I
10.1016/S0168-1656(99)00129-7
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The supply of oxygen is a crucial parameter when cultivating animal cells in fixed-bed reactors because of the reaction-diffusion limitation within the porous carriers. To reduce limitation and increase productivity, the dissolved oxygen concentration was raised to above air saturation (hyperoxia) in long-term experiments using hybridoma cultures. This resulted in a threefold increase of the steady-state antibody production at high dilution rates compared to air saturated medium. A reaction-diffusion model was developed as a tool to describe the oxygen distribution in fixed-bed systems. The model corresponded well to the experimental data. It was also used to study the influence of several parameters on the performance of the fixed-bed system, such as the carrier size, the dissolved oxygen concentration, or the superficial flow velocity. By adapting the model it was shown that reaction-diffusion limitation is generally not a problem for other substrates such as glucose or glutamine. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:169 / 184
页数:16
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