Recent developments in modeling of solid-state fermentation: heat and mass transfer in bioreactors

被引:91
作者
Mitchell, DA
von Meien, OF
Krieger, N
机构
[1] Univ Fed Parana, Dept Bioquim & Biol Mol, BR-81531990 Curitiba, Parana, Brazil
[2] Univ Fed Parana, Dept Engn Quim, BR-81531990 Curitiba, Parana, Brazil
[3] Univ Fed Parana, Dept Quim, BR-81531990 Curitiba, Parana, Brazil
关键词
solid-state fermentation; bioreactors; modeling; packed-bed bioreactors; rotating-drum bioreactors; gas-solid fluidized bed bioreactors; tray bioreactors;
D O I
10.1016/S1369-703X(02)00126-2
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 [微生物学]; 0836 [生物工程]; 090102 [作物遗传育种]; 100705 [微生物与生化药学];
摘要
Mathematical models are important tools for optimizing the design and operation of solid-state fermentation (SSF) bioreactors. Such models must describe the transport phenomena within the substrate bed and mass and energy exchanges between the bed and the other subsystems of the bioreactor, such as the bioreactor wall and headspace gases. The sophistication with which this has been done for SSF has improved markedly over the last decade or so. The current article reviews these advances, showing how the various transport phenomena have been modeled. It also discusses the insights that have been achieved through the modeling work and the improvements to models that will be necessary in order to make them even more powerful tools in the optimization of bioreactor performance. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:137 / 147
页数:11
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