作者: R. Manfredini , V. Cavallera , L. Marini , G. Donati
关键词: Mixing (process engineering) 、 Chemistry 、 Limiting oxygen concentration 、 Oxygen transfer 、 Chromatography 、 Dimensionless quantity 、 Axial distribution 、 Aeration 、 Industrial fermentation 、 Oxygen 、 Thermodynamics
摘要: A set of experiments has been performed in an industrial 112 m(3) fermentor order to get a complete map oxygen concentration and temperature distribution the system. Five fermentations non-Newtonian broths two different strains, various operating conditions, were examined. simple model developed which takes into account both mixing mass-transfer properties fermentor, dimensionless parameter identified is sufficient characterize axial reactor any condition.