南京工业大学学报（自然科学版）2013，Vol.35Issue(4)：72-77,6.DOI:10.3969/j.issn.1671-7627.2013.04.015
自吸式反应器的数值模拟及在酵母发酵中的应用
CFD simulation of gas-inducing reactor and its application in yeast production
摘要
Abstract
The gas-liquid two-phase flow and mass transfer in the self-inducing reactor were studied in terms of the computational fluid dynamics (CFD) simulation and experiments of yeast fermentation.CFD results showed that fluid flow and gas-liquid mass transfer in gas-inducing reactor were strengthened with the adding of the gas distributor.For yeast fermentation at the same process conditions,the average yield increased by 23.64％ in self-inducing reactor with the gas distributor.关键词
自吸式反应器/计算流体力学/气液两相流/局部气含率/容积传质系数Key words
gas-inducing reactor/ CFD/ gas-liquid two-phase flow/ local gas holdup/ volumetric mass transfer coefficient分类
化学化工引用本文复制引用
石东升,张庆文,温佳文,宋晓丽,洪厚胜..自吸式反应器的数值模拟及在酵母发酵中的应用[J].南京工业大学学报（自然科学版）,2013,35(4):72-77,6.基金项目
国家高技术研究发展计划(863计划)(2012AA021201) （863计划）
