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CFD modeling of turbulent reacting flow in a semi-batch stirred-tank reactor 被引量:6

CFD modeling of turbulent reacting flow in a semi-batch stirred-tank reactor
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摘要 For the mixing-sensitive reactions, both chemical kinetics and mixing conditions of the reactants determine the distributions of products. The direct quadrature method of moments combining with the interaction by exchange with the mean micro-mixing model(DQMOM-IEM) has been validated for the chemical reacting flows in microreactors. Quite encouraging simulation results offer great promise, but the applicability of this method is needed to be explored furthermore, such as in stirred reactors. In this work, the two-environment DQMOM-IEM model was created with C language and used to customize Fluent through the user-defined functions. The mixing effects on the course of parallel competing chemical reactions carried out in a semi-batch single-phase stirred reactor were predicted. The simulation results show that the rising feed velocity enlarges the volume of reaction zone and maximize the yield of the by-product, which also indicates that the feed stream is more difficultly dispersed into the main stream and the zone surrounding feedpipe exit with high turbulent kinetic dissipation rate cannot be efficiently used. For the mixing-sensitive reactions, both chemical kinetics and mixing conditions of the reactants determine the distributions of products. The direct quadrature method of moments combining with the interaction by exchange with the mean micro-mixing model(DQMOM-IEM) has been validated for the chemical reacting flows in microreactors. Quite encouraging simulation results offer great promise, but the applicability of this method is needed to be explored furthermore, such as in stirred reactors. In this work, the two-environment DQMOM-IEM model was created with C language and used to customize Fluent through the user-defined functions. The mixing effects on the course of parallel competing chemical reactions carried out in a semi-batch single-phase stirred reactor were predicted. The simulation results show that the rising feed velocity enlarges the volume of reaction zone and maximize the yield of the by-product, which also indicates that the feed stream is more difficultly dispersed into the main stream and the zone surrounding feedpipe exit with high turbulent kinetic dissipation rate cannot be efficiently used.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2018年第4期675-683,共9页 中国化学工程学报(英文版)
基金 Supported by the National Basic Research Program of China(2012CB224806) the National Natural Science Foundation of China(21306197,91434126) the Major National Scientific Instrument Development Project(21427814) Jiangsu National Synergetic Innovation Center for Advanced Materials
关键词 反应堆 搅动 流动 CFD 模特儿 混合效果 坦克 化学反应 CFD Mixing Segregation DQMOM-IEM Mixture fraction Stirred tanks
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