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CFD Simulation and Optimization of Gas-Solid Phase Temperature of Isothermal Acetylene Hydrogenation Reactor  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:CFD Simulation and Optimization of Gas-Solid Phase Temperature of Isothermal Acetylene Hydrogenation Reactor

作者:Hu, Guihua[1,2];Ye, Zhencheng[1,2];Du, Wenli[1,2];Qian, Feng[1,2]

机构:[1]East China Univ Sci & Technol, State Key Lab Chem Engn, 130 Meilong Rd, Shanghai 200237, Peoples R China;[2]East China Univ Sci & Technol, Sch Informat Sci & Engn, 130 Meilong Rd, Shanghai 200237, Peoples R China

年份:2018

卷号:16

期号:5

外文期刊名:INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING

收录:;EI(收录号:20181605034406);WOS:【SCI-EXPANDED(收录号:WOS:000431875200006)】;

基金:This study is supported by National Natural Science Foundation of China (Key Program: 61333010), National Science Fund for Distinguished Young Scholars (61725301), National Natural Science Foundation of China (21506050) and the Programme of Introducing Talents of Discipline to Universities (the 111 Project) under Grant B17017.

语种:英文

外文关键词:acetylene hydrogenation; CFD; two-temperature porous medium model; optimization

摘要:Gas-solid coupled heat transfer in an industrial isothermal acetylene hydrogenation reactor was carried out using computational fluid dynamics (CFD). A two-temperature porous medium model was established by adding source terms to energy equations of the solid and gas phases. The combination of a genetic algorithm with CFD methods is applied to optimization of the kinetic and process parameters of the reaction. The model was validated by comparing the simulated results with those obtained from a one-temperature porous medium model, a two-temperature porous medium model, and industrial data. The optimal hydrogen-to-acetylene ratio and inlet temperature are 1.78 and 326K, respectively. The optimized ethylene yield increase and hydrogenation selectivity are 0.53 % and 0.18 % higher than the values before optimization, respectively. Finally, the effects of the hydrogen-to-acetylene ratio and inlet temperature on the increase in ethylene yield and hydrogenation selectivity are analyzed. Therefore, the hydrogen-to-acetylene ratio and inlet temperature should be reasonably controlled during production.

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