机构：[1]College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao, 266042, People’s Republic of China[2]First People’s Hospital of Yunnan Province, Kunming, 650021, People’s Republic of China云南省第一人民医院
The mathematical model of gas-solid flow 2D fluidized bed was established. The CFD simulation was carried out with commercial software FLUENT6.3 by using Eulerian-Eulerian multiphase models, based on the kinetic theory of granular flow and PC-SIMPLE algorithm. In order to provide a basis on optimizing the operating conditions of the fluidized bed applied in benzene series organosilicon reactor, the processes of bubble formation, growth and disappearance under different cases were analyzed.
基金：
This work was supported by the Shandong Natural Science Foundation (No. ZR2011BQ006) and the
National Natural Science Foundation of China (No.21276132).
语种：
外文
WOS：
第一作者：
第一作者机构：[1]College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao, 266042, People’s Republic of China
通讯作者：
推荐引用方式(GB/T 7714)：
XinFeng Han,JianLong Li,Ning Xu.CFD Simulation of the Fluidized Bed Applied in the Synthesis of Benzene Series Organosilicon[J].MATERIALS PROCESSING AND MANUFACTURING III, PTS 1-4.2013,753-755:2663-+.doi:10.4028/www.scientific.net/AMR.753-755.2663.
APA：
XinFeng Han,JianLong Li&Ning Xu.(2013).CFD Simulation of the Fluidized Bed Applied in the Synthesis of Benzene Series Organosilicon.MATERIALS PROCESSING AND MANUFACTURING III, PTS 1-4,753-755,
MLA：
XinFeng Han,et al."CFD Simulation of the Fluidized Bed Applied in the Synthesis of Benzene Series Organosilicon".MATERIALS PROCESSING AND MANUFACTURING III, PTS 1-4 753-755.(2013):2663-+
