首页|Numerical simulation on gas-solid flow during circulating fluidized roasting of bauxite by a computational particle fluid dynamics method
Numerical simulation on gas-solid flow during circulating fluidized roasting of bauxite by a computational particle fluid dynamics method
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A full-cycle numerical simulation of a circulating fluidized bed(CFB)by the use of the computational particle fluid dynamics(CPFD)method has been developed.The effects of the presence or absence of the secondary air,different secondary air positions,and different secondary air ratios on the gas-solid flow characteristics were explored.The results show that the presence of the secondary air makes a core-annular structure of the velocity distribution of particles in the fluidized bed,which enhances the uni-formity of particles'distribution and the stability of fluidization.The position and the ratio of the sec-ondary air have a significant impact on the particle distribution,particle flow rate,and gas flow rate in the fluidized bed.When the secondary air position and ratio are optimal,the particles,particle flow rate,and air flow rate in the CFB are evenly distributed,the gas-solid flow state is good,and the CFB can operate stably.
Circulating fluidized bedCPFD methodSecondary air positionSecondary air ratioGas-solid flow characteristics
Chengming Xie、Rongbin Li、Qijin Wei、Fengqin Liu、Hongliang Zhao、Yongmin Zhang、Hong Yong Sohn
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State Key Laboratory of Green and Low-carbon Metallurgy,University of Science and Technology Beijing,Beijing 100083,China
School of Metallurgical and Ecological Engineering,University of Science and Technology Beijing,Beijing 100083,China
BGRIMM Technology Group,Beijing 100160,China
State Key Laboratory of Heavy Oil Processing,China University of Petroleum,Beijing,102249,China
Department of Materials Science and Engineering,The University of Utah,Salt Lake City,UT 84112,USA
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National Key Research and Development Program of ChinaGuangxi Science and Technology Major Project