Effect of Gas Distributor Structure on Fluidization Characteristics in a Gas-Solid Fluidized Bed  

作　　者：Jang Kwangbyol Feng Yali Li Haoran 

机构地区：[1]School of Civil&Resource Engineering,University of Science and Technology Beijing,Beijing 100083 [2]National Key Laboratory of Biochemical Engineering,Institute of Process Engineering,Chinese Academy of Sciences,Beijing 100080

出　　处：《China Petroleum Processing & Petrochemical Technology》2020年第2期102-110,共9页中国炼油与石油化工（英文版）

基　　金：supported by the China Ocean Mineral Resources Research&Development Program(DY125-15-T-08);the National Natural Science Foundation of China(21176026,21176242)。

摘　　要：In the present paper,the experimental method and computational fluid dynamics(CFD)method were used to investigate the effect of gas distributors with different orifice sizes and orifice pitches on fluidization characteristics in a gas-solid fluidized bed.The Euler-Euler two fluid model(TFM)approach based on the kinetic theory of granular flow(KTGF)and the standard k-epsilon turbulence model was employed in the numerical simulation by using ANSYS Fluent 15.0.The results showed that the orifice size and the orifice pitch of gas distributor had a significant influence on the flow characteristics in the gas-solid fluidized bed.With a decreasing orifice size and orifice pitch of gas distributor having the same opening area,the distributor pressure drop,the initial bubble size,and the height of dead zone just above the distributor were decreased,and the bed pressure drop was increased more than that of the larger orifice size and orifice pitch of distributors,the distribution of solid volume fraction was also more homogeneous for the smaller orifice size.

关 键 词：fluidized bed gas distributor orifice size BUBBLE numerical simulation 

分 类 号：TQ021.1[化学工程]