咨询与建议

看过本文的还看了

相关文献

该作者的其他文献

文献详情 >Axial gas mixing in conical sp... 收藏

Axial gas mixing in conical spouted beds with high density particles

作     者:Neslin Dogan Murat Koksal Gorkem Kulah Neslin Dogan;Murat Koksal;Gorkem Kulah

作者机构:Department of Chemical EngineeringMiddle East Technical UniversityAnkaraTurkey Department of Mechanical EngineeringHacettepe UniversityBeytepeAnkaraTurkey 

出 版 物:《Particuology》 (颗粒学报(英文版))

年 卷 期:2023年第81卷第10期

页      面:45-57页

核心收录:

学科分类:07[理学] 0817[工学-化学工程与技术] 0805[工学-材料科学与工程(可授工学、理学学位)] 070202[理学-粒子物理与原子核物理] 0702[理学-物理学] 

基  金:This work was carried out with the financial support of the Scientific and Technological Research Council of Turkey(Project No:MAG 115M392) 

主  题:Conical spouted bed Gas dispersion coefficient Axial gas mixing High-density particles 

摘      要:Conical spouted beds operating with high-density particles(ρp2500 kg/m^(3))have recently gained attention because of their potential use as nuclear fuel coaters for next-generation nuclear *** the literature,the number of axial gas mixing studies in conical and conical-cylindrical spouted beds is very limited and all axial mixing studies were carried out with relatively light particles(ρp≤2500 kg/m^(3)).Therefore,the objective of this study was to generate experimental data that can be used to explain the gas axial mixing behavior in conical spouted beds operating with both low-and high-density *** were conducted in two(γ=30°,60°)conical spouted beds with three different types of particles:zirconia(ρp=6050 kg/m^(3)),zirconia toughened alumina(ρp=3700 kg/m^(3))and glass beads(ρp=2460 kg/m^(3)).In order to be able to compare experimental data obtained at different conditions,a 1-D convection-diffusion gas mixing model originally developed by San Joséet al.(1995)was implemented to determine the axial dispersion *** results show that the axial dispersion coefficients range between m^(2)/s and m^(2)/s,increase with superficial gas velocity and are higher than the corresponding dispersion coefficients of fixed beds,lower than the dispersion coefficients of fluidized beds and in the same range with the cylindrical spouted beds reported in the *** corresponding Peclet numbers were in the range of 0.6–7.8 for all operating conditions and slightly higher Peclet numbers were obtained with glass beads indicating the relative importance of gas convective transport over gas dispersion for light particles compared to heavy particles.

读者评论 与其他读者分享你的观点

用户名:未登录
我的评分