首页 | 本学科首页   官方微博 | 高级检索  
     

内构件对高密度提升管内气体混合行为的影响
引用本文:魏飞,杨艳辉,金涌.内构件对高密度提升管内气体混合行为的影响[J].化工学报,2001,52(9):766-770.
作者姓名:魏飞  杨艳辉  金涌
作者单位:清华大学化学工程系
摘    要:在Φ18 6mm的提升管内 ,以空气和FCC颗粒为实验对象 ,采用气体稳态示踪技术对高密度提升管内气体混合规律研究的结果表明 :引入钝体的高密度提升管内 ,远离构件区域的气体在径向上的混合仍符合气体的拟均相二维扩散模型 ,颗粒的引入使得气体的径向扩散变差 .钝体的引入 ,使得床内流体产生强烈的绕流 ,径向分布变得均匀 .模拟结果表明 ,气体的径向扩散系数Er达到了 1.0× 10 3cm2 ·s-1,比提升管 30cm2 ·s-1高出一个半量级 ,可很好地改善高密度提升管内气体的径向混合行为

关 键 词:高密度提升管  钝体内构件  气体混合  稳态示踪  混合模型  流体力学  气固循环流化床反应器
文章编号:0438-1157(2001)08-0766-05
修稿时间:1999年11月15

EFFECT OF INTERNALS ON GAS DISPERSION IN HIGH DENSITY RISER
WEI Fei,YANG Yanhui,JIN Yong.EFFECT OF INTERNALS ON GAS DISPERSION IN HIGH DENSITY RISER[J].Journal of Chemical Industry and Engineering(China),2001,52(9):766-770.
Authors:WEI Fei  YANG Yanhui  JIN Yong
Abstract:Experiment results of the effect of internals in high density circulating fluidized bed (HDCFB) on gas dispersion were reported in this paper .Gas dispersion behavior was investigated by using steady gas tracer (propylene) technique and FCC particles (particle density 1398 kg·m -3 , mean diameter 54 μm) for a 0.186 m ID,9.0 m high riser.Experiment results indicated that gas mixing could be well described by a two-dimensional dispersion model. Due to internals, fluid in HDCFB experienced violent roll flowing,and radial distribution of gas concentration was more uniform than in that free bed.The radial dispersion coefficient showed a value of 1000 cm 2·s -1 ,a one and a half order of magnitude larger than that in conventional HDCFB.
Keywords:high density circulating fluidized bed  bluff internal  gas dispersion  steady tracing  dispersion model
本文献已被 CNKI 万方数据 等数据库收录!
点击此处可从《化工学报》浏览原始摘要信息
点击此处可从《化工学报》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号