首页 | 本学科首页   官方微博 | 高级检索  
     检索      

内循环流化床烟气脱硫装置结构及流化性能
引用本文:杨柳春,杨文奇,童志权.内循环流化床烟气脱硫装置结构及流化性能[J].环境科学,2003,24(5):39-43.
作者姓名:杨柳春  杨文奇  童志权
作者单位:湘潭大学环境工程系,湘潭,411105
摘    要:提出了开发一种新型内循环流化床烟气脱硫装置的设想,通过不同型式床顶、床底结构的试验,确定了实现这一构想的最佳流化床结构型式;研究了冷态条件下该装置内床料流化的状态及固含率轴向分布情况,初步考察了其流体力学性质.实验结果表明,气速在2.5~5m/s时,装置能实现大量固体颗粒的内循环,床料在床内的运动呈"环-核"结构,床内固体颗粒物浓度高于传统等径流化床,可将其用于烟气脱硫工艺.

关 键 词:内循环流化床  烟气脱硫  固含率
文章编号:0250-3301(2003)05-05-0039
收稿时间:2002/9/10 0:00:00
修稿时间:2002年9月10日

Structure and Fluidization of an Internally Circulating Fluidized Bed for FGD Process
Yang Liuchun,Yang Wenqi and Tong Zhiquan.Structure and Fluidization of an Internally Circulating Fluidized Bed for FGD Process[J].Chinese Journal of Environmental Science,2003,24(5):39-43.
Authors:Yang Liuchun  Yang Wenqi and Tong Zhiquan
Institution:Dept. of Environmental Engineering, Xiangtan University, Xiangtan 411105, China. yangliuc@21cn.com
Abstract:A new internally circulating fluidized bed for FGD process was developed, and different types of top and bottom structures were employed in the experiment to find out the best fluidized bed structure. Fluidizing status, the axial distribution of solid hold-up and the fluid mechanics under cold conditions were investigated .The results indicate that the unit can realize internally circulating of a large number of solid particles which presents an core-annulus structure when the velocity of fluidizing gas was at the range of 2.5 to 5 m/s, and that the solid density in the bed is higher than that in traditional equal diameter fluidized bed, which provide the equipment with potential for application in FGD process.
Keywords:internally circulating fluidized bed  FGD  solid hold-up
本文献已被 CNKI 维普 万方数据 PubMed 等数据库收录!
点击此处可从《环境科学》浏览原始摘要信息
点击此处可从《环境科学》下载免费的PDF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