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 .
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.
出处
《环境科学》
EI
CAS
CSCD
北大核心
2003年第5期39-43,共5页
Environmental Science
关键词
内循环流化床
烟气脱硫
固含率
internally circulating fluidized bed
FGD
solid hold-up
