期刊文献+

CFB-FGD脱硫塔密相区固体颗粒径向运动特性研究

Radial Motion Characteristics of Solid Particles in CFB-FGD Desulfurization Tower Dense Phase
下载PDF
导出
摘要 针对循环流化床烟气脱硫(circulating fluid bed-flue gasdesulfurization,CFB-FGD)过程中遇到的塔内黏壁问题,搭建烟气循环流化床冷态实验台,根据相似理论进行模化试验研究。采用粒子图像测速技术(particle image velocimetry,PIV)对导流板前给料、单侧给料和双侧给料3种不同布置方式下脱硫塔内反应密相区脱硫剂颗粒的径向速度和加速度进行研究,以分析不同给料方式下固体颗粒对脱硫塔壁的冲击和黏附状况。实验结果表明,在双侧给料工况下,固体颗粒的冲壁程度最小,有利于改善塔内黏壁的问题,减少壁面上脱硫灰结垢和给料口积灰,保持脱硫系统稳定运行。 To solve the problem of tower wall sticking in circulating fluidized bed flue gas desulfurization (CFB-FGD) technology, a flue gas circulating fluidized bed cold state test bench was built based on the similarity theory model of experimental research. Through the method of particle image velocimetry (PIV), the radial velocity and acceleration of desulfurizer particles in the dense phase area of the desulfurizing tower under three kinds of feeding modes were compared. The feeding modes were before deflector feeding, unilateral feeding and bilateral feeding. The condition of impact and adhesion of solid particles to the desulfurization tower was analyzed by PIV. The experimental results show that the extent of the impact to the wall of solid particles in the tower under the bilateral feeding layout mode is minimal, which is beneficial to improve the adhesion in the tower wall, reduce scaling of the ash of desulfuration on the wall and the ash clogging in the feeding entrance, and keep the stable operation of the desulfurization system.
出处 《中国电机工程学报》 EI CSCD 北大核心 2013年第8期16-21,5,共6页 Proceedings of the CSEE
关键词 烟气脱硫 循环流化床 给料方式 粒子图像测速技术 径向运动 flue gas desulfurization (FGD) circulating fluidized bed (CFB) feeding mode particle image velocimetry radial motion
  • 相关文献

参考文献20

  • 1魏星,李伟力,凡凤仙,袁竹林.脱硫塔气固两相流场优化的数值模拟研究[J].中国电机工程学报,2006,26(7):12-18. 被引量:44
  • 2赵旭东,项光明,姚强,马春元.循环流化床烟气脱硫吸收塔内结垢现象及机理分析[J].化工学报,2006,57(2):397-402. 被引量:20
  • 3Aguillon J, Shakourzadeh K, Guigon P. A new method for local solid concentration measurement in circulating fluidizedbed[J]. Powder Technol, 1996, 86(9): 251-255.
  • 4Kaoru Miyazaki, Gang Chen Fujao Yamamoto, et al. PIV measurement of particle motion in spiral gas-solid two-phase flow[J]. Experimental Thermal and Fluid Science, 1999, 19(4): 194-203.
  • 5Horio M, Kuroki H. Three dimensional flow visualization of dilute dspersed solids in bubbling and fluidized beds[J]. ChemicalEngineering Science, 1994, 49(7): 2413-2421.
  • 6田文栋,魏小林,吴东垠,盛宏至.内旋流流化床颗粒运动的研究[J].热能动力工程,2000,15(1):9-11. 被引量:2
  • 7高翔,李兴华,刘海蛟,骆仲泱,岑可法.半干法烟气脱硫塔内速度场研究[J].能源工程,2005,25(2):26-29. 被引量:5
  • 8Vander Meer E H, Thorpe R B, Davidson J F. Dimensionless groups for practicable similarity of circulating fluidized beds[J]. Chemical Engineering Science, 1999, 54(22): 5369-5376.
  • 9Vander Meer E H. Riser exits and sealing of circulating fluidised beds[D]. Cambridge, U K: University of Cambridge, 1997.
  • 10Horio M, Ishii H, Kobu Kai Y, et al. A scaling law for circulating fluidized beds[J]. Journal of chemical Engineering of Japan, 1989, 22(6): 587-592.

二级参考文献90

共引文献140

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部