期刊文献+

Flow dynamics and contact efficiency in a novel fast-turbulent fluidized bed with ring-feeder internals 被引量:3

Flow dynamics and contact efficiency in a novel fast-turbulent fluidized bed with ring-feeder internals
原文传递
导出
摘要 The flow dynamics in a novel fast-turbulent fluidized bed (FTFB) with middle-upper expanding structure and two different ring-feeder internals (mixed and vortex ring-feeder) were studied to achieve a reduction in gasoline olefin production, Compared with a conventional circulating fluidized bed, the novel FTFB displayed unique characteristics and advantages. A higher solids holdup and more uniform solids holdup distribution existed in the diameter-expanding region, especially for the FTFB with vortex ring-feeder structure, A probability density distribution analysis indicated that the novel fluidized bed could reduce gas-solids segregation and enhance gas-solids interaction. A constant carbon dioxide tracer system was used to simulate the reactant gas distribution. The gas-solids contact efficiency was defined according to the solid dispersibility and the amount of gas covering the solid surface. Novel FTFB risers, especially those with vortex ring-feeders, have a much higher gas-solids contact efficiency than that of traditional risers. The flow dynamics in a novel fast-turbulent fluidized bed (FTFB) with middle-upper expanding structure and two different ring-feeder internals (mixed and vortex ring-feeder) were studied to achieve a reduction in gasoline olefin production, Compared with a conventional circulating fluidized bed, the novel FTFB displayed unique characteristics and advantages. A higher solids holdup and more uniform solids holdup distribution existed in the diameter-expanding region, especially for the FTFB with vortex ring-feeder structure, A probability density distribution analysis indicated that the novel fluidized bed could reduce gas-solids segregation and enhance gas-solids interaction. A constant carbon dioxide tracer system was used to simulate the reactant gas distribution. The gas-solids contact efficiency was defined according to the solid dispersibility and the amount of gas covering the solid surface. Novel FTFB risers, especially those with vortex ring-feeders, have a much higher gas-solids contact efficiency than that of traditional risers.
出处 《Particuology》 SCIE EI CAS CSCD 2015年第4期203-211,共9页 颗粒学报(英文版)
基金 the financial support of the CNPC in the National Program on Key Basic Research Project(973 Program) of China(No.2012CB215000)
关键词 Flow dynamics Fast-turbulent fluidized bed Ring-feeder internal Carbon dioxide tracer Gas-solids contact efficiency Flow dynamics Fast-turbulent fluidized bed Ring-feeder internal Carbon dioxide tracer Gas-solids contact efficiency
  • 相关文献

参考文献3

二级参考文献17

  • 1祝京旭,魏飞,杨勇林.气固下行流化床反应器 Ⅰ 下行管反应器的发展及其应用[J].化学反应工程与工艺,1996,12(2):214-224. 被引量:15
  • 2赖周平.重油催化裂化进料高效雾化喷嘴[J].石油化工设备技术,1996,17(5):15-18. 被引量:10
  • 3甘宁俊,蒋大洲,白丁荣,金涌,俞芷青.内置钝体对快速流化床中颗粒浓度分布的影响[J].高校化学工程学报,1990,4(3):273-277. 被引量:15
  • 4黄哲.-[J].化工机械,1985,12(6):8-8.
  • 5Chen Bing-yu, Fang Guo-ping, Yang Chen-yan. Experimental investigation of the entrance structure for the reactor with G/S co-current downflow [J]. Chemical Metallurgy, 1992, 13(1): 44-50.
  • 6WEI Fei, LIU Jin-zhong, YONG Jin, YU Zhi-qing. Hydrodynamics and mixing behavior in the entrance region of a downer [A].in Mooson Kwauk, LI Jing-hai, eds. Circulating Fluidized Bed Technology V [C]. Bcijing: Science Press, 1996, 122-127.
  • 7刘金忠,学位论文,1992年
  • 8陆坊斌,学位论文,1991年
  • 9黄哲,化工机械,1985年,12卷,6期,8页
  • 10许友好等.一种制取异丁烷和富含异构烷烃汽油的催化转化方法.中国,CN1232069A.1999

共引文献221

同被引文献40

引证文献3

二级引证文献21

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