期刊文献+

耦合流化床提升管流动结构及边壁层厚度的研究 被引量:1

Experimental Study on the Flow Structure and Wall Layer Thickness in the Riser of Coupled Fluidized Bed
下载PDF
导出
摘要 在射流流化床与提升管耦合的多段分级转化流化床冷态实验装置上,采用压力传感器和PV-6型颗粒速度测量仪,对提升管流动结构和边壁层厚度进行了系统研究。结果表明,一定的操作气速下,固体循环量增加使提升管中气固流动状态从稀相气力输送过渡到快速流态化区域。当提升管处于快速流态化区域时,一定固体循环量下,表观气速增加使提升管轴向各个位置的边壁层厚度减小;一定气速下,固体循环量增加使提升管各个截面的边壁层厚度增加,且低气速时提升管各个截面的边壁层厚度随固体循环量增加的程度明显高于高气速时。拟合得到了边壁层厚度与截面平均固体浓度的关系式,较好地预测了快速流态化区域内边壁层厚度随截面平均固体浓度的变化关系,该表达式的计算值和实验值吻合较好。 The cold flow behavior and wall layer thickness of a gas riser which couples with a multi-stage jetting fluidized bed were studied experimentally with a pressure transducer and a PV-6 optical fiber probe. The experimental results show that flow in the riser transits from the dilute pneumatic conveying state to the fast fluidization state when the circulating solid increases while keeping a constant gas velocity in the riser. At the fast fluidization state, the wall layer thickness decreases with the increase of the riser gas velocity at a constant solid circulation rate, and it increases with the increase of the solid circulation rate at a constant riser gas velocity. The increase of the wall layer thickness is more prominent at the low gas velocity region. An empirical correlation was finally developed to describe the relationship between the wall layer thickness and the solid concentration at the fast fluidization state. A favorable agreement between the predicted results and experimental data were reached.
出处 《化学反应工程与工艺》 CAS CSCD 北大核心 2012年第5期385-390,共6页 Chemical Reaction Engineering and Technology
基金 中国科学院战略性先导科技专项(XDA07050100)
关键词 耦合流化床 提升管 快速流态化 边壁层厚度 coupled fluidized bed riser fast fluidization wall layer thickness
  • 相关文献

参考文献17

  • 1Makkawi Y T,Wrigbt P C. Fluidization regimes in a conventional fluidizcd bed characterized by means of clcctrical capacitance tomography[J].Chemical Engineering Science,2002,(13):2411-2437.doi:10.1016/S0009-2509(02)00138-0. 被引量:1
  • 2Zhou J,Grace J R,Lim C J,ctal. Particle velocity profiles in a circulating fluidizcd bed riser of square cross-section[J].Chemical Engineering Science,1995,(02):237-244.doi:10.1016/0009-2509(94)00241-I. 被引量:1
  • 3Namkung W,Kim S D. Gas backmixing characteristics in a circulating fluidized bed[J].Powder Technology,1998,(01):70-78. 被引量:1
  • 4Horio M,Lei H W. Significance of core diameter variation in the lateral solid transfer model for the upper dilute region of circulating fluidized beds[J].Advanced Powder Technology,1998,(02):107-127. 被引量:1
  • 5Bai D,Shibuya E,Masuda Y. Distinction between upward and downward flows in circulating fluidized beds[J].Powder Technology,1995,(01):75-81. 被引量:1
  • 6Basu P,Nag P K. An investigation into heat transfer in circulating fluidized beds[J].International Journal of Heat and Mass Transfer,1987,(11):2399-2409. 被引量:1
  • 7Harris A T,Thorpe R B,Davidson J F. Characterisation of the annular film thickness in circulating fluidized-bed risers[J].Chemical Engineering Science,2002,(13):2579-2587. 被引量:1
  • 8Kim S W,Kirbas G,Bi H T. Flow structure and thickness of annular downfiow layer in a circulating fluidized bed riser[J].Powder Technology,2004,(01):48-58. 被引量:1
  • 9Werther J. Fluid mechanics of large-scale CFB units[A].American Institute of Chemical Engineers.New York,1994.1-14. 被引量:1
  • 10Bi H T,Zhou J,Qin S z. Annular wall layer thickness in circulating fluidized bed risers[J].Canadian Journal of Chemical Engineenng,1996,(05):811-814.doi:10.1002/cjce.5450740534. 被引量:1

同被引文献10

引证文献1

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