期刊文献+

埋管流化床颗粒流动行为的数值模拟 被引量:6

Numerical study of solids behavior in fluidized bed with multi-immersed tubes
下载PDF
导出
摘要 提出区域覆盖法,实现了正交结构化网格(DEM网格)与非规则网格(Fluent网格)的快速耦合,通过减少颗粒搜索量的方法,提高计算效率;采用向量法高效、精确定位颗粒在非规则网格内的位置,进而形成基于非规则网格的CFD-DEM数值模拟平台。在宽和高分别为250mm和800mm的二维多埋管流化床内对颗粒流动行为进行了数值模拟研究。结果表明:基于区域覆盖法建立的CFD-DEM模型能够模拟具有复杂几何结构流化床内的气固流动行为;多埋管流化床内的颗粒上升流磨损埋管的迎风面,在背风面形成颗粒浓度较低的区域;而颗粒下降流对埋管的影响与上升流的影响相反;多埋管流化床内的颗粒行为可划分为颗粒上升流、颗粒下降流、颗粒循环流和无颗粒区。 The domain coverage method(DCM)was proposed to couple orthogonal structured DEM mesh with irregular Fluent mesh.DCM increased calculation efficiency by decreasing particle searching capacity for each Fluent cell.Particles were positioned in irregular Fluent cells with the vector method.The CFD-DEM platform was built based on DCM.And then solids behavior was studied in a fluidized bed 250 mm in bed width and 800mm in bed height with multi-immersed tubes.Simulation results showed that the proposed CFD-DEM model based on DCM could simulate gas-solids flow behavior in a fluidized bed with complex geometries.Particles moving upward collides with windward side of the fluidized bed and the other side formed a region with low solids fraction.Particles moving downward had an opposite effect on solids behavior comparing with particles moving upward.Solids behavior could be expressed into four regions:solids flow moving upward,solids flow moving downward,solids flow moving circularly and no solids region.
出处 《化工学报》 EI CAS CSCD 北大核心 2013年第8期2788-2793,共6页 CIESC Journal
基金 山东省自然科学基金项目(ZR2011EL042)~~
关键词 流化床 区域覆盖法 非规则网格 埋管 fluidized bed domain coverage method irregular mesh immersed tube
  • 相关文献

参考文献3

二级参考文献14

  • 1赵永志,程易,金涌.提升管与下行床颗粒团聚行为的离散颗粒模拟[J].化工学报,2007,58(1):44-53. 被引量:25
  • 2Lyczkowski R W, Folga S, Chang S L,et al. State-of-theart computation of dynamics and erosion in fluidized bed tube banks [ A ]. Proceedings of the 10^th International Conference on Fluidized Bed Combustion [ C ]. San Francisco:ASME Press, 1989. 465-478.
  • 3Ding J, Lyczkowski R W. Three-dimensional kinetic theory modeling of hydrodynamics and erosion in fluidized beds [J]. Powder Technology, 1992, 73(2): 127-138.
  • 4Li C, Zakkay V. Hydrodynamics and erosion modeling of fluidized bed combustions [ J ]. Journal of Fluids Engineering, 1994, 116(4) : 746-755.
  • 5He Y, Lu H, Sun Q, et al. Hydrodynamics of gas-solid flow around immersed tubes in bubbling fluidized beds [ J ]. Powder Technology, 2004, 145 (2) : 88-105.
  • 6Cundall P A, Strack O D L. A discrete numerical model for granular assemblies [J]. Geotechnique, 1979, 29 ( 1 ) : 47-65.
  • 7Tsuji Y, Kawaguchi T, Tanaka T. Discrete particle simulation of two dimensional fluidized bed [ J ]. Powder Technology, 1993, 77(1): 79-87.
  • 8Rong D, Mikami T, Horio M. Particle and bubble movements around tubes immersed in fluidized beds-a numerical study [ J ]. Chemical Engineering Science, 1999, 54(23) : 5737-5754.
  • 9Rong D, Horio M. Behavior of particles and bubbles around immersed tubes in a fluidized bed at high temperature and pressure: A DEM simulation [J]. International Journal of Multiphase Flow, 2001, 27( 1 ) : 89-105.
  • 10赵永志,程易.水平滚筒内二元颗粒体系径向分离模式的数值模拟研究[J].物理学报,2008,57(1):322-328. 被引量:37

共引文献6

同被引文献47

  • 1LI Hai-feng , LUO Zhi-guo , ZOU Zong-shu , SUN Jun-jie , HAN Li-hao , DI Zhan-xia ( Northeastern University , Shenyang 110004 , Liaoning , China ).Mathematical Simulation of Burden Distribution in COREX Melter Gasifier by Discrete Element Method[J].Journal of Iron and Steel Research(International),2012,19(9):36-42. 被引量:15
  • 2赵永志,程易,丁宇龙,金涌.不同入口结构下行床内气固流动及混合行为的CFD-DEM模拟[J].化工学报,2007,58(6):1396-1403. 被引量:4
  • 3赵永志,程易.沉浸管式流化床的颗粒尺度模拟[J].化学工程,2007,35(11):21-24. 被引量:4
  • 4Liu Guanqing, Li Shuiqing, Zhao Xianglong, et al.Experimental studies of particle flow dynamics in a two- dimensional spouted bed [ J ]. Chemical Engineering Science, 2008, 63(4) : 1131 - 1141.
  • 5Zhang Yong, Jin Baosheng, Zhong Wenqi. Experiment on particle mixing in flat-bottom spout-fluid bed [ J ]. Chemical Engineering and Processing: Process Intensi- fication, 2009, 48( 1 ) : 126 - 134.
  • 6Luo Kun, Yang Shiliang, Zhang Ke, et al. Particle dis- persion and circulation patterns in a 3D spouted bed with or without draft tube [ J ]. Industrial & Engineering Chemistry Research, 2013,52 (28) : 9620 - 9631.
  • 7Liu Daoyin, Chen Xiaoping, Zhou Wu, et al. Simula- tion of char and propane combustion in a fluidized bed by extending DEM-CFD approach[ J ]. Proceedings of the Combustion Institute, 2011,33(2) : 2701 -2708.
  • 8Zhao Yongzhi, Jiang Maoqiang, Liu Yanlei, et al. Par- ticle-scale simulation of the flow and heat transfer be- haviors in fluidized bed with immersed tube [ J ]. AICh[ Journal, 2009, 55(12): 3109-3124.
  • 9Wu Chunliang, BerrouA S, Nandakumar K. Three-di- mensional discrete particle model for gas-solid fluidized beds on unstructured mesh [ J]. Chemical Engineering Journal, 2009, 152 (2/3) : 514 - 529.
  • 10Zhao Xianglong, Li Shuiqing, Liu Guanqing, et al. DEM simulation of the particle dynamics in two-di- mensional spouted beds [J ]. Powder Technology, 2008, 184(2): 205-213.

引证文献6

二级引证文献15

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