Analysis of Flow Structure and Calculation of Drag Coefficient for Concurrent-up Gas-Solid Flow

被引:0
作者
杨宁
王维
葛蔚
李静海
机构
[1] Chinese Academy of Sciences Beijing 100080
[2] Institute of Process Engineering
[3] Chinese Academy of Sciences
[4] China
[5] Multi-PhaseReaction Laboratory
基金
中国国家自然科学基金;
关键词
drag coefficient; two-phase flow; multi-scale; flow structure; two-fluid model;
D O I
暂无
中图分类号
O359 [多相流];
学科分类号
080704 ;
摘要
This study investigates the heterogeneous structure and its influence on drag coefficient for concurrent-up gas-solid flow. The energy-minimization multi-scale (EMMS) model is modified to simulate the variation of structure parameters with solids concentration, showing the tendency for particles to aggregate to form clusters and for fluid to pass around clusters. The global drag coefficient is resolved into that for the dense phase, for the dilute phase and for the so-called inter-phase, all of which can be obtained from their respective phase-specific structure parameters. The computational results show that the drag coefficients of the different phases are quite different, and the global drag coefficient calculated from the EMMS approach is much lower than that from the correlation of Wen and Yu. The simulation results demonstrate that the EMMS approach can well describe the heterogeneous flow structure, and is very promising for incorporation into the two-fluid model or the discrete particle model as
引用
收藏
页码:83 / 88
页数:6
相关论文
共 9 条
  • [1] Experimental Study on Gas-Solid Mass Transfer in Circulating Fluidized Beds[J]. 王琳娜 ,张苓 ,靳东杰 ,李静海.Chinese Journal of Chemical Engineering. 2002(01)
  • [2] An Experimental Investigation on Solid Acceleration Length in the Riser of a Long Circulating Fluidized Bed[J]. 黄卫星 ,祝京旭.Chinese Journal of Chemical Engineering. 2001(01)
  • [3] Compromise and resolution — Exploring the multi-scale nature of gas–solid fluidization[J] . Jinghai Li.Powder Technology . 2000 (1)
  • [4] Discrete simulations of heterogeneous structure and dynamic behavior in gas–solid fluidization[J] . Jie Ouyang,Jinghai Li.Chemical Engineering Science . 1999 (22)
  • [5] The EMMS model — its application, development and updated concepts[J] . Jinghai Li,Congli Cheng,Zhongdong Zhang,Jie Yuan,Anton Nemet,Franz N. Fett.Chemical Engineering Science . 1999 (22)
  • [6] Dissipative structure in concurrent-up gas–solid flow[J] . Jinghai Li,Lixiong Wen,Wei Ge,Heping Cui,Jingqiang Ren.Chemical Engineering Science . 1998 (19)
  • [7] Numerical simulation of the gas-solid flow in a fluidized bed by combining discrete particle method with computational fluid dynamics
    Xu, BH
    Yu, AB
    [J]. CHEMICAL ENGINEERING SCIENCE, 1997, 52 (16) : 2785 - 2809
  • [8] Particle-Fluid Two-Phase Flow: The Energy-Minimization Multi-Scale Method. Li J H, Kwauk M. Metallurgical Industry Press . 1994
  • [9] Mechanics of fluidization. Wen CY, Yu YH. Chemical Engineer London . 1966