循环流化床提升管内气固流动不仅受操作工况的影响,还与出口结构密切相关.本文应用双流体模型结合EMMS曳力模型,对T型突变出口提升管内两种工况的气固流动进行了二维模拟.模拟得到的轴向固体浓度分布和实验值符合较好.验证了EMMS曳力模型对于快速流态化气固不均匀流动模拟的适用性.
参考文献
[1] | Mabrouk R;Chaouki J;Guy C .Exit Effect on Hydrodynamics of the Internal Circulating Fluidized Bed Riser[J].Powder Technology,2007,182(03):406-414. |
[2] | Senior R C;Brereton C .Modelling of Circulating Fluidized-Bed Solids Flow and Distribution[J].Chemical Engineering Science,1992,47(02):281 296. |
[3] | Wilde J D;Guy B M;Geraldine J et al.The Effects of Abrupt T-Outlets in a Riser:3D Simulation Using the Kinetic Theory of Granular Flow[J].Chemical Engineering Science,58(3-6):877-885. |
[4] | Qi HY;Li F;Xi B;You CF .Modeling of drag with the Eulerian approach and EMMS theory for heterogeneous dense gas-solid two-phase flow[J].Chemical Engineering Science,2007(6):1670-1681. |
[5] | Wang JW;Ge W;Li JH .Eulerian simulation of heterogeneous gas-solid flows in CFB risers: EMMS-based sub-grid scale model with a revised cluster description[J].Chemical Engineering Science,2008(6):1553-1571. |
[6] | Enwald H;Peirano E;Almstedt A E .Eulerian Two-Phase Flow Theory Applied to Fluidization[J].International Journal of Multiphase Flow,1996,22(Supp 1):21-66. |
上一张
下一张
上一张
下一张
计量
- 下载量()
- 访问量()
文章评分
- 您的评分:
-
10%
-
20%
-
30%
-
40%
-
50%