Simulation and analysis on gas flow distribution in radial flow air adsorber

被引:0
|
作者
Tang Z. [1 ,2 ]
Xu M. [1 ,2 ]
Zhang J. [1 ,2 ]
机构
[1] School of Chemical Engineering and Technology, Tianjin University, Tianjin
[2] State Key Laboratory of Chemical Engineering(Tianjin University), Tianjin
来源
Tang, Zhongli (zltang@tju.edu.cn) | 1600年 / Tianjin University卷 / 49期
关键词
Air separation; CFD simulation; Gas flow distribution; Radial flow; Structure optimization;
D O I
10.11784/tdxbz201410080
中图分类号
学科分类号
摘要
Gas flow distribution and its influence factors in a eighty thousand tons adsorber have been investigated by computational fluid dynamics (CFD). It is found that the axial uniformity of the flow distribution can be maximized when the cross-sectional area ratio of the center pipe to the annular channel reaches a certain value in adsorption process and desorption process. The uniformity in the two layers can both be improved by lowering the porosity of molecular sieve layer. In addition, a cone distributor can cause a little decrease of the uniformity in adsorption process, but can cause a relatively large increase in desorption process. An optimal solution is proposed as follows: Adjusting the porosity of the inner molecular sieve layer and the alumina layer to 0.33 and 0.35, respectively; Adding a cone distributor, the uniformity in the two layers can be improved with a slight increase of the pressure drop in both adsorption and desorption processes. © 2016, Editorial Board of Journal of Tianjin University(Science and Technology). All right reserved.
引用
收藏
页码:305 / 313
页数:8
相关论文
共 13 条
  • [1] Lu J., Zhang X., Qiu L., Et al., Theoretical analysis of uniform flow distribution in vertical radical adsorption bed, CIESC Journal, 63, pp. 21-25, (2012)
  • [2] Lobanov E.L., Skipin Y.A., Increasing the operating efficiency of radial reactors in reforming, Chemistry and Technology of Fuels and Oils, 22, 6, pp. 275-278, (1981)
  • [3] Suter D., Bartroli A., Schneider F., Et al., Radial flow reactor optimization for highly exothermic selective oxidation reactions, Chemical Engineering Science, 45, 8, pp. 2169-2176, (1990)
  • [4] Song X., Wang Z., Jin Y., Et al., The research of the fluid mechanics behavior of the moving bed radial reactor, CIESC Journal, 43, 3, pp. 268-274, (1992)
  • [5] Heggs P.J., Ellis D.I., Ismail M.S., The modeling of fluidflow distributions and pressure changes in multi-layered annular packed beds, Gas Separation and Purification, 8, 4, pp. 257-264, (1994)
  • [6] Heggs P.J., Ellis D.I., Ismail M.S., Prediction of flow distributions and pressure changes in multi-layered annular packed beds, Gas Separation and Purification, 9, 4, pp. 243-252, (1995)
  • [7] Kareeri A.A., Zughbi H.D., Al-Ali H.H., Simulation of flow distribution in radial flow reactors, Industrial and Engineering Chemistry Research, 45, 8, pp. 2862-2874, (2006)
  • [8] Mu Z., Wang J., Wang T., Et al., Optimum design of radial flow moving-bed reactors based on a mathematical hydrodynamic model, Chemical Engineering and Processing: Process Intensification, 42, 5, pp. 409-417, (2003)
  • [9] Manjhi N., Verma N., Salem K., Et al., Simulation of 3D velocity and concentration profiles in a packed bed adsorber by lattice Boltzmann methods, Chemical Engineering Science, 61, 23, pp. 7754-7765, (2006)
  • [10] Li R., Chen C., Wu Y., Et al., Parameters for uniform distribution of stream in large-scale radial flow reactors, Chemical Engineering, 37, 10, pp. 28-31, (2009)