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旋流沉砂池除砂废水流场与结构参数优化模拟 被引量:13

NUMERICAL SIMULATION OF FLOW FIELD AND OPTIMIZATION OF STRUCTURE PARAMETERS OF VORTEX GRIT CHAMBER FOR SANDSTONE WASTEWATER TREATMENT
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摘要 在旋流沉砂池砂石废水处理中,具有复杂流态的高浓度固液两相流问题一直是难以攻克的难题,给工程设计与运行带来很大困难。该文采用分子动理学方法从固液两相流相互作用的微观特性出发,得出合理描述旋流沉砂池内高浓度下颗粒间碰撞项的Eulerian-Eulerian两相流模型。采用滑移网格技术实现了旋流沉砂池桨叶转动区域的模拟。结合西南某水电工程砂石废水处理中的旋流沉砂池流场进行了模拟,并讨论了搅拌桨转速、桨叶位置、叶片数量和叶片角度对旋流沉砂池内水相、颗粒相的影响。结果表明:该水电站砂石处理系统旋流沉砂池的最佳桨叶结构和运行工况为:桨叶转速r=105rap/min,桨叶位置z=592mm,叶片数量为4片,叶片角度为45°。 The problem of high concentration solid-liquid two-phase flow is difficult to overcome because the flow is complex in the vortex grit chamber. It leads to poor engineering design and operation. Eulerian - Eulerian solid-liquid two-phase flow model with the consideration of collision between particles is presented in this paper. The model is gained from the perspective of microscopic interaction between liquid and solid through the molecular kinetic theory and the computational fluid dynamics. Sliding mesh technology is used to simulate the vortex grit chamber in a hydropower sandstone wastewater treatment, Southwest China. The influences of the four factors including rotate speed, distance between the propeller and the base, number of propeller blades and angle of the propeller on the efficiency of the grit removal efficiency are studied. According to the single factor test, the optimal condition for the novel vortex grit chamber is that, the rotate speed of propeller is 105 rap/min, the distance between the propeller and the base is 592mm, the number of propeller blades is 4 and the angle of the propeller is 45°.
出处 《工程力学》 EI CSCD 北大核心 2012年第6期300-307,共8页 Engineering Mechanics
基金 国家自然科学基金项目(50879053) 国家自然科学基金创新研究群体科学基金项目(51021004)
关键词 旋流沉砂池 Eulerian-Eulerian两相流 高浓度砂石废水 滑移网格 水电工程 vortex grit chamber Eulerian-Eulerian two-phase flow high concentration sandstone wastewater sliding mesh hydroelectric engineering
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参考文献18

  • 1Keller R J. Hydraulics of grit chamber (Lecture)[R]. Introduction to Wastewater System Design and Practice, 2001.
  • 2Bache J C. Vortex grit trap for separating grit from sewage flow comprises tank having grit separation and collection zones, and divider having skirt with perforations to generate air bubbles and impeller to generate rotational flow in separation zone[P]. WO2005035093-A1, 2003-10-09.
  • 3Kaibara K. Precipitator used for sedimentation of suspended solids wastewater, has rotary blade provided between deposition region of suspended solid, and natural-water introducing portion, and produces rotational flow of natural water[P]. JP2009082959-A, 2007-09-28.
  • 4Weis F G, Davis R, Weis F. Grit removal unit for waste system e.g. municipal wastewater system, comprises a grit size restrictor including a shear having a plate, and two sets of bars arranged at specific locations[P]. US2008105604-A1, 2006-11-06.
  • 5徐文刚,胡春萍.旋流沉砂池的排砂系统设计[J].中国给水排水,2002,18(1):74-75. 被引量:6
  • 6李涛.沉砂池的设计及不同池型的选择[J].中国给水排水,2001,17(9):37-42. 被引量:34
  • 7包宏明. 旋流沉砂池工艺及设备[C]. 中国水污染防治 技术设备论文集, 2003: 295-301.
  • 8汪家权,蒋文韬,王淦.新型高效旋流沉砂池除砂效果研究[J].中国给水排水,2007,23(15):98-100. 被引量:18
  • 9邱峰,汪家权,王淦.新型旋流沉砂池除砂和有机物分离效率的研究[J].工业用水与废水,2008,39(3):84-87. 被引量:7
  • 10唐学林,徐宇,吴玉林.高浓度固-液两相流紊流的动理学模型[J].力学学报,2002,34(6):956-962. 被引量:13

二级参考文献24

  • 1龙干,颜振邦,赵华.旋流沉砂池在上海白龙港污水处理厂的应用[J].中国市政工程,2001(z1):26-30. 被引量:6
  • 2汪家权,蒋文韬,王淦.新型高效旋流沉砂池除砂效果研究[J].中国给水排水,2007,23(15):98-100. 被引量:18
  • 3Imam E,McCorquodale J A.Simulation of flow in rectangular clarifiers[J].Journal of Environmental Engineering,1983,109(3):713-730.
  • 4Imam E,McCorquodale J A,Bewtra J K.Numerical modeling of sedimentation tanks[J].Journal of Hydraulic Engineering,1983,109 (12):1740-1754.
  • 5Adams E W,Rodi W.Modeling flow and mixing in sedimentation tanks[J].Journal of Environmental Engineering,1990,116(7):895-913.
  • 6Lyn D A,Stamou A I,Rodi W.Density currents and shearinduced flocculation in sedimentation tanks[J].Journal of Hydraulic Engineering,1987,113 (6):849-867.
  • 7Zhou Siping,McCorquodale J A.Modeling of rectangular settling tanks[J].Journal of Hydraulic Engineering,1992,118(10):1391-1405.
  • 8Mazzolani G,Pirozzi F,d'Antonoi G.A generalized settling approach in the numerical modeling of sedimentation tanks[J].Water Science and Technology,1998,38(3):95-100.
  • 9Kim H S,Shin M S,Jang D S,et al.Study of flow characteristics in a secondary elarifier by numerical simulation and radioisotope tracer technique[J].Applied Radiation and Isotopes,2005,63(4):519-526.
  • 10Krebs P,Vischer D,Gujer W.Inlet-structure design for final clarifiers[J].Journal of Environmental Engineering,1995,121 (8):558-564.

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