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糖用微涡流重力沉降器中的流体特征流动与颗粒絮凝沉降(英文)

Characteristic Flows of Fluid and Flocculation Settling of Particles in Micro-Vortex Settler for Sugar Mills
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摘要 介绍了一种在糖厂用于澄清无滤布吸滤机滤汁的波纹斜槽板微涡流重力沉降器.探讨了该沉降器的工作原理,分析了流体在波纹斜槽中的流动情况.在一定的简化条件下,推导了斜槽区水力学特征流动的速度分布表达式.指出对沉降固液分离产生强化作用的特征流动是直立斜槽板上的涡旋流和沿波纹斜槽轴向的二次流,涡旋流与二次流的流速都随主体流速的增大而增大,随斜槽直径的减小而增大.文中还推导出了产生涡旋流?二次流的斜槽结构条件下颗粒的沉降速度.结果表明,颗粒的沉降速度随涡旋流和二次流的加剧而提高,从而证明在新型沉降器中,形成的特征流动对颗粒沉降具有强化作用,这也为该新型沉降器的进一步改进提供了理论依据. A micro-vortex settler with corrugated inclined troughs, which has been used for the clarification of filtrate from non-cloth vacuum rotary filter in several Chinese sugar mills, is introduced in this paper. The working principle of the settler is then discussed and the flows of the fluid in the corrugated inclined troughs are analyzed. Moreover, the corresponding velocity equations of hydraulic characteristic flows are deduced with certain simplification. It is pointed out that, in the settler, the characteristic flows of the fluid that enhance the separation of floccule from the filtrate are the vortex flow on the upstanding corrugated plates and the secondary flow in the axial direction of corrugated inclined troughs, and that the velocities of both the vortex and the secondary flows increase with the increasing of main body flow velocity and with the decreasing of trough diameter. Simplified equations for the particle settling rates under such characteristic flows are deduced too. The results show that the settling rate of particles increases with the intensification of the vortex flow and the secondary flow. It can thus be concluded that the settling rate is enhanced by the characteristic flows in the settler. This may provide theoretical references for the modification of the novel settler.
出处 《华南理工大学学报(自然科学版)》 EI CAS CSCD 北大核心 2007年第10期131-136,共6页 Journal of South China University of Technology(Natural Science Edition)
基金 高等学校博士学科点专项基金项目(20050561014)~~
关键词 沉降器 涡流 二次流 颗粒絮凝 沉降速度 糖厂 settler vortex flow secondary flow particle flocculation settling rate sugar mill
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参考文献9

  • 1Burgos R,Concha F.Further development of software for the design and simulation of industrial thickeners[J].Chemical Engineering Journal,2005,111:135-144.
  • 2Kahane R,Nguyen T,Schwarz M P.CFD modelling of thickeners at Worsley Alumina Pty Ltd[J].Applied Mathematical Modelling,2002,22:281-296.
  • 3邬亦俊.迷宫斜板沉淀池设计[J].净水技术,1998,16(2):33-38. 被引量:4
  • 4周少基,郭祀远,李琳.波纹斜槽板沉降器中的旋流絮凝特性[J].华南理工大学学报(自然科学版),2007,35(4):67-71. 被引量:1
  • 5湛含辉,张晶晶,张晓琪.二次流沉降方法及装置,中国:01114484x[P].2003-07-25.
  • 6周少基,曾仪飞.一种固液分离沉降器,中国:200420065487.3[P].2005-05-18.
  • 7周少基,刘慧霞,李琳,郭祀远.新型微旋流-重力沉降器的开发及其在甘蔗糖厂的应用(英文)[J].广西大学学报(自然科学版),2006,31(3):256-261. 被引量:7
  • 8张梓雄,董曾南.粘性流体力学[M].北京:清华大学出版社,1998.
  • 9东北工学院.流动理论基础[M].北京:工业出版社,1982.

二级参考文献12

  • 1张雨虹.密封系统中冲洗液粒子的分离[J].流体工程,1993,21(6):33-38. 被引量:12
  • 2周少基,刘慧霞,李琳,郭祀远.新型微旋流-重力沉降器的开发及其在甘蔗糖厂的应用(英文)[J].广西大学学报(自然科学版),2006,31(3):256-261. 被引量:7
  • 3Pearse M J,Weir S,Adkins S J,et al.Advances in mineral flocculation[J].Minerals Engineering,2001,14(11):1505-1511.
  • 4Farrow J B,Fawell P D,Johnston R R M,et al.Recent developments in techniques and methodologies for improving thickener performance[J].Chem Eng J,2000,80:149-155.
  • 5Büger R.Phenomenological foundation and mathematical theory of sedimentation consolidation processes[J].Chemical Engineering J,2000,80:177-188.
  • 6Kahane R,Nguyen T,Sehwarz M P.CFD modelling of thickeners at worsley Alumina Pty Ltd[J].Applied Mathematical Modelling,2002,22:281-296.
  • 7湛含辉,张晶晶,张晓琪.二次流沉降方法及装置,中国:01114484x[P].2003-07-25.
  • 8周少基,曾仪飞.一种固液分离沉降器,中国:200420065487.3[P].2005-05-18.
  • 9东北工学院.两相流动理论基础[M].北京:冶金工业出版社,1982.
  • 10Adachi Y.Kinetic aspects of coagulation and flocculation[J].Advances in Colloid and Interface Science,1995(56):1-31.

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