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锥形流化床混凝装置内混凝指标和絮凝体分形维数

Flocculation parameter and fractal dimension model in a conical fluidized bed

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【作者】 王婷周丹丹董双石郑文宇杨毅

【Author】 WANG Ting1,2,ZHOU Dandan1,DONG Shuangshi1,ZHENG Wenyu3,YANG Yi1(1College of Environment and Resource,Jilin University,Changchun 130026,Jilin,China;2College of Environmental Science and Technology,Shanghai 200092,China;3China Northeast Municipal Engineering Design and Research Institute,Changchun 130021,Jilin,China)

【机构】 吉林大学环境与资源学院同济大学环境科学与工程学院中国市政工程东北设计研究院

【摘要】 利用锥形流化床混凝工艺中固相颗粒的流化运动在液相中形成的微涡流,使液相中的胶体颗粒碰撞和聚集,形成絮体。结果表明在论文研究范围内,高岭土悬浊液去除率(23.97%~85.37%)随GT(1836.51~5399.53)增加而提高。G值的减小(169.2~189.7s-1)和混凝时间增加都会引起混凝效率的升高。采用分形维数模型计算得到,相同运行条件下形成絮体的分形维数相关系数均在0.9以上,表明絮体性质具有相似性,因此相同操作条件下絮体自由沉降速度区间分布狭窄,相同沉速的颗粒数量百分比峰值达45%。

【Abstract】 Micro-vortex in liquid phase of conical fluidized-bed flocculation reactor,caused by fluidizing solid particles,was utilized to make colloids collision and aggregation,which results in the formation of flocs.When the value of GT increased from 1836.51 to 5399.53,the removal fraction (RF) of kaolin clay suspension increased from 23.97% to 85.37%.Also,The RF increased with the decreasing of G and the increasing of T,when G was within 169.2—189.7 s-1.According to the Fractal Dimension model,the correlation coefficient of flocs was above 0.9 at the similar operation conditions of reactor.This indicated the similarity of the flocs properties,which led to a narrow distribution of free falling velocity,and the maximum value of amount of flocs particles with the same falling velocity was up to 45%.

【基金】 国家自然科学基金项目(50908096, 50908097);高等学校博士学科点专项科研基金(20090061120035);吉林大学基本科研业务费项目(200903155);长春市科技计划项目(09SF08)~~
  • 【分类号】TQ028
  • 【被引频次】5
  • 【下载频次】211
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