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Fluidization of fine particles and its optimal operation condition in multimedia water filter

机译:多媒体水过滤器中细颗粒的流化及其最佳运行条件

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摘要

Approach: Backwashing process was implemented using column of deep bed filter with different media characteristics to provide optimal operation condition. Minimum velocity of fluidization (V_(mf)) and porosity at minimum fluidization (e_(mf)) were investigated under different operation condition and grains size. The results were compared with Wen and Yu equation and Richardson-Zaki correlation, respectively. Backwashing model was developed to predict the effect of fluid shear strength (τ_a), velocity grade (G), dissipation rate coefficient (C_a), and parameters of random motion (C_a~(0.5)/Re) on the energy dissipation rate during fluidization process. Results: The simulated result of proposed models gives a good convergence to observed data. It was seen that a smaller size of sand media need a lower value of backwash velocity than a higher size for lifting filter media. Fixed bed porosity increased from 0.510 to 0.704 at bigger size of sand media (1.18 mm), while it increased to 0.680 at smaller size of sand media (0.5 mm). The simulated result showed that Richardson-Zaki model has a good convergence with experimental result of expanded porosity for all effective size of sand media. Conclusion: It was concluded that low superficial velocity produced through the system at higher velocity grade (G). In addition to that the fluid shear strength (τ_a) increased along with expanded porosity. The maximum fluid shear strength (τ_a) was occurred at porosity equal to 0.730 and in large effective size of sand media (1.18 mm). Also, the lighter particles caused a high increasing rate in the random motion parameters compared with heavier particles. The study showed that the effluent suspended solid and hydrodynamics detachment of deposited fine particles reduces with time of fluidization but it rises with backwash discharge. The bigger grain of sand media has a lower peak point of optimum backwash time than smaller grain due to accumulation a large amount of deposit fine particles. The study was shown that the energy dissipation rate and the velocity grade have a dominant mechanism in filter backwashing and increases with increasing particle population in a expanded bed. The result revealed that the random motion parameter increased along with increasing in fraction solids and a higher rate was appeared in the lighter particles that it caused increasing in random motion parameter compared with heavier particles.
机译:方法:采用具有不同介质特性的深层过滤器柱实施反冲洗过程,以提供最佳的操作条件。研究了不同操作条件和晶粒尺寸下的最小流化速度(V_(mf))和最小流化时的孔隙率(e_(mf))。将结果分别与Wen和Yu方程以及Richardson-Zaki相关进行了比较。建立了反洗模型以预测流体抗剪强度(τ_a),速度等级(G),耗散率系数(C_a)和随机运动参数(C_a〜(0.5)/ Re)对流化过程中耗能率的影响处理。结果:所提出模型的仿真结果使观测数据具有很好的收敛性。可以看出,与提升过滤器介质所需的较大尺寸相比,较小尺寸的沙质介质需要较低的反冲洗速度值。在较大尺寸砂介质(1.18 mm)下,固定床孔隙率从0.510增加到0.704,而在较小尺寸砂介质(0.5 mm)下,固定床孔隙率增加到0.680。模拟结果表明,对于所有有效尺寸的砂土,Richardson-Zaki模型与孔隙率扩展的实验结果具有良好的收敛性。结论:结论是在较高的速度等级(G)下,通过系统产生的表观速度较低。除此之外,流体的剪切强度(τ_a)随着孔隙率的增加而增加。最大流体抗剪强度(τ_a)发生在孔隙度等于0.730且砂土有效尺寸较大(1.18 mm)的情况下。而且,较轻的颗粒与较重的颗粒相比导致随机运动参数的增加率很高。研究表明,流出的悬浮固体和沉积的细颗粒的水动力分离随流化时间的增加而减少,但随着反洗排放的增加而增加。由于积累了大量的沉积细颗粒,较大的砂介质颗粒的最佳反冲洗时间峰值比较小的颗粒要小。研究表明,能量耗散率和速度等级是过滤器反冲洗的主要机制,并随着膨胀床中颗粒数量的增加而增加。结果表明,随分数固体的增加,随机运动参数增加,较轻的颗粒出现较高的速率,这导致与较重的颗粒相比,随机运动参数增加。

著录项

  • 来源
    《Desalination and water treatment》 |2013年第24期|4768-4778|共11页
  • 作者单位

    School of Energy and Environment, Southeast University, Sipailou Road, Nanjing 210096, PR China,College of Engineering, Departments of Civil Engineering and Chemical Engineering, University of Basrah, Basra, Iraq;

    School of Energy and Environment, Southeast University, Sipailou Road, Nanjing 210096, PR China,College of Engineering, Departments of Civil Engineering and Chemical Engineering, University of Basrah, Basra, Iraq;

    School of Energy and Environment, Southeast University, Sipailou Road, Nanjing 210096, PR China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Fluidization; Fine particle; Media; Water filter; Expanded bed;

    机译:流化;细颗粒;媒体;净水器;扩充床;

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