Source Jouranl of CSCD
Source Journal of Chinese Scientific and Technical Papers
Included as T2 Level in the High-Quality Science and Technology Journals in the Field of Environmental Science
Core Journal of RCCSE
Included in the CAS Content Collection
Included in the JST China
Indexed in World Journal Clout Index (WJCI) Report
Volume 41 Issue 4
Apr.  2023
Turn off MathJax
Article Contents
CHAI Tongshan, FU Yu, CHENG Huaiyu, LONG Xinping. NUMERICAL SIMULATION OF PARTICLE AGGREGATION IN GRID FLOCCULATION TANK BASED ON CFD-PBM[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(4): 40-48. doi: 10.13205/j.hjgc.202304006
Citation: CHAI Tongshan, FU Yu, CHENG Huaiyu, LONG Xinping. NUMERICAL SIMULATION OF PARTICLE AGGREGATION IN GRID FLOCCULATION TANK BASED ON CFD-PBM[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(4): 40-48. doi: 10.13205/j.hjgc.202304006

NUMERICAL SIMULATION OF PARTICLE AGGREGATION IN GRID FLOCCULATION TANK BASED ON CFD-PBM

doi: 10.13205/j.hjgc.202304006
  • Received Date: 2022-03-24
    Available Online: 2023-05-26
  • Publish Date: 2023-04-01
  • In order to explore the influencing factors of particle aggregation behavior in the flocculation tank, the population balance model (PBM) was used to simulate the particle aggregation behavior in this paper. By means of CFD-PBM coupling method, the effects of initial average particle size and volume fraction of flocculated particles on particle aggregation behavior in a grid flocculation tank were studied. An index of average particle size growth rate was proposed to characterize the flocculation effect inside the flocculation tank under the CFD-PBM coupling method. The results showed that: 1) when the inlet particle volume fraction was 0.1, as the initial average particle size of flocculated particles increased from 10 μm to 76 μm, the particle size at the outlet increased from 117.54 μm to 154.82 μm, but the average particle size growth rate decreased from 1075.4% to 103.7%; 2) when the initial particle size of the inlet particles was 40 μm, as the particle volume fraction increased from 0.05 to 0.2, the particle size at the outlet position increased from 127.16 μm to 155.74 μm, and the average particle size growth rate also increased from 208.7% to 289.4%; 3) overall, within the particle volume fraction range of 0.05 to 0.1, the average particle size growth rate was the highest, and the flocculation effect improved most significantly.
  • loading
  • [1]
    伏雨,龙云,肖波,等. 栅条絮凝池内部流场及颗粒运动状态模拟分析[J]. 环境工程, 2021, 39(4): 25-29.
    [2]
    朱昭福. 微絮凝直接过滤工艺在自来水厂扩建工程中的应用[J]. 工程建设与设计, 2020(11): 237-238.
    [3]
    KHELIFA A, HILL P S. Models for effective density and settling velocity of flocs[J]. Journal of Hydraulic Research, 2006, 44(3): 390-401.
    [4]
    BIGGS C A, LANT P A. Activated sludge flocculation: on-line determination of floc size and the effect of shear[J]. Water Research, 2000, 34(9): 2542-2550.
    [5]
    COUFORT C, BOUYER D, LINÉ A, et al. Modelling of flocculation using a population balance equation[J]. Chemical Engineering & Processing Process Intensification, 2007, 46(12): 1264-1273.
    [6]
    COUFORT C, DUMAS C, BOUYER D, et al. Analysis of floc size distributions in a mixing tank[J]. Chemical Engineering & Processing Process Intensification, 2008, 47(3): 287-29410.
    [7]
    HULBURT H M, KATZ S. Some problems in particle technology: a statistical mechanical formulation[J]. Chemical Engineering Science, 1964, 19(8): 555-574.
    [8]
    MAHONEY A W, RAMKRISHNA D. Efficient solution of population balance equations with discontinuities by finite elements[J]. Chemical Engineering Science, 2002,57(7):1107-1119.
    [9]
    GERSTLAUER A, MITROVIĆ A, MOTZ S, et al. A population model for crystallization processes using two independent particle properties[J]. Chemical Engineering Science, 2001, 56(7): 2553-2565.
    [10]
    IMMANUEL C D, CORDEIRO C F, SUNDARAM S S, et al. Modeling of particle size distribution in emulsion co-polymerization: comparison with experimental data and parametric sensitivity studies[J]. Computers & Chemical Engineering, 2002, 26(7/8): 1133-1152.
    [11]
    MILLIES M, MEWES D. Interfacial area density in bubbly flow[J]. Chemical Engineering and Processing-Processing Intensification, 1999, 38(4/5/6): 307-319.
    [12]
    BIGGS C A, LANT P A. Modelling activated sludge flocculation using population balances[J]. Powder Technology, 2002, 124(3):201-211.
    [13]
    李振亮. 基于群体平衡的活性污泥絮凝动力学[D]. 重庆:重庆大学, 2014.
    [14]
    宋峻林,唐荣联,王洪. 絮凝过程CFD数值模拟研究[J]. 现代化工, 2018, 38(8): 231-235.
    [15]
    张世豪,艾恒雨,崔婉莹,等. 基于CFD模拟的絮凝效果评价指标研究[J]. 中国给水排水, 2022, 38(5): 45-53.
    [16]
    刘存,王庆涛,陈翔宇,等. 网格絮凝池结构参数对流场影响的数值模拟[J]. 水资源与水工程学报, 2018, 29(4): 162-167.
    [17]
    姚萌,冉治霖,相会强,等. 搅拌桨叶类型对絮凝池内流场特性的仿真模拟[C]//环境工程2019年全国学术年会,北京,2019.
    [18]
    GOLZARIJALAL M, ZOKAEE ASHTIANI F, DABIR B. Modeling of microalgal shear-induced flocculation and sedimentation using a coupled CFD-population balance approach[J]. Biotechnol Prog, 2018,34(1):160-174.
    [19]
    YANG N, WEN Y. Numerical simulation of secondary sedimentation tank based on population balance model[J]. IOP Conference Series Earth and Environmental Science, 2019, 358: 32052.
    [20]
    LI Z L, LU P L, ZHANG D J, et al. Simulation of floc size distribution in flocculation of activated sludge using population balance model with modified expressions for the aggregation and breakage[J]. Mathematical Problems in Engineering, 2019, 6:5243860.
    [21]
    ABRAHAMSON J. Collision rates of small particles in a vigorously turbulent fluid[J]. Chemical Engineering Science, 1975, 30(11): 1371-1379.
    [22]
    SAFFMAN P G, TURNER J S. On the collision of drops in turbulent clouds[J]. Journal of Fluid Mechanics, 1956, 1(1): 16-30.
    [23]
    HOUNSLOW M J, RYALL R L, MARSHALL V R. A discretized population balance for nucleation, growth, and aggregation[J]. Aiche Journal, 1988, 34(11):1821-1832.
    [24]
    ELDUAYEN-ECHAVE B, LIZARRALDE I, LARRAONA G S, et al. A new mass-based discretized population balance model for precipitation processes: application to struvite precipitation[J]. Water Research, 2019,155:26-41.
    [25]
    BIGGS C A, LANT P A. Modelling the effect of shear history on activated sludge flocculation[J]. Water Science and Technology, 2003, 47(11): 251-257.
  • 加载中

Catalog

    通讯作者: 陈斌, bchen63@163.com
    • 1. 

      沈阳化工大学材料科学与工程学院 沈阳 110142

    1. 本站搜索
    2. 百度学术搜索
    3. 万方数据库搜索
    4. CNKI搜索

    Article Metrics

    Article views (235) PDF downloads(10) Cited by()
    Proportional views
    Related

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return