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Numerical study of hydrodynamic characteristics in a moving bed biofilm reactor

机译:移动床生物膜反应器中流体动力学特性的数值研究

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摘要

The moving bed biofilm reactor (MBBR) has certain advantages, such as high wastewater treatment efficiency, low maintenance and operating costs, and simple operation. It has emerged as a valuable option for small decentralized facilities. The filling ratio, aeration mode and aeration intensity are the main factors that affect the performance of MBBRs in wastewater treatment. However, the information that concerns the used criteria that pertain to the process design for the MBBR is not adequate. In this study, a three dimensional computational fluid dynamics (CFD) model was constructed and the maximum error was only 1.98%, which was much smaller than the traditional 2D-CFD model. The filling ratio, aeration mode and aeration intensity of MBBR were optimized by CFD model from the point of view of fluid mechanics. The results show that the fluidization performance of the filling is the best under the one-side aeration mode with 30% filling ratio. The cost-performance ratio of the reactor with 30% filling ratio was 1.53, 25% and 35% filling ratio were only 1.17 and 1.14 respectively. Increasing the aeration intensity could improve the fluidization performance. However, the effect of high aeration intensity on the fluidization performance of the carrier was limited and the energy consumption increased greatly. The results revealed that when the aeration intensity increased from 0.07 min~(-1) to 0.13 min~(-1), the proportion of the carrier area increased by 16.56%. The proportion of the carrier area with an aeration rate of 0.20 min~(-1) was only 4.23%, which is higher than 0.13 min~(-1). The main factors that control the fluidization of the carrier were the range of the flow zone and the flow velocity of the liquid. Increasing the range of the flow zone could facilitate the flow of the carriers. The critical value of the flow velocity of the liquid in the flow zone was 0.04 m/s. These results could guide the optimization design of the filling ratio and the aeration conditions and provide a theoretical basis for the application of MBBR.
机译:移动床Biofilm反应器(MBBR)具有一定的优点,如高废水处理效率,维护和运营成本低,操作简单。它作为小型分散设施的有价值选择。填充率,曝气模式和通气强度是影响MBBRS在废水处理中性能的主要因素。但是,涉及与MBBR的过程设计有关的使用标准的信息并不充分。在该研究中,构建了三维计算流体动力学(CFD)模型,最大误差仅为1.98%,比传统的2D-CFD模型小得多。从流体力学的角度来看,通过CFD模型优化了MBBR的填充率,曝气模式和通气强度。结果表明,填充物的流化性能是单侧曝气模式下最好的填充率。具有30%填充率的反应器的成本性比率为1.53,25%和35%填充率仅为1.17和1.14。增加曝气强度可以提高流化性能。然而,高曝气强度对载体流化性能的影响有限,能耗大大增加。结果表明,当曝气强度从0.07分钟增加到0.13分钟〜(-1)时,载体面积的比例增加了16.56%。曝气速率为0.20分钟〜(-1)的载体区域的比例仅为4.23%,高于0.13分钟〜(-1)。控制载体流化的主要因素是流动区的范围和液体的流速。增加流动区域的范围可以促进载体的流动。流动区中液体流速的临界值为0.04米/秒。这些结果可以指导填充率和曝气条件的优化设计,并为MBBR应用提供理论依据。

著录项

  • 来源
    《Environmental research》 |2021年第3期|110614.1-110614.9|共9页
  • 作者单位

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

    School of Energy and Power Engineering Xihua University Chengdu 610039 Sichuan China;

    School of Environmental Science and Engineering Zhejiang Gongshang University Hangzhou 310012 Zhejiang China Instrumental Analysis Center of Zhejiang Gongshang University Hangzhou 310012 Zhejiang China;

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

    MBBR; CFD model; Filling ratio; Fluidized performance; Hydrodynamic characteristic;

    机译:MBBR;CFD模型;填充率;流化性能;流体动力学特征;
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