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Biological wastewater treatment using inverse, upflow and horizontal moving bed biofilters.

机译:使用逆流,上流和水平移动床生物滤池的生物废水处理。

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摘要

This study investigated the hydrodynamic characteristics and nitrification features of three types of biofilters: down-flow, upflow and horizontal moving bed biofilters. Measurements were taken in pilot-scale systems and in biofilters operating at salmon smolt hatcheries in St. George and Oak Bay, New Brunswick. Key variables that affect the performance of biofilters, such as bed expansion and residence time distribution (RTD), were studied. New models are proposed to predict the bed expansion and RTD of biofilters. They were validated using data reported in the literature and experimental results generated in this work. A pressure profile method is also proposed to determine the distributions of bioparticle size and density within fluidized sand biofilters. The bioparticle sizes calculated using this method are in good agreement with the measured values. It is shown that biofilm thickness is zero near the distributor plate and approaches a maximum value as height increases.;The horizontal moving bed biofilter was found to behave as a well-mixed system whereas the fluidized sand and down-flow biofilters behaved as plug flow systems. At the operating temperature of the hatcheries (11-14°C), the rate of nitrification was first order with respect to the TAN concentration in all three biofilters. The nitrification rate constant based on bed volume was 0.0020 s-1 and 0.0026 s-1 in the fluidized sand and Kaldnes media biofilters, respectively. Compared to the fluidized sand and down-flow biofilters, the horizontal moving bed biofilter has the extra advantages of reducing CO2 concentration, keeping a high oxygen level in the effluent and having a low pressure drop.
机译:这项研究调查了三种类型的生物滤池的水动力特性和硝化特性:下流式,上流式和水平移动床生物滤池。测量是在新不伦瑞克省圣乔治和橡树湾鲑鱼孵化场的中试规模系统和生物滤池中进行的。研究了影响生物滤池性能的关键变量,例如床膨胀和停留时间分布(RTD)。提出了新的模型来预测生物滤池的床膨胀和RTD。使用文献中报告的数据和这项工作中产生的实验结果对它们进行了验证。还提出了一种压力分布方法来确定流化砂生物滤池内生物颗粒大小和密度的分布。使用该方法计算出的生物颗粒尺寸与测量值高度吻合。结果表明,分布板附近的生物膜厚度为零,并随着高度的增加而接近最大值。;发现水平移动床生物滤池表现为良好混合的系统,而流化砂和下流式生物滤池表现为活塞流。系统。在孵化场的操作温度(11-14°C)下,相对于所有三个生物滤池中的TAN浓度,硝化率是一阶的。在流化砂和Kaldnes介质生物滤池中,基于床体积的硝化速率常数分别为0.0020 s-1和0.0026 s-1。与流化砂和下流式生物滤池相比,卧式移动床生物滤池具有降低CO2浓度,保持废水中高氧含量和低压降的额外优势。

著录项

  • 作者

    Ma, Zhijie.;

  • 作者单位

    University of New Brunswick (Canada).;

  • 授予单位 University of New Brunswick (Canada).;
  • 学科 Engineering Chemical.;Engineering Environmental.;Engineering Sanitary and Municipal.
  • 学位 M.Sc.E.
  • 年度 2005
  • 页码 210 p.
  • 总页数 210
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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