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Operating the activated sludge process to decrease cell yield without increasing oxygen consumption.

机译:操作活性污泥工艺可降低电池产量而不增加氧气消耗。

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摘要

The objective of this study was to demonstrate that cell yield in activated sludge processes can be decreased without increasing oxygen consumption by applying operating conditions that encourage "futile cycling". During futile cycling, compounds are synthesized and catabolized by the microbial culture without a corresponding change in cell mass.;In this study, laboratory-scale activated sludge reactors were used and operated as sequencing batch processes. As part of the experimental program conducted, the performance of these reactors were monitored as their operation was changed from normal to intermittent operating conditions. Under normal operation, the reactors were fed once and aerated uniformly during the react step. Under intermittent operation, the reactors were either fed or aerated intermittently during the react step to induce "futile cycling".;During intermittent feeding, cell yield decreased by 24 percent and oxygen consumption decreased by 18 percent, on the average. During intermittent aeration, cell yield decreased by 23 percent and oxygen consumption increased by 4 percent, on the average.;Intermittent feeding and intermittent aeration operating schemes may be applied to full-scale systems using sequencing batch operation or to continuous-flow processes using a modified configuration of tapered aeration, step aeration, or contact stabilization. The results anticipated are reductions in both cell yield and oxygen consumption greater than were demonstrated using laboratory-scale reactors.;The two major operating expenses for an activated sludge wastewater treatment facility are associated with sludge handling and aeration. Sludge handling requirements are affected by cell yield and aeration requirements are affected by oxygen consumption, defined as the mass of oxygen consumed per mass of substrate utilized. By operating the activated sludge process such that cell yield decreases without increasing oxygen consumption, significant reductions in the operating costs for an activated sludge wastewater treatment facility may be realized.
机译:这项研究的目的是证明通过应用鼓励“无效循环”的操作条件,可以在不增加耗氧量的情况下降低活性污泥工艺中的细胞产率。在无效的循环过程中,化合物通过微生物培养进行合成和分解代谢,而细胞质量没有相应变化。在本研究中,实验室规模的活性污泥反应器被用作分批测序过程。作为进行的实验计划的一部分,随着反应堆的运行从正常运行状态变为间歇运行状态,对这些反应堆的性能进行了监控。在正常操作下,将反应器进料一次并在反应步骤中均匀充气。在间歇操作下,反应器在反应步骤中被间歇进料或充气,以引起“无效循环”。在间歇进料期间,平均电池产率降低24%,耗氧量平均降低18%。在间歇曝气期间,平均电池产量降低23%,耗氧量平均增长4%。锥形曝气,阶梯曝气或接触稳定化的改进配置。预期的结果是电池产量和耗氧量的减少均大于使用实验室规模的反应器所显示的结果。活性污泥废水处理设施的两个主要运营费用与污泥处理和曝气有关。污泥处理要求受电解池产量的影响,曝气要求受耗氧量的影响,耗氧量定义为所用底物质量所消耗的氧气量。通过操作活性污泥工艺使得细胞产率降低而不增加氧气消耗,可以实现活性污泥废水处理设备的运行成本的显着降低。

著录项

  • 作者

    Chun, Westley Kyung Choon.;

  • 作者单位

    University of California, Davis.;

  • 授予单位 University of California, Davis.;
  • 学科 Civil engineering.;Engineering Sanitary and Municipal.
  • 学位 Ph.D.
  • 年度 1988
  • 页码 113 p.
  • 总页数 113
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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