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Two Stage Membrane Biofilm Reactors for Nitrification and Hydrogenotrophic Denitrification.

机译:用于硝化和氢营养反硝化的两级膜生物膜反应器。

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摘要

Membrane biofilm reactors (MBfR) utilize membrane fibers for bubble-less transfer of gas by diffusion and provide a surface for biofilm development. Nitrogen removal was attempted using MBfR in various configurations - nitrification, denitrification and consecutive nitrification and denitrification.;Effects of mineral precipitation, dissolved oxygen and temperature on hydrogenotrophic denitrification were investigated in a stand-alone denitrifying MBfR. Mineral precipitation, caused by intended pH control, caused the deterioration of denitrification performance by inhibiting the diffusion of hydrogen and nitrate. Operating reactor in various dissolved oxygen conditions showed that the denitrification performance was not affected by dissolved oxygen in MBfR. Optimum temperature of the hydrogenotrophic denitrification system was around 28°C.;Total nitrogen removal in a two-step MBfR system incorporating sequential nitrification and hydrogen-driven autotrophic denitrification was investigated in order to achieve nitrogen removal by autotrophic bacteria alone. Long-term stable operation, which proved difficult in previous studies due to excessive biofilm accumulation in autotrophic denitrification systems, was attempted by biofilm control. Average specific nitrification rate of 1.87 g N/m 2d was achieved and the performance was very stable throughout the experimental periods over 200 days. Performance of autotrophic denitrification was maintained stably throughout the experimental periods, however biofilm control by nitrogen sparging was required for process stability. The average specific denitrification rate increased from 1.50 g N/m2d to 1.92 g N/m2d with nitrogen sparging, over J90 days thus demonstrating the feasibility of stable long-term operation. Biofilm thickness was also stably maintained at an average of 270 mum by the gas sparging biofilm control. Maximum achievable nitrogen removal rate in consecutive operation turned out to be 6 g N/m2d.;According to the cost analysis of denitrifying MBfR, hydrogenotrophic denitrification can be an economical tertiary treatment option compared to conventional denitrifying filter although its economic feasibility highly depends on the cost of hydrogen gas.;Effects of loading rate and dissolved oxygen on nitrification performance were primarily investigated in a stand-alone nitrifying MBfR. Specific nitrification rate increased linearly with specific loading rate, up to the load of 3.5 g N/m2d. Beyond that load, substrate diffusion limitation inhibited further increase of specific nitrification rate. 100% oxygen utilization was achievable under limited oxygen supply condition.;Although this study was conducted in a lab-scale, the findings from this study can be a valuable stepping stone for larger scale application and open the door for system modifications in future.
机译:膜生物膜反应器(MBfR)利用膜纤维通过扩散实现气体的无气泡传输,并为生物膜显影提供了表面。尝试使用MBfR以多种配置脱氮-硝化,反硝化以及连续硝化和反硝化;;在独立的反硝化MBfR中研究了矿物沉淀,溶解氧和温度对氢营养反硝化的影响。预期的pH控制引起的矿物沉淀通过抑制氢和硝酸盐的扩散而导致反硝化性能的下降。在各种溶解氧条件下运行的反应器表明,MBfR中的溶解氧不会影响反硝化性能。氢营养型反硝化系统的最佳温度约为28°C;研究了采用连续硝化和氢驱动的自养型反硝化的两步MBfR系统中的总氮去除量,目的是仅通过自养型细菌实现氮的去除。通过生物膜控制,试图长期稳定运行,这在先前的研究中被证明是由于自养反硝化系统中生物膜积聚过多而造成的。达到1.87 g N / m 2d的平均比硝化率,并且在200天内的整个实验期间,性能非常稳定。自养型反硝化的性能在整个实验期间均保持稳定,但是需要通过氮气鼓泡控制生物膜以确保工艺稳定性。在J90天之内,平均氮气比反硝化率从1.50 g N / m2d增加到1.92 g N / m2d,从而证明了稳定长期运行的可行性。通过气体喷射生物膜控制,生物膜厚度也稳定地保持在平均270μm。连续运行的最大脱氮率达到6 g N / m2d。根据MBfR脱氮的成本分析,与常规脱氮滤池相比,氢营养脱氮可以是一种经济的三级处理方案,尽管其经济可行性在很大程度上取决于主要在独立的硝化MBfR中研究了负载率和溶解氧对硝化性能的影响。比硝化率随比负载率线性增加,最大负载量为3.5 g N / m2d。超过该负荷,底物扩散限制抑制了比硝化速率的进一步增加。在有限的氧气供应条件下,可以实现100%的氧气利用率。尽管此研究是在实验室规模进行的,但这项研究的发现可能是大规模应用的有价值的垫脚石,并为将来的系统改造打开了大门。

著录项

  • 作者

    Hwang, Jong Hyuk.;

  • 作者单位

    University of Manitoba (Canada).;

  • 授予单位 University of Manitoba (Canada).;
  • 学科 Engineering Civil.;Engineering Sanitary and Municipal.;Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2010
  • 页码 203 p.
  • 总页数 203
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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