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Evaluation of the Sulfate Reduction-Autotrophic Denitrification-Nitrification Integrated (SANI) Process for Saline Wastewater Treatment .

机译:硫酸盐还原-自养反硝化-硝化综合(SANI)工艺处理含盐废水的评价。

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摘要

Hong Kong has practiced seawater toilet flushing since 1950s. It saves 22% of fresh water but inevitably results in high sulfate-laden saline sewage, causing corrosion of pressure sewers and odor (mainly H2S) at sewage treatment plants. The former has been solved by applying anti-corrosion pipes and dosing with super-oxygenated liquids. However, the latter cannot be solved at low cost because there are two major odor sources: 1) primary treatment and 2) sludge treatment. At the same time, current sewage treatment plants in Hong Kong produce 1000 tonnes of dried sludge per day, which has to be incinerated in the near future since the landfill capacity will be surpassed by 2017. In order to solve these problems cost-effectively as well as to maximize the benefits of the seawater toilet flushing practice, we have recently developed a novel biological nitrogen removal process for saline sewage treatment, which is named Sulfate reduction, Autotrophic denitrification and Nitrification Integrated (SANIRTM) process. The key features of this novel process include: elimination of primary treatment and sludge production as well as oxygen demand in organic matter removal. This novel process uses sulfate in the saline sewage originating from seawater toilet flusing to realize biological sulfate reduction (BSR) for effective removal of organic matter under an anaerobic condition. The produced sulfide dissolved completely due to production of sufficient alkalinity, providing adequate electron donors for subsequent autotrophic denitrification. Since all the three major biomasses, sulfate-reducing bacteria (SRB), autotrophs for denitrification and nitrification produce little sludge, total sludge production can thus be minimized significantly. A 500-day lab-scale system has demonstrated that no purposeful withdrawal of excess sludge was needed. In order to verify these results and further understand this feature, a steady-state model was developed in this research based on the mass balances of chemical oxygen demand (COD), nitrogen, sulfur and charge and the stoichiometries of the sulfate reduction, autotrophic denitrification and nitrification. The model predictions agreed well with the measured data on COD, nitrate and sulfate removals, sulfide production, effluent Total Suspended Solids (TSS) as well as the mass balances of COD, sulfur and nitrogen in the system. The model also well explained the performance of the SANIRTM lab-scale system in the sludge production and the COD and nitrogen removals under various operating conditions.;In order to further demonstrate the SANIRTM process in treating real saline sewage, a pilot-scale study was conducted with 10 m3/day of 6-mm screened saline sewage at the Tung Chung Sewage Pumping Station. The SANIRTM pilot plant consisted of a sulfate reduction up-flow sludge bed (SRUSB), an anoxic bioreactor for autotrophic denitrification and an aerobic bioreactor for nitrification. The plant was operated at a steady state for 225 days, during which the average removal efficiencies of both COD and TSS were 87% and no excess sludge was purposefully withdrawn. The total nitrogen (TN) removal efficiency was found to be 55% only, which was attributed to a very high fraction (26.5%) of inert soluble organic nitrogen in the incoming sewage, which mainly originated from the wastewater of the Hong Kong International Airport. Furthermore, a tracer test of the SRUSB revealed 5% shortcircuit flow and 34.6% dead zones in this key reactor of the plant, indicating a good possibility to maximize the treatment capacity of the process for full-scale saline sewage treatment through reactor design optimization. Compared with conventional biological nitrogen removal processes, the SANIRTM process eliminates 90% sludge waste, saves 35% energy and reduces 36% greenhouse gas (GHG) emission. This research work has confirmed that the SANIRTM process not only helps to eliminate the major odor sources originating from primary treatment and sludge treatment, but also promotes saline water supply as an economic and sustainable solution for water scarcity and sewage treatment in water-scarce costal areas. (Abstract shortened by UMI.)
机译:自1950年代以来,香港便开始使用海水冲厕。它可以节省22%的淡水,但不可避免地会导致富含硫酸盐的污水,导致污水处理厂的下水道腐蚀和产生异味(主要是H2S)。前者已通过使用防腐蚀管并添加超氧液体解决了。但是,由于存在两种主要的气味来源,因此不能以低成本解决后者:1)初级处理和2)污泥处理。同时,香港目前的污水处理厂每天生产1000吨干污泥,由于在2017年之前将超过垃圾填埋量,因此必须在不久的将来进行焚化。为了经济有效地解决这些问题,为了最大程度地利用海水抽水马桶冲洗的好处,我们最近开发了一种新的生物脱氮工艺,用于盐类污水处理,称为硫酸盐还原,自养反硝化和硝化一体化(SANIRTM)工艺。这种新颖工艺的关键特征包括:消除了初级处理和污泥的产生,以及去除有机物中的氧气需求。这种新颖的方法在源自海水抽水马桶融化的盐水中使用硫酸盐来实现生物硫酸盐还原(BSR),以在厌氧条件下有效去除有机物。产生的硫化物由于产生足够的碱而完全溶解,从而为随后的自养反硝化提供了足够的电子供体。由于所有三种主要生物质,还原硫酸盐细菌(SRB),用于反硝化和硝化的自养生物几乎不产生污泥,因此可以将污泥的总产量降至最低。一个500天的实验室规模的系统表明,不需要有目的地抽取多余的污泥。为了验证这些结果并进一步理解此功能,本研究基于化学需氧量(COD),氮,硫和电荷的质量平衡以及硫酸盐还原,自养反硝化的化学计量比建立了稳态模型和硝化作用。该模型预测与COD,硝酸盐和硫酸盐去除量,硫化物产量,废水总悬浮固体(TSS)以及系统中COD,硫和氮的质量平衡的测量数据非常吻合。该模型还很好地解释了SANIRTM实验室规模系统在各种操作条件下的污泥生产以及COD和氮去除的性能。为了进一步展示SANIRTM工艺处理实际含盐污水的过程,我们进行了中试规模的研究。在东涌污水泵站每天进行10立方米6毫米筛分的盐水污水处理。 SANIRTM中试装置由硫酸盐还原上流污泥床(SRUSB),用于自养反硝化的缺氧生物反应器和用于硝化的好氧生物反应器组成。该设备在稳定状态下运行225天,在此期间,COD和TSS的平均去除效率均为87%,并且没有有目的地清除过量的污泥。发现总氮(TN)去除效率仅为55%,这归因于进来的污水中有很高比例的惰性可溶有机氮(26.5%),其主要来自香港国际机场的废水。此外,SRUSB的示踪剂测试显示该工厂的关键反应器中有5%的短路流和34.6%的死区,这表明通过优化反应器设计可以最大程度地最大化该工艺的处理能力,以进行大规模盐水处理。与传统的生物脱氮工艺相比,SANIRTM工艺可消除90%的污泥废物,节省35%的能源,并减少36%的温室气体(GHG)排放。这项研究工作已经证实,SANIRTM工艺不仅有助于消除源自初级处理和污泥处理的主要臭味源,而且还可以促进盐水供应,作为缺水沿海地区缺水和污水处理的经济且可持续的解决方案。 (摘要由UMI缩短。)

著录项

  • 作者

    Lu, Hui.;

  • 作者单位

    Hong Kong University of Science and Technology (Hong Kong).;

  • 授予单位 Hong Kong University of Science and Technology (Hong Kong).;
  • 学科 Engineering Civil.;Engineering Sanitary and Municipal.
  • 学位 Ph.D.
  • 年度 2011
  • 页码 209 p.
  • 总页数 209
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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