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首页> 外文期刊>Environmental Science: Water Research & Technology >Opportunities for rotating belt filters in novel wastewater treatment plant configurations
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Opportunities for rotating belt filters in novel wastewater treatment plant configurations

机译:新型废水处理厂配置中旋转带式过滤器的机会

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Novel wastewater treatment plants (WWTPs), which are based on a partial nitritation-anammox (PN-anammox) process, enable higher chemical oxygen demand (COD) recovery to produce biogas and lower treatment costs. In this study, rotating belt filters (RBFs) were examined in different configurations to identify the opportunities for RBFs to be included in novel WWTP configurations. RBFs enable recovery of 22-37% of the influent COD and removal of 34-56% of hydrophobic organic micropollutants (OMPs). However, the effluent was not suitable for treatment in a PN-anammox process due to its high COD. Chemically enhanced settling (CES) enabled these limitations to be overcome and caused an increase in OMP removal to 73-94%. However, a dose of 300 mg L-1 of ferric chloride was required to produce a suitable effluent for a PN-anammox reactor. The combination of RBFs and CES not only produced effluents suitable for treatment in PN-anammox units but also decreased the alkalinity consumption and the required chemical dose 3-fold to achieve comparable COD recovery and OMP removal. The methane yield of the combined sludges that were produced (184 L(N) CH4 per kg CODinfluent) was 75% higher than that obtained from a conventional wastewater treatment (105 L(N) CH4 per kg CODinfluent), and the electricity requirements decreased from 0.54 to 0.41 kWh m(-3) of treated wastewater. The energetic calculations showed that a WWTP incorporating this combined treatment could attain energy autarky with 29% lower operational costs than that of a conventional treatment (0.022 vs. 0.031 (sic) m(-3)) as long as a minimum alkalinity-to-ammonium ratio of 1-1.25 g IC to g NH4+-N was ensured in the effluent of the combined treatment.
机译:基于部分硝化-厌氧氨(PN-anammox)工艺的新型废水处理厂(WWTP),能够提高化学需氧量(COD)的回收率以生产沼气,并降低处理成本。在这项研究中,以不同的配置检查了旋转带式过滤器(RBF),以确定将RBF包含在新型WWTP配置中的机会。 RBF能够回收进水COD的22-37%,并去除34-56%的疏水性有机微污染物(OMP)。但是,由于其高的COD,该废水不适用于PN-厌氧氨氧化工艺。化学增强沉降(CES)使这些限制得以克服,并使OMP去除率提高到73-94%。但是,需要300 mg L-1的氯化铁剂量才能生产出适合PN-厌氧氨氧化反应器的废水。 RBF和CES的结合不仅产生了适用于PN-厌氧氨处理装置的废水,而且将碱度消耗和所需化学剂量降低了3倍,以实现可比的COD回收率和OMP去除率。产生的混合污泥的甲烷产率(每千克COD流入量为184 L(N)CH4)比常规废水处理(每千克COD流出量为105 L(N)CH4)获得的甲烷产率高75%,电力需求降低从0.54到0.41 kWh m(-3)处理过的废水。能量计算表明,采用这种联合处理的污水处理厂可以实现能源自给自足,其运行成本比传统处理方法要低29%(0.022 vs. 0.031(sic)m(-3)),只要达到最低碱度即可。合并处理后的出水可确保1-1.25 g IC与g NH4 + -N的铵比。

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    Univ Santiago de Compostela, Dept Chem Engn, Sch Engn, E-15782 Santiago De Compostela, Spain;

    Univ Santiago de Compostela, Dept Chem Engn, Sch Engn, E-15782 Santiago De Compostela, Spain;

    Univ Santiago de Compostela, Dept Chem Engn, Sch Engn, E-15782 Santiago De Compostela, Spain;

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