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APPLICABILITY OF A BIOLOGICAL NITROGEN AND PHOSPHORUS REMOVAL PROCESS USED WITH IMMOBILIZED MEDIA

机译:用于固定化介质的生物氮和磷去除过程的适用性

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The strong movement towards effluent criteria for both nitrogen and phosphorus in Japan has created a need to introduce nutrient removal processes in the existing wastewater treatment plants. However, it is difficult to afford additional space for retrofitting the existing plants to the nitrogen and phosphorus removal process, because most of the treatment plants are located in densely populated areas. Therefore it is necessary to develop a new process, which can decrease the volume of reactor required as well as meet the more stringent standards for nutrients discharge. A biological nitrogen and phosphorus removal process, five-stage Bardenpho with immobilized nitrifiers, was proposed here as one of the high-end technologies in the case of more stringent discharge standards and space limitation for the treatment plant. Figure 1 shows the schematic diagram of the pilot plant. The reactor was divided into 5 parts defined as anaerobic, first anoxic, first aerobic, second anoxic and final aerobic tank respectively. The second anoxic tank was provided for additional denitrification using nitrate produced in the aerobic tank as the electron acceptor and the endogenous organic carbon as the electron donor. The final aerobic tank was used to strip residual nitrogen gas from solution and to minimize the release of phosphorus in the final clarifier. Mixed liquor from the first aerobic tank was recycled to the first anoxic tank for denitrification. PAC (poly-alum-chloride) was added to the final aerobic tank to support phosphorus removal when it was necessary. Methanol was added to the second anoxic tank in the case of insufficient carbon source. Fluidized immobilization carriers were added to nitrification reactor to keep a high concentration of nitrifying bacteria. In order to investigate the applicability of the process to the exiting municipal wastewater treatment plant, a pilot scale study was conducted. Relationships between varied operating conditions and nutrient removal performance were examined. The contribution of suspended activated sludge and immobilized carriers to the nitrification, as well as factors affecting denitrification, were investigated. Phosphorus removal capacity was evaluated with phosphorus release and uptake rates in the anaerobic and aerobic condition. Two types of carriers, bound and entrapped immobilized carriers, were used alternatively in the first aerobic tank with the purpose of decreasing reactor volumes. The main results of this study can be concluded as follows. (1) Regardless of a large concentration fluctuation in influent, the process showed a good performance in the removal of nitrogen, phosphorus and organic substances. With the application of the process, it was possible to get annually averaged water quality as follows. BOD5<3 mg/L; T-N<3.0mg/L; T-P<0.3 mg/L (2) It was observed that the nitrification activity of the immobilized carrier was insensitive to the temperature change compared with the suspended activated sludge. Due to an increased contribution of the carrier on nitrification as temperature decreased, it was possible to
机译:日本氮和磷的氮和磷的污水标准的强劲运动已经产生了在现有的废水处理厂中引入营养去除过程。然而,难以提供额外的空间,用于将现有植物改装给氮气和磷去除过程,因为大多数治疗厂位于浓密的人口稠密的区域中。因此,有必要开发一种新的方法,这可以降低所需的反应器的体积以及满足更严格的营养物质排放标准。在此提出了一种生物氮和磷去除方法,五阶Bardenpho,其作为一种高端技术之一,在处理厂的放电标准和空间限制的情况下。图1显示了导频设备的示意图。将反应器分为5份定义为厌氧,第一缺氧,第一有氧,第二缺氧和最终的有氧罐。提供了使用在有氧罐中产生的硝酸盐作为电子受体和作为电子供体的内源性有机碳的硝酸盐提供另外的脱氧罐。最终的好氧罐用于从溶液中剥离残留的氮气,并最大限度地减少最终澄清器中磷的释放。来自第一有氧罐的混合液被再循环到第一脱氧罐以进行反硝化。将PAC(聚 - 氯化酰氯)加入到最终的好氧罐中以在必要时支撑磷去除。在碳源不足的情况下将甲醇加入第二脱氧池中。将流化的固定载体加入硝化反应器中以保持高浓度的硝化细菌。为了调查该过程的适用性向退出的市政废水处理厂进行了试验规范研究。检查了各种操作条件与营养去除性能之间的关系。研究了悬浮的活性污泥和固定化载体对硝化的贡献,以及影响反硝化的因素。在厌氧和有氧条件下,用磷释放和吸收率评估磷去除能力。两种类型的载体,结合和捕获的固定载体,替代地使用在第一有氧罐中,目的是降低反应堆体积。本研究的主要结果可以如下结束。 (1)无论在流入物的大浓度波动如何,该过程在去除氮气,磷和有机物质方面表现出良好的性能。随着该过程的应用,可以如下获得每年平均水质。 BoD5 <3 mg / L; T-N <3.0mg / L; T-P <0.3mg / L(2)观察到,与悬浮的活性污泥相比,固定载体的硝化活性对温度变化不敏感。由于载体对硝化的贡献增加,随着温度降低,可以

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