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Increasing the capacity of an extended nutrient removal plant by using different techniques

机译:通过使用不同的技术来提高扩展营养去除植物的能力

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A comprehensive investigation which included full scale tests was initiated towards the late 1980:s with the primary aim to find an appropriate upgrading technology for the Klagshamn wastewater treatment plant in Malmo, Sweden. The finally selected strategy enabled that a concentration of less than 8 mg N/l could be reached in the secondary effluent without having to extend either the primary or secondary treatment step at the actual load on the plant. In order to comply with a future stringent phosphorus standard however, a tertiary filtration plant has to be built. In future, it has to be anticipated that the load on the plant may be doubled due to the fact that a bridge between Malmo and Copenhagen is being built. As a consequence, it was important to continue the upgrading work by estimating the ultimate plant capacity and to look for measures to increase the capacity if necessary. By optimising the plant operation, it seems possible to reach an effluent nitrogen concentration of less than 12 mg/l at a load corresponding to the future design load. The suggested approach implies that the plant has to be operated on the margin and as a consequence the possibility to include a denitrification step as part of the filtration plant was also investigated. As a result, ii was decided to build a separate denitrification step at the same time as the filtration plant was built. (C) 1998 IAWQ. Published by Elsevier Science Ltd [References: 10]
机译:到1980年代末期开始进行包括全面测试的全面调查,其主要目的是为瑞典马尔默的Klagshamn废水处理厂找到合适的升级技术。最终选择的策略使得在二级废水中的浓度可以达到8 mg N / l,而不必在工厂的实际负荷下延长一级或二级处理步骤。然而,为了符合未来的严格磷标准,必须建造第三级过滤设备。将来,由于正在建造马尔默和哥本哈根之间的桥梁,因此必须预料工厂的负荷可能会加倍。因此,重要的是要通过估算工厂的最终产能来继续进行升级工作,并在必要时寻求措施来提高产能。通过优化工厂运行,在与将来的设计负荷相对应的负荷下,似乎可以达到小于12 mg / l的污水氮浓度。建议的方法意味着该设备必须在边缘运行,因此,还研究了将反硝化步骤作为过滤设备一部分的可能性。结果,ii决定在建造过滤设备的同时建立一个单独的反硝化步骤。 (C)1998 IAWQ。由Elsevier Science Ltd发布[参考:10]

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