首页> 外国专利> Process for the biological oxidation of organic carbon compounds (BOD reduction) by nitrification and denitrification of the nitrogen compounds of effluents without external H-donors for the denitrification and plant for carrying out the process

Process for the biological oxidation of organic carbon compounds (BOD reduction) by nitrification and denitrification of the nitrogen compounds of effluents without external H-donors for the denitrification and plant for carrying out the process

机译:通过不带外部H供体的废水氮化合物的硝化和反硝化,对有机碳化合物进行生物氧化(减少BOD)的方法,以及进行该过程的设备

摘要

The invention relates to a process for the biological oxidation of organic carbon compounds (BOD reduction) by nitrification and denitrification of the nitrogen compounds of effluents without external H-donors for the denitrification and to a plant for carrying out the process. The effluent in this case is treated in at least three separate successive purification stages. In the first stage, for the biological oxidation of organic carbon compounds, the effluent is subjected to a highly loaded activation process known per se with intermediate clarification and internal activated sludge circulation. In the second stage, the effluent is completely nitrified after passing through a bio-film reactor known per se. In the third state, in a denitrification secondary treatment tank, the effluent flows through three zones functionally separated from each other vertically arranged so that sludge is thickened and surplus sludge is withdrawn in the bottom zone, the effluent is denitrified in the central zone and sludge is separated from the effluent in the top zone. During this, part of the return sludge from the first highly-loaded activation stage, with or without thickening, with or without washing, in an intermediate stage are introduced into the central zone of the secondary treatment tank as H-donor for the denitrification with the nitrate-containing efflux water of the biofilm reactor.
机译:本发明涉及一种通过硝化和反硝化没有外部H供体的流出物中的氮化合物使有机碳化合物生物氧化(减少BOD)的方法,以及一种进行该方法的设备。在这种情况下,流出物在至少三个单独的连续纯化阶段中进行处理。在第一阶段,为了有机碳化合物的生物氧化,对废水进行本身已知的高负荷活化过程,并进行中间澄清和内部活化污泥循环。在第二阶段中,废水经过本身已知的生物膜反应器后被完全硝化。在第三种状态下,在脱氮二级处理池中,废水流经三个功能上相互垂直分隔的区域,从而使污泥变稠,底部污泥被抽出,废水在中心区域和污泥中被脱氮。从顶部区域的废水中分离出来。在此期间,来自第一高负荷活化阶段的一部分返回污泥,在中间阶段有或没有增稠,有洗或无洗,都作为H-给体引入到二级处理池的中央区域,以进行反硝化。生物膜反应器的含硝酸盐的流出水。

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