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Method for processing manure, fermented manure and ammonium nitrogen containing waste water

机译:粪肥,发酵粪肥和含铵氮废水的处理方法

摘要

The invention relates to a method for processing manure, fermented liquid manure being subjected to nitrification in a first step and to denitrification in a subsequent step, an aerated reactor which contains active sludge rich in nitrifying bacteria being used in the nitrification step and acid-neutralizing chemicals being added to said reactor if necessary and a continuously fed upflow sludge bed (USB) reactor which contains a very compact biomass which is capable of converting nitrate to nitrogen gas and to which an organic substrate is added being used in the denitrification step, the loading of the reactor being controlled to obtain an optimum nitrification and denitrification and this is obtained on the basis of one or more of the following data:PPthe incoming nitrogen load;PPthe information from the WAZU respiration meter;PPthe pH in the nitrification reactor, the criterion for which is that the pH is in the range limited by 6 and 8. 5; PPthe temperature in both the nitrification reactor and the denitrification reactor is kept below 40 C.;P Pthe concentration of oxidized nitrogen in the influent for the denitrification reactor, the criterion for which is that the concentration is between 0 and 4 g N/l;P Pthe concentration of oxidized nitrogen in the nitrification reactor, the criterion for which in the sludge/liquid mixture in the reactor is that the concentration is between 0 and 4 g N/l;PPthe concentration of the carbon source in the effluent from the denitrification reactor;PPthe gas production in the denitrification reactor. The invention further relates to an apparatus for performing this method comprising at least one WAZU respirator meter.
机译:本发明涉及一种处理肥料的方法,首先对发酵的液体肥料进行硝化,然后在随后的步骤中进行反硝化,其中在硝化步骤中使用含有富含硝化细菌的活性污泥的曝气反应器并进行酸中和。在必要时,将化学药品添加到所述反应器中,并将包含非常紧凑的生物质的连续进料上流污泥床(USB)反应器用于脱硝步骤,该生物质能够将硝酸盐转化为氮气,并向其中添加有机底物。控制反应器的负荷以获得最佳的硝化作用和反硝化作用,这是基于以下数据中的一个或多个获得的:输入的氮负荷; P的信息WAZU呼吸计;硝化反应器中的pH,其标准是pH在6和8限制的范围内。5;

硝化反应器和反硝化反应器的温度均保持在40°C以下;

反硝化反应器进水口中氧化氮的浓度,其标准是浓度在0至4 g N / l之间;

在硝化反应器中氧化氮的浓度,在反应器中的污泥/液体混合物中,其浓度在0至4 g之间的标准N / l;

来自反硝化反应器的流出物中碳源的浓度;

反硝化反应器中的气体产生。本发明还涉及一种用于执行该方法的设备,该设备包括至少一个WAZU呼吸仪。

著录项

  • 公开/公告号US5296147A

    专利类型

  • 公开/公告日1994-03-22

    原文格式PDF

  • 申请/专利权人 ECOTECHNIEK B.V.;

    申请/专利号US19930070112

  • 发明设计人 IMAN W. KOSTER;ABRAHAM KLAPWIJK;

    申请日1993-06-01

  • 分类号C02F3/30;

  • 国家 US

  • 入库时间 2022-08-22 04:32:04

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