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Anaerobic and aerobic activated sludge process

机译:厌氧和好氧活性污泥工艺

摘要

PURPOSE:To provide an anaerobic and aerobic activated sludge method easy to control and capable of achieving the space saving of treatment facilities by the fuzzy inference of an air sending amt. based on the respiration speed and dissolved oxygen amt. of the nitration reaction in an aerobic tank. CONSTITUTION:An anaerobic tank 10 performing denitrification treatment due to denitrifying bacteria, an aerobic tank 20 provided to the next stage of the anaerobic tank 10 and performing the oxidative decomposition of org. matter and ammonia nitration treatment due to nitrifying bacteria and a final sedimentation basin for sedimenting sludge 30 provided to the next stage of the aerobic tank 20 are provided. Air is sent into the aerobic tank 20 in a required air sending amt. and a part of the sludge sedimented in the final sedimentation basin is returned to the anaerobic tank 10 and excessive sludge is drawn out to the outside in a required drawing-out amt. and a nitration soln. is returned to the anaerobic tank 10 from the rear end of the aerobic tank 20 in a required rate and circulated. By this constitution, an air sending amt. is subjected to fuzzy inference on the basis of the respiration speed and dissolved oxygen amt. of the nitration reaction in the aerobic tank 20. As a result, an anaerobic and aerobic activated sludge method easy to control and capable of achieving the space saving of facilities is provided.
机译:目的:提供一种厌氧和好氧活性污泥的方法,该方法易于控制,并且可以通过空气输送罐的模糊推理来实现处理设施的空间节省。根据呼吸速度和溶氧量。好氧罐中的硝化反应组成:一个厌氧池10,由于进行反硝化细菌而进行反硝化处理,一个需氧池20设置在厌氧池10的下一阶段并进行氧化分解。提供由硝化细菌引起的物质和氨的硝化处理,以及设置在好氧槽20的下一级的用于沉淀污泥30的最终沉淀池。空气以所需的空气输送罐被输送到需氧罐20中。然后,将沉淀在最终沉淀池中的一部分污泥返回到厌氧池10中,并且将多余的污泥以所需的排出装置排出到外部。和硝化溶液从需氧罐20的后端以所需的速率返回到厌氧罐10并循环。通过这种构造,可以发送空气。根据呼吸速度和溶氧量进行模糊推理。结果,提供了一种好氧罐20中硝化反应的方法。结果,提供了一种易于控制并且能够实现设施的空间节省的厌氧和好氧活性污泥法。

著录项

  • 公开/公告号JP3422065B2

    专利类型

  • 公开/公告日2003-06-30

    原文格式PDF

  • 申请/专利权人 株式会社明電舎;

    申请/专利号JP19940029409

  • 发明设计人 小西 隆裕;

    申请日1994-02-28

  • 分类号C02F3/34;C02F3/30;

  • 国家 JP

  • 入库时间 2022-08-22 00:20:45

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