首页> 外国专利> METHOD FOR TREATING A WASTE STREAM IN AN ANAEROBIC MEMBRANE BIOREACTOR

METHOD FOR TREATING A WASTE STREAM IN AN ANAEROBIC MEMBRANE BIOREACTOR

机译:在厌氧膜生物反应器中处理废水的方法

摘要

A waste stream having anaerobically biodegradable components is fed to an anaerobic reactor where the components react with microorganisms to biodegrade the components and produce biomass and biogas. Mixing occurs in select portions of the anaerobic reactor, particularly the bottom and top portions of the reactor. Relatively heavy solids settle to the bottom and are mixed with the mixed liquor while relatively light or fine solids float to the top portion of the anaerobic reactor where they are mixed with the mixed liquor. This leaves an intermediate or middle portion of the anaerobic reactor where the concentration of solids is relatively lower compared to the concentration of solids in the upper or lower portion of the anaerobic reactor. Mixed liquor is pumped from the intermediate portion of the anaerobic reactor to a membrane separation unit where the mixed liquor is separated into a permeate stream and a retentate stream that is concentrated with solids. The retentate stream is recycled back to the anaerobic reactor and mixed with the mixed liquor therein. Further, mixed liquor and the relatively heavy solids are pumped from the bottom of the anaerobic reactor to a solids separator such as a hydrocyclone. Here the mixed liquor and solids are separated into a stream concentrated with heavier solids including a high percentage of inorganic precipitants and a lighter solids stream that contains a high percentage of biomass. This lighter solids liquid stream containing mixed liquor is recycled back to the anaerobic reactor for further treatment while the solid stream can be directed to a dewatering unit.
机译:具有厌氧可生物降解成分的废物流被送入厌氧反应器,在此该成分与微生物反应以生物降解成分并产生生物质和沼气。混合发生在厌氧反应器的选定部分,特别是反应器的底部和顶部。相对重的固体沉降到底部并与混合液混合,而相对轻或细的固体则漂浮到厌氧反应器的顶部,在此处与混合液混合。这留下了厌氧反应器的中间或中间部分,其中该固体的浓度与厌氧反应器的上部或下部中的固体的浓度相比相对较低。将混合液从厌氧反应器的中间部分泵送到膜分离单元,在此将混合液分离成渗透物流和保留有固体的渗余物流。截留物流被循环回到厌氧反应器,并与其中的混合液混合。此外,将混合液和相对重的固体从厌氧反应器的底部泵送到固体分离器例如水力旋流器中。在这里,混合的液体和固体被分离成由较重的固体浓缩的物流,其中包括较高百分比的无机沉淀剂和较轻的固体物流,其中包含较高百分比的生物质。将该包含混合液的较轻的固体液体料流再循环回厌氧反应器以进行进一步处理,同时可以将固体料流引入脱水装置。

著录项

  • 公开/公告号PL2558422T3

    专利类型

  • 公开/公告日2019-07-31

    原文格式PDF

  • 申请/专利权人 VEOLIA WATER SOLUTIONS & TECHNOLOGIES SUPPORT;

    申请/专利号PL20110769516T

  • 发明设计人 EWING JOHN;

    申请日2011-04-13

  • 分类号C02F3/28;

  • 国家 PL

  • 入库时间 2022-08-21 12:01:19

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号