Method and installation for treating wastewater containing ammonia

    公开(公告)号:US09815722B2

    公开(公告)日:2017-11-14

    申请号:US14085841

    申请日:2013-11-21

    申请人: cyklar-stulz GmbH

    发明人: Geert Nyhuis

    IPC分类号: C02F3/30 C02F3/12 C02F1/38

    摘要: A method and installation for treating wastewater containing ammonia includes feeding activated sludge from an aeration tank into a hydrocyclone. The sludge is separated into a specifically heavy fraction containing mostly anaerobic ammonia-oxidizing bacteria (anammox) and a specifically light fraction containing mostly aerobic oxidizing bacteria (AOB), which are returned to the aeration tank. The hydrocyclone includes a roughened inner wall surface for at least partially removing an organic or inorganic cover layer disposed on the anaerobic ammonium-oxidizing bacteria (anammox).

    DUAL RETURN ACTIVATED SLUDGE PROCESS IN A FLOW-EQUALIZED WASTEWATER TREATMENT SYSTEM

    公开(公告)号:US20170253515A1

    公开(公告)日:2017-09-07

    申请号:US15601678

    申请日:2017-05-22

    申请人: John H. Reid

    发明人: John H. Reid

    IPC分类号: C02F11/04 C02F3/22 C02F3/30

    摘要: A common final clarifier is provided downstream of a two-stage or three-stage activated sludge (AS) system that includes: (A) one or more flow equalization basin (FEB) reactors and a nitritation reactor as the first AS stage, and an anammox reactor as the second AS stage, or (B) a carbonaceous biological oxygen demand (BOD) removal reactor and one or more FEBs as the first AS stage, a nitritation reactor as the second AS stage, and an anammox reactor as the third AS stage. A first return activated sludge (RAS) flow is conducted from the final clarifier to the first AS stage and a second segregated RAS flow is conducted to the second AS stage. Alternatively, a third segregated RAS flow is conducted to the third AS stage.

    Simultaneous treatment of ammonia and phosphorus in a vertical reactor
    7.
    发明授权
    Simultaneous treatment of ammonia and phosphorus in a vertical reactor 有权
    在立式反应器中同时处理氨和磷

    公开(公告)号:US09522833B2

    公开(公告)日:2016-12-20

    申请号:US14286123

    申请日:2014-05-23

    IPC分类号: C02F3/30

    CPC分类号: C02F3/308 C02F3/301 C02F3/307

    摘要: There is described a number of biological nutrient removal processes including Anammox Process, Biological Phosphorus Removal (BPR), Partial Nitrification, Full Nitrification, Partial Denitrification, Full Denitrification and Denitrification via BPR taking place in a Simultaneous Treatment of Anammox/PAOs Reactor (STAR) coupled with an Anaerobic Lateral Unit (ALU). In one aspect, there is a wastewater treatment system comprises a bioreactor having three consecutive stages: and an anaerobic lateral unit (ALU) coupled to the bioreactor; the bioreactor and ALU are configured to conduct biological removal of nutrients from the wastewater using a plurality of biological processes simultaneously. The three consecutive stages of the bioreactor comprise two Anoxic stages configured consecutively followed by one Aerobic stage. The stages may be oriented vertically and use gravity for fluid flow.

    摘要翻译: 描述了在Anammox / PAOs反应器(STAR)的同时处理中通过BPR发生的一些生物营养物去除方法,包括Anammox Process,生物除磷(BPR),部分硝化,全硝化,部分脱氮,全反硝化和脱氮。 再加上厌氧侧向单位(ALU)。 一方面,废水处理系统包括具有三个连续阶段的生物反应器和与生物反应器耦合的厌氧侧向单元(ALU); 生物反应器和ALU被配置为使用多个生物过程同时从废水中进行营养物质的生物去除。 生物反应器的三个连续阶段包括两个缺氧阶段,连续配置一个有氧阶段。 阶段可以垂直取向,并使用重力来进行流体流动。

    PROCESS FOR BIOLOGICAL REMOVAL OF NITROGEN FROM WASTEWATER
    10.
    发明申请
    PROCESS FOR BIOLOGICAL REMOVAL OF NITROGEN FROM WASTEWATER 审中-公开
    从废水中生物去除氮的方法

    公开(公告)号:US20160052811A1

    公开(公告)日:2016-02-25

    申请号:US14784830

    申请日:2014-04-03

    申请人: PAQUES I.P. B.V.

    IPC分类号: C02F3/30

    摘要: The invention relates to a process for biological removal of nitrogen from wastewater comprising: (a) providing a stream of wastewater comprising ammonium; (b) continuously supplying the stream of wastewater to a reactor containing granular sludge comprising granules having a core of anammox bacteria and an outer rim of ammonia oxidizing bacteria; (c) subjecting the wastewater in the reactor to ammonium oxidation under ammonium oxidizing conditions comprising a temperature in the range of from 5 to 25° C., a concentration of dissolved oxygen in the wastewater in the range of from 0.4 mg/L to 4.0 mg/L, and a hydraulic retention time of the wastewater in the reactor in the range of from 0.5 hours to 1.5 days, to obtain a gaseous stream comprising nitrogen and a dispersion of granular sludge and non-granular sludge in treated wastewater; and (d) continuously separating the dispersion obtained into a stream comprising granular sludge and a stream comprising treated wastewater and non-granular sludge and recycling the stream comprising granular sludge to the reactor and discharging the non-granular sludge from the process, wherein the granular sludge has a retention time in the reactor of at least ten times the hydraulic retention time, and wherein the retention time of any non-granular sludge in the reactor is equal to or at most three times the hydraulic retention time.

    摘要翻译: 本发明涉及从废水中生物去除氮的方法,包括:(a)提供包含铵的废水流; (b)连续地将废水流供应到含有含有氨氧化细菌核和氨氧化细菌外缘的颗粒的含有颗粒污泥的反应器中; (c)使反应器中的废水在包含5至25℃范围内的温度,废水中的溶解氧浓度在0.4mg / L至4.0的范围内的铵氧化条件下进行铵氧化 mg / L,反应器废水的水力停留时间为0.5〜1.5天,得到含氮气体和处理废水中颗粒污泥和非颗粒污泥的分散体; 和(d)将得到的分散体连续地分离成包含颗粒污泥的流和包含经处理的废水和非颗粒污泥的料流,并将包含颗粒污泥的料流再循环到反应器中并从该方法排出非颗粒污泥,其中颗粒状 污泥在反应器中的停留时间为水力停留时间的至少十倍,并且其中反应器中任何非颗粒污泥的停留时间等于或至多为水力停留时间的三倍。