METHOD FOR TREATING AND/OR PRETREATING LIQUID MANURE OR BIOGAS PLANT REJECT FOR THE ELIMINATION OF HARMFUL SUBSTANCES, PARTICULARLY NITROGEN, PHOSPHORUS, AND ODOR MOLECULES
    22.
    发明公开
    METHOD FOR TREATING AND/OR PRETREATING LIQUID MANURE OR BIOGAS PLANT REJECT FOR THE ELIMINATION OF HARMFUL SUBSTANCES, PARTICULARLY NITROGEN, PHOSPHORUS, AND ODOR MOLECULES 有权
    方法用于治疗或液体肥料或沼气厂废物消除有机物的治疗,尤其是氮,磷,产生臭气分子的

    公开(公告)号:EP2279153A1

    公开(公告)日:2011-02-02

    申请号:EP09735169.6

    申请日:2009-04-24

    申请人: Pellon Group Oy

    摘要: The invention relates to a method and an apparatus for treating and/or pre- treating liquid manure or biogas plant reject for eliminating harmful substances, particularly nitrogen, phosphorus, and odor molecules. Process tanks (5), which include inlet means (4) for supplying a process tank (5) with a substance to be treated, outlet means for passing a post-treatment matter out of the tank, and air inlet means (2) for supplying the process tank with air required by a biological process, are used for conducting a biological treatment on the matter to be treated. The process tanks (5) are first provided with a microbe population adapted for treating the matter to be treated. The matter to be treated is supplied gradually into the first process tank and thence further into a subsequent process tank, such that the microbe population initially provided in the process tanks displaces in a step- by-step manner the original microbe population present in the matter to be treated. The matter, which is substantially free of the original microbes and has been expelled from the final process tank, is returned into the first process tank for diluting the matter to be treated. Downstream of the process tanks is conducted a nitrogen removal treatment by feeding the matter to be treated from the process tank (5) of a stripping tower (22A), in which the pH of a matter to be treated has been raised by means of a biological treatment to a level sufficient from the standpoint of nitrogen removal.

    摘要翻译: 本发明涉及用于治疗和/或预处理液体肥料或沼气拒绝消除有害物质,特别是氮,磷,和气味分子的方法和装置的植物。 处理槽(5),其中包括进气装置(4),用于与物质供给处理槽(5)的待处理,出口装置用于使后处理物从槽中取出,并空气进气装置(2),用于 供给与由生物处理所需空气的处理槽,用于对此事进行生物处理来对待。 处理罐(5)首先被设置有微生物种群angepasst用于处理物质来对待。 待处理的物质逐渐供应到第一处理槽,并由此进一步进入后续处理槽,检查的确在处理罐最初提供的微生物种群以一步一步方式位移微生物种群存在于物质的原 来对待。 这件事,所有这一切基本上不含原微生物,并从最终的处理罐被排出,返回到第一处理罐的稀释将待处理。 下游的处理槽的是通过将所述物质从处理槽治疗传导氮去除处理(5)汽提塔(22A),在待处理的物质的pH值已通过的手段提出了 生物处理以从除氮的观点出发充足的水平。

    Système et procède de traitement des eaux usées
    23.
    发明公开
    Système et procède de traitement des eaux usées 审中-公开
    系统zur Behandlung von Brauchwasser

    公开(公告)号:EP2213627A1

    公开(公告)日:2010-08-04

    申请号:EP10001027.1

    申请日:2010-01-29

    IPC分类号: C02F3/04 C02F3/34 C02F3/20

    摘要: L'invention concerne un système de traitement des eaux usées comprenant :
    - un réacteur principal (1) contenant la matière d'un lit filtrant (2) granulaire, ladite matière étant fixe et reposant sur un bac de récupération (3) des eaux traitées,
    - un dispositif (4) pour injecter les eaux usées disposé dans le réacteur principal (1), au-dessus du lit filtrant (2),
    - un dispositif (7) pour injecter du gaz oxygéné ou de l'air dans le lit filtrant,
    se caractérisant par le fait que :
    - ledit système comprend un réacteur primaire (5) configuré pour assurer le stockage préalable temporaire des eaux usées à traiter avant leur injection régulière dans le lit filtrant (2), ledit réacteur primaire contenant un lit enzymatique (50), les eaux usées transitant par ledit réacteur primaire avant d'être injectées dans le réacteur principal (1),
    - le dispositif (4) pour injecter les eaux usées comprend des buses (40) aménagées au-dessus du lit filtrant (2) et disposées de manière à assurer une répartition uniforme des eaux usées dans ledit lit filtrant, ledit dispositif d'injection étant configuré pour injecter les eaux usées de manière discontinue dans ledit lit filtrant,
    - le dispositif (7) pour injecter le gaz oxygéné ou l'air est disposé dans la partie inférieure du lit filtrant (2), au coeur de celui-ci, ledit dispositif d'injection étant configuré pour injecter le gaz oxygéné ou l'air de manière discontinue.

    摘要翻译: 废水处理系统包括含有颗粒过滤床(2)的材料的主反应器(1),用于不连续地将设置在主反应器上的废水排放到过滤床上方的装置(4),以使下沉式废水流入回收罐 (3)通过床,以及装置(7),以在过滤床中不连续地注入氧气或空气。 材料是固定的,基于处理水的回收罐。 布置第一反应器(5),用于在喷射过滤床之前将待处理的废水初次临时储存一天。 废水处理系统包括含有颗粒过滤床(2)的材料的主反应器(1),用于不连续地将设置在主反应器上的废水排放到过滤床上方的装置(4),以使下沉式废水流入回收罐 (3)通过床,以及装置(7),以在过滤床中不连续地注入氧气或空气。 材料是固定的,基于处理水的回收罐。 布置第一反应器(5),用于在注入过滤床之前将待处理的废水初始临时储存一天,并且包括酶床,以加速和促进废水中包含的细菌质量的发展。 废水注入装置包括布置在过滤床上方的喷嘴,以确保床中的废水均匀分布。 氧气或空气注入装置布置在过滤床的底部或过滤床的核心内,使得好氧废水在其通过期间被充气。 与废水同时注入氧气或空气。 第一反应器连接到主反应器或独立于主反应器,并且配备有液位传感器,使得当废水达到预定的时间时,泵送装置的单元允许将来自第一反应器的富含细菌的废水进入主反应器 水平。 氧气或空气注入装置包括在过滤床的核心处的喷嘴,其中喷嘴连接到耦合到一组光伏电池的空气泵,用于提供电力供应。 颗粒过滤床材料由粒度为15-20mm的砂粒组成,由非钙质硅质砂制成,粒度为2-5mm。 回收罐与带格栅或格栅的过滤床分离。 废水处理过程包括独立权利要求。

    REACTEUR BIOLOGIQUE SEQUENTIEL A SELECTEUR POUR LE TRAITEMENT D'EAUX RESIDUAIRES URBAINES OU INDUSTRIELLES
    24.
    发明公开
    REACTEUR BIOLOGIQUE SEQUENTIEL A SELECTEUR POUR LE TRAITEMENT D'EAUX RESIDUAIRES URBAINES OU INDUSTRIELLES 有权
    与选择用于处理城市和工业废水连续生物反应器

    公开(公告)号:EP2193101A2

    公开(公告)日:2010-06-09

    申请号:EP08859070.8

    申请日:2008-10-01

    申请人: DEGREMONT

    IPC分类号: C02F3/12

    摘要: Sequential biological reactor (R), comprising: a tank (1) delimited by a base and peripheral walls (3); an inlet (11) equipped with a selector (S) that determines a baffled route with contacting of the effluent to be treated and a portion (5) of the recirculated sludges; a means (6) for discharging the treated water in the top part of the water surface of the tank, and an outlet (7) for discharging the excess sludges in the bottom of the tank. The selector (S) comprises a vessel (8) placed in the tank (1) at a distance from the peripheral walls (3); the vessel is compartmentalized into several sectors (8.1, 8.2, 8.3, 8.4), the outlet from one sector, which is also the inlet of the following sector, being alternately low and high, or vice versa, and a last step is defined by a chamber (13) formed by two partitions (14, 15) that extend between the wall of the vessel (8) and the peripheral walls (3) of the tank and that surround the top outlet (12) of the last sector of the vessel, the lower edge of the partitions being at a distance from the base and determining two low openings for passage of the effluent into the tank.

    METHOD AND APPARATUS FOR BIOLOGICALLY TREATING ORGANIC DISCHARGED WATER
    25.
    发明公开
    METHOD AND APPARATUS FOR BIOLOGICALLY TREATING ORGANIC DISCHARGED WATER 审中-公开
    方法和装置的有机废水生物处理

    公开(公告)号:EP2022763A1

    公开(公告)日:2009-02-11

    申请号:EP06745862.0

    申请日:2006-04-28

    IPC分类号: C02F3/12 C02F1/44 C02F11/02

    摘要: In a single-tank activated sludge process or a multistage activated-sludge process using predation action of animalcules, an improvement in treatment efficiency and a decrease in the amount of excess sludge generation are achieved, while maintaining stable treated water qualities. In a biological treatment wherein organic wastewater is introduced to a first biological treatment tank 1A and is biologically treated with bacteria, the treatment liquid containing the bacteria in the first biological treatment tank 1A is introduced to a second biological treatment tank 1B and is activated-sludge treated, and the treatment liquid from the second biological treatment tank 1B is separated into sludge and treated water, a portion of the sludge in the second biological treatment tank 1B and/or at least a portion of the separated sludge is introduced into a sludge treatment tank 3 having a submerged filter element 4 with a pore diameter of 5 to 100 µm in the tank and is subjected to aerobic biological treatment, and the liquid permeated through the submerged filter element 4 is returned to the first biological treatment tank 1A and/or the second biological treatment tank 1B. Both high effect of reduction in the amount of sludge and satisfactory treated water qualities can be simultaneously achieved by reducing the amount of sludge with animalcules in the sludge treatment tank 3, allowing residual fine components to permeate through the submerged filter element 4, and, again, returning the fine components to the filter predation animalcule tank 1B for predation.

    摘要翻译: 在单罐活性污泥法或者利用微型动物以改善处理效率,并在剩余污泥的产生得以实现的量的减少的捕食作用,同时保持稳定的处理水质量的多级活性污泥法。 在worin有机性废水的生物处理被引入到第一生物处理槽1A和进行生物与细菌治疗,包含在第1生物处理槽1A中的细菌的处理液导入到第2生物处理槽1B,是活性污泥 处理,并从第2生物处理槽1B的处理液分离成污泥和处理水,在第2生物处理槽1B所涉及的污泥的一部分和/或至少将分离污泥的一部分被引入到污泥处理 槽3具有浸渍滤材元件4中的罐5至100微米的孔径,并进行需氧性生物处理,并通过浸没过滤器元件4渗透的液体返回到所述第1生物处理槽1A和/或 第2生物处理槽1B。 减少污泥和满意的处理后的水的质量的量的两个高的效果可以通过减少污泥量与在污泥处理槽3微型动物,允许残留微细成分透过浸没式过滤器元件4渗透同时实现,并且,再次 ,返回微细成分到过滤捕食了微生物槽1B用于捕食。

    AEROBIC BIOMASS GRANULES FOR WASTE WATER TREATMENT
    27.
    发明公开
    AEROBIC BIOMASS GRANULES FOR WASTE WATER TREATMENT 审中-公开
    好氧颗粒污泥生物量的废水处理

    公开(公告)号:EP1476403A4

    公开(公告)日:2006-12-20

    申请号:EP03742694

    申请日:2003-01-28

    IPC分类号: C02F3/10 C02F3/12 C02F3/00

    摘要: The method of producing aerobic biogranules for the treatment of waste water comprising the steps of: a) introducing waste water into a reactor; b) seeding the reactor with a active biomass material; c) supplying the oxygen-containing gas to the reactor to provide a mixing action to the suspension of biomass material in said waste water, the supply of oxygen-containing gas providing a superficial upflow gas velocity greater than 0.25 cm/s; d) initiating a period of nutrient starvation of the biomass material while continuing to supply oxygen-containing gas; e) allowing formed aerobic granules to settle in a settling zone in said reactor; f) discharging at least a portion of the waste water; g) repeating steps (a) to (f) until at least a portion of the biogranules in said settling zone are within a predetermined properties; and h) recovering said biomass granules within those predetermined properties.

    PROCESS FOR PRODUCING POLYHYDROXYALKANOATE
    30.
    发明公开

    公开(公告)号:EP3383806A1

    公开(公告)日:2018-10-10

    申请号:EP16805812.1

    申请日:2016-12-02

    申请人: Paques I.P. B.V.

    发明人: DIJKMAN, Hendrik

    IPC分类号: C02F3/12 C02F3/34 C12P7/62

    摘要: High levels of microbial storage compound (MSC) such as polyhydroxyalkanotaes (PHA) can be produced from wastewater comprising Readily Biodegradable COD (RBCOD) using activated sludge comprising microorganisms capable of accumulating MSC by contacting the wastewater with the activated sludge in the presence of dissolved oxygen during a first period of time, to obtain MSC-loaded activated sludge comprising MSC at a level of at least 60 wt.% based on dry weight of the organic part of the sludge, and then supplying elements essential for growth such as nitrogen and phosphorus and allowing up-take of these elements and limited growth during a second period of time, the supplied amount of at least of one of said essential elements compared to the amount of RBCOD supplied in step a) limiting the growth to an extent that not all MSC is used for growth, to obtain grown activated sludge comprising residual MSC at a level of at least 20 wt.% based on dry weight of the organic part of the sludge; and removing or harvesting part of the MSC-loaded activated sludge and/or part of the grown activated sludge, so that the total average retention time of the sludge is less than 72 h.