PROCESS FOR ENHANCING POLYHYDROXYALKANOATE ACCUMULATION IN ACTIVATED SLUDGE BIOMASS
    3.
    发明公开
    PROCESS FOR ENHANCING POLYHYDROXYALKANOATE ACCUMULATION IN ACTIVATED SLUDGE BIOMASS 审中-公开
    提高活性污泥生物质中聚羟基烷酸酯积累的方法

    公开(公告)号:EP3186201A1

    公开(公告)日:2017-07-05

    申请号:EP15772010.3

    申请日:2015-08-06

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

    摘要: A process for producing PHA comprises obtaining biomass produced in the course of biologically treating a first wastewater source containing RBCOD. The biomass is to be exploited with a second wastewater source having a different RBCOD content from the first wastewater source in order to accumulate and thereby produce PHA. Before subjecting the biomass to a PHA accumulation process, the biomass PHA accumulation potential is enhanced via an acclimation process with the second wastewater source. During acclimation, the biomass is subjected to repeated feast-famine periods. During each feast period, the biomass is exposed to a fraction of the second wastewater source. The RBCOD uptake and/or biomass respiration rate is directly or indirectly measured during each feast period. The famine period is maintained for a period of time that is at least two times greater than the length of time of the proceeding feast period. After at least two feast-famine acclimation periods or after one or more measured parameters reveal an increased RBCOD relative uptake or respiration rate of the biomass during a subsequent feast period, the biomass is subjected to a PHA accumulation process using the second wastewater source.

    摘要翻译: 生产PHA的方法包括获得在生物处理含有RBCOD的第一废水源的过程中产生的生物质。 生物质将与来自第一废水源的具有不同RBCOD含量的第二废水源一起开采,以积累并由此生产PHA。 在使生物质经受PHA积累过程之前,通过使用第二废水源的适应过程来增强生物质PHA积聚潜力。 在适应期间,生物质遭受反复的盛宴 - 饥荒期。 在每个节日期间,生物质暴露于第二废水源的一部分。 在每个节日期间直接或间接测量RBCOD吸收量和/或生物量呼吸速率。 饥荒时期保持一段时间,至少比正在进行的盛宴时间长两倍。 在至少两次盛宴 - 饥荒适应期之后或者在一个或多个测量参数之后,揭示在随后的盛宴期间生物质的RBCOD相对摄取或呼吸速率增加,使用第二废水源对生物质进行PHA积聚过程。

    SBR-KLÄRANLAGE
    5.
    发明公开
    SBR-KLÄRANLAGE 审中-公开
    SBR污水处理厂

    公开(公告)号:EP3135637A1

    公开(公告)日:2017-03-01

    申请号:EP15183081.7

    申请日:2015-08-31

    申请人: KLARO GmbH

    发明人: Graf, Otto P.

    IPC分类号: C02F3/12

    摘要: In einer SBR-Kläranlage (K) mit einem Ablauf (6) und einer bedarfsabhängig aktivierbaren, zum Ablauf (6) führenden Klarwasser-Hebevorrichtung (3) sind unter einem Auslass (2) der Hebevorrichtung eine sich selbst in die SBR-Kläranlage (K) entleerende Abscheidekammer (4) und zwischen der Abscheidekammer (4) und dem Ablauf (6) ein über eine Überlaufschwelle (10) aus der Abscheidekammer (4) speisbarer Probenahmebehälter (5) vorgesehen, um einen anfänglichen verschmutzten Spülstoß bei einem Abzugszyklus vom Probenahmebehälter (5) fernzuhalten.

    摘要翻译: 在一个SBR处理厂(K)具有出口(6)和一个需求依赖性激活时,端部(6)的出口领先清水提升装置(3)(2)的提升装置的自(在SBR处理厂的K )从分离室排空分离室(4)和(之间的分离室中提供4)和出口(6)(通过溢流阈10)(4)speisbarer采样容器(5)的初始污染的第一齐平(在从取样容器的剥离周期 保持5)。

    WASTEWATER PROCESSING METHOD, SYSTEM, AND METHOD FOR MEASURING POLLUTANT-DECOMPOSITION ACTIVITY
    7.
    发明公开
    WASTEWATER PROCESSING METHOD, SYSTEM, AND METHOD FOR MEASURING POLLUTANT-DECOMPOSITION ACTIVITY 审中-公开
    废品处理系统,程序和方法测量有害的分解作用

    公开(公告)号:EP2565166A4

    公开(公告)日:2016-08-10

    申请号:EP11774969

    申请日:2011-04-25

    申请人: IRIE RYOZO

    发明人: IRIE RYOZO

    IPC分类号: C02F3/12 C02F3/00

    摘要: There is provided a method which eliminates a decrease in activity of an activated sludge treatment microorganism group, which greatly increases treatment ability of the microorganism group, to enhance treatment efficiency and to reduce the amount of excess sludge. The wastewater treatment method of the present invention includes, when raw water (1a) is subjected to an activated sludge treatment, performing a first sludge returning step (Va) (a step of returning sludge, which was previously aerated and stirred in a first excess sludge tank or sludge retention tank (12a) equipped with an aerator and a stirrer, to an treatment tank, a sequencing batch reactor or an anaerobic tank; and/or a step of returning sludge, which was previously aerated and stirred in a second excess sludge tank or thickened sludge retention tank (13a) equipped with an aerator and a stirrer, to a treatment tank, a sequencing batch reactor or an anaerobic tank), and maintaining the number of genus Bacillus bacteria in the treatment tank, the sequencing batch reactor or the anaerobic tank, to which the sludge has been returned, at 2.0×10 5 to 22.5×10 5 cfu/mL.