会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Method for purifying carbon-containing pollution and denitrifying waste water in oxygenic medium
    • 含氧污染净化方法和含氧介质中的废水脱氮方法
    • US06254778B1
    • 2001-07-03
    • US09254173
    • 1999-03-02
    • Pavel ChudobaClaude GrimaudRoger Pujol
    • Pavel ChudobaClaude GrimaudRoger Pujol
    • C02F312
    • C02F3/06C02F3/006C02F3/12C02F3/30C02F3/302C02F2209/04C02F2209/14C02F2209/15Y02W10/15
    • The invention is a biological process for purifying waste water in order to produce an effluent with a low content of carbon and of oxygenated nitrogen compounds. The process includes an initial step of mixing the waste water in a biological reactor with activated sludge to denitrify the resulting mixture. Then, air is introduced into the mixture to form an anoxic sludge thereby directly oxidizing carbon present in the anoxic sludge and removing carbon therefrom, simultaneous with the denitrification. The anoxic sludge is clarified to separate it from a denitrified intermediate effluent. The clarified anoxic sludge is recycled to the biological reactor. Then, intermediate effluent is nitrified to form a nitrified liquor and a portion of the nitrified liquor is recycled into the anoxic sludge that is present in the biological reactor, thereby subjecting the anoxic sludge to oxygen present in nitrified compounds and consequently further removing carbon from the anoxic sludge, simultaneous with the denitrification. The rate of removal of carbon is controlled as a function of the flow rate/pollution characteristics of the anoxic sludge while a redox potential of the anoxic sludge is continuously measured. A nitrate concentration of the intermediate effluent is continuously measured. There is an adjustment of an amount of air introduced into the anoxic sludge in accordance with the measured redox potential and measured nitrate concentration. A recycling flow rate of the nitrified liquor is adjusted in accordance with the measured redox potential and measured nitrate concentration. The remaining nitrified liquor is the final effluent.
    • 本发明是用于净化废水以生产低碳含量和含氧氮化合物的流出物的生物过程。 该方法包括将生物反应器中的废水与活性污泥混合以使得到的混合物脱氮的初始步骤。 然后,将空气引入混合物中以形成缺氧污泥,从而直接氧化存在于缺氧污泥中的碳,并与脱氮同时除去碳。 澄清缺氧污泥以将其与反硝化中间体流出物分离。 澄清的缺氧污泥被再循环到生物反应器中。 然后,将中间体流出物硝化以形成硝化液,并将一部分硝化液循环到存在于生物反应器中的缺氧污泥中,从而使缺氧污泥对存在于硝化化合物中的氧进行再次除去, 缺氧污泥,同时脱氮。 作为缺氧污泥的流量/污染特性,连续测定缺氧污泥的氧化还原电位,控制碳的除去速度。 连续测量中间体流出物的硝酸盐浓度。 根据测量的氧化还原电位和测量的硝酸盐浓度,调节引入到缺氧污泥中的空气量。 根据测得的氧化还原电位和测量的硝酸盐浓度调节硝化液的再循环流量。 剩余的硝化液是最后的废水。
    • 2. 发明授权
    • Method for eliminating phosphorous contained in effluents
    • 消除污水中含磷的方法
    • US6077430A
    • 2000-06-20
    • US308891
    • 1999-05-26
    • Pavel ChudobaRoger Pujol
    • Pavel ChudobaRoger Pujol
    • C02F3/00C02F3/12C02F3/30G01N33/18
    • C02F3/1215C02F3/006C02F3/30C02F3/308G01N33/182C02F2209/11C02F2209/18Y02W10/15Y10S210/906
    • This method measures the soluble phosphorus concentration in the treated water for at least two different places of the treatment line: at the intake of the secondary clarification step to obtain a measurement P1 and at the outlet of the treatment line to obtain a measurement P2, the measurement P1 determining the amounts of the product precipitating the phosphorus in the liquor of at least one of the tanks in which the anoxic or aerobic steps are carried out upstream of the secondary clarification. The measurement P2 is continuously compared to the measurement P1 so as to detect a possible salting out of the phosphorus at the level of the secondary clarification. When the difference between these two measurements (.DELTA.P1-P2) is noted, one of the two following measures occurs: supplementary injection of the precipitating product, before the secondary clarification, or modification of the flow rate of recirculation of the sludge of the clarification step towards the first anaerobic step.
    • PCT No.PCT / FR97 / 01877 Sec。 371日期1999年5月26日 102(e)日期1999年5月26日PCT 1997年10月20日PCT公布。 第WO98 / 23542号公报 日期1998年6月4日该方法测量处理水处理水中可溶性磷浓度至少两个不同处:在二次澄清步骤摄入时,获得测量值P1,并在处理线出口获得 测量P2,测量P1确定在二级澄清的上游进行缺氧或需氧步骤的至少一个罐的液体中沉淀出磷的产物的量。 将测量P2与测量P1连续地进行比较,以便检测在二次澄清水平上磷的可能的盐析。 当注意到这两个测量值(DELTA P1-P2)之间的差异时,出现以下两个措施之一:补充注入沉淀产物,在二次澄清之前,或修改澄清物污泥的再循环流量 迈向第一个厌氧步骤。
    • 3. 发明授权
    • Process for the treatment of liquid effluents by activated sludge
    • 活性污泥处理液体废水的方法
    • US5643453A
    • 1997-07-01
    • US457698
    • 1995-06-01
    • Michele PannierPavel Chudoba
    • Michele PannierPavel Chudoba
    • C02F3/10C02F3/12C02F3/28C02F3/30
    • C02F3/085C02F3/10C02F3/2806Y02W10/15Y10S210/903
    • Process for the treatment of liquid effluents, such as waste water, for the purpose of removal of carbon, nitrogen and phosphorus pollution using an activated sludge, according to which the effluent, after having been subjected to mechanical pretreatments, is brought into contact with the activated sludge. The effluent/activated sludge mixture is the subjected to clarification/settling in order to separate the treated water from the thickened sludge, the latter then being recycled at the head of the aeration treatment and the excess sludge being continuously discharged. An inert material of inorganic origin is injected into the activated sludge, this material being immediately and homogeneously dispersed in the activated sludge, in order to create a mixed culture containing both, and in a single bacterial floc, free heterotrophic species and autotrophic species partially fixed on the particles of the said material within the floc. The structure of the latter contains in the order of 40 to 65% of organic matter, the remainder being the said inert material, consisting of one or a number of particles of the said material surrounded by activated sludge. The extraction of the excess sludge is carried out continuously and without separation of the injected material.
    • 用于使用活性污泥去除碳,氮和磷污染的废水等液体流出物的处理方法,根据该方法,流出物经过机械预处理后与 活性污泥。 废水/活性污泥混合物进行澄清/沉降,以将经处理的水与增稠污泥分离,然后在曝气处理的头部再循环,并且剩余的污泥被连续排出。 将无机起源的惰性材料注入活性污泥中,将该物质立即均匀地分散在活性污泥中,以便产生含有单一细菌絮凝物的单一细菌絮凝物和部分固定的自养物种的混合培养物 在絮凝物中的所述材料的颗粒上。 后者的结构包含有机物质的40至65%的量级,其余为所述惰性材料,由活性污泥包围的所述材料的一个或多个颗粒组成。 多余的污泥的提取是连续进行的,没有分离注入的物质。