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    • 3. 发明授权
    • Method for the treatment of liquids on granular materials
    • 颗粒材料处理液体的方法
    • US4659476A
    • 1987-04-21
    • US797813
    • 1985-11-13
    • Jean BurriatBernard CausseJean-Marie Rovel
    • Jean BurriatBernard CausseJean-Marie Rovel
    • B01J47/02B01J49/00B01J49/02C02F1/42
    • C02F1/42B01J47/026B01J49/0078B01J49/02
    • A method for the treatment of liquids containing particles in suspension, by percolation of the liquid from top to bottom through a bed of granular material, notably of a ion exchanger resin, includes treatment cycles of the liquid and regeneration cycles of the resin, preceded by decompaction and washing operations, carried out in the same enclosure the inner space of which is divided into two superimposed compartments in mutual communication. The lower compartment is totally filled with granular material and the upper compartment is partly filled with granular material. The decompaction and washing operations of the granular material contained in the enclosure upper compartment are carried out periodically prior to each regeneration cycle by expanding the granular material by means of a current of liquid flowing from bottom to top.
    • 一种用于处理悬浮液中含有颗粒的液体的方法,通过从顶部到底部通过颗粒材料床(特别是离子交换树脂)渗滤液体,包括液体的处理循环和树脂的再生循环,之前是 分解和洗涤操作,在相同的外壳中进行,其内部空间被分成两个相互通信的叠加隔间。 下隔室完全充满颗粒状物料,上隔室部分填满粒状物料。 通过从底部向上流动的液体流膨胀粒状材料,在每个再生循环之前,周期性地进行容纳在外壳上部隔室中的粒状材料的分解和洗涤操作。
    • 6. 发明授权
    • Method for sewage treatment
    • 污水处理方法
    • US5798044A
    • 1998-08-25
    • US513869
    • 1995-09-15
    • Andreas StrohmeierIngulf SchroeterJean-Marie Rovel
    • Andreas StrohmeierIngulf SchroeterJean-Marie Rovel
    • C02F3/06C02F3/12C02F3/28C02F3/30
    • C02F3/1215C02F3/06C02F3/2806C02F3/30C02F3/302Y02W10/15Y10S210/903Y10S210/906
    • Described is a two-stage sewage treatment plant (10), in particular for domestic sewage, wherein the first biological purification stage (12) is dimensioned so that besides the carbon load, the mean nitrogen load is maximally degraded. Any peak loads that may appear are degraded in the second biological purification stage (13). This makes possible a space-saving construction and an economical operation. The second biological purification stage (13) is always a two-stage filtering installation with a filter stage (20) for nitrification and a filter stage (21) for denitrification. The first biological purification stage (12) can be an activated sludge stage as per A 131, a pure oxygen activated sludge or likewise a two-stage filtering installation.
    • PCT No.PCT / EP94 / 00765 Sec。 371 1995年9月15日第 102(e)1995年9月15日PCT PCT 1994年3月11日PCT公布。 出版物WO94 / 21568 日期1994年9月29日描述的是一个两级污水处理厂(10),特别是生活污水,其中第一个生物净化阶段(12)的尺寸使得除了碳负荷之外,平均氮负荷最大程度地降低。 可能出现的任何峰值负荷在第二生物净化阶段(13)中降解。 这使得节省空间的建筑和经济运行成为可能。 第二个生物净化阶段(13)始终是一个两级过滤装置,具有用于硝化的过滤段(20)和用于脱氮的过滤段(21)。 第一个生物净化阶段(12)可以是根据A 131的活性污泥阶段,纯氧活性污泥或类似于两级过滤装置。
    • 7. 发明授权
    • Process for the biological purification of effluent
    • 污水生物净化工艺
    • US5348653A
    • 1994-09-20
    • US951012
    • 1992-09-25
    • Jean-Marie Rovel
    • Jean-Marie Rovel
    • C02F3/12C02F3/02C02F3/06C02F3/28C02F3/34C02F9/00C02F3/30
    • C02F3/02C02F3/06C02F3/2806Y02W10/15Y10S210/903Y10S210/921
    • Process for the biological purification of effluent which makes it possible either to ensure complete treatment of the carbon pollution and the nitrogen pollution at the nominal output, or to remove the biological oxygen demand or BOD only during a substantial increase in the nominal output, especially if it rains, using bacteria in fixed cultures, said process comprising the step of using the modifications of the surrounding environment, that is to say the oxidation-reduction potential which depends on the presence or absence of dissolved oxygen, and the composition of the water in contact with the bacteria, either to modify the enzymatic system of the flora present in the bacterial film of the fixed culture in order to assign to the removal of the BOD a fixed culture which up until then carried out denitrification, or to promote, in the same bacterial film, the development of the most appropriate flora for the desired objective: the removal of the BOD or nitrification.
    • 流出物的生物净化方法使得有可能确保在名义产量下完全处理碳污染和氮污染,或仅在名义产量大幅度增加时除去生物需氧量或BOD,特别是如果 下雨,在固定培养物中使用细菌,所述方法包括使用周围环境的改变的步骤,也就是说取决于溶解氧的存在或不存在的氧化还原电位,以及水的组成 与细菌接触,以改变固定培养物的细菌膜中存在的菌群的酶系,以便指定去除BOD的固定培养物,直至进行脱氮,或者在 相同的细菌膜,开发最合适的菌群为期望的目标:去除BOD或硝化。
    • 8. 发明授权
    • Process and apparatus for treating by ion exchange or adsorption fluids
having solid particles suspended therein
    • 用固体颗粒悬浮在其中的离子交换剂或吸附液进行处理的方法和装置
    • US4269715A
    • 1981-05-26
    • US99719
    • 1979-12-03
    • Christian BarraqueJean BurriatJean-Marie Rovel
    • Christian BarraqueJean BurriatJean-Marie Rovel
    • B01D15/04B01J49/00
    • B01J49/0078
    • A treatment column includes a treatment zone which is completely filled with a bed of granular treatment material. A normal treatment operation includes passing a fluid to be treated in a downward direction through the bed of treatment material, thereby treating the fluid. Solid particles suspended in the fluid are removed by the upper portion of the bed of treatment material and are retained therein. Regeneration of the bed is achieved in a countercurrent direction within the treatment column. Retained solid particles are removed from the upper portion of the bed by periodically removing the upper portion only of the bed from the treatment column and transferring such upper portion to a separate washing column whereat the portion of the bed is cleaned and washed. The thus cleaned and washed treatment material is then returned to the upper portion of the treatment zone within the treatment column to replenish the bed.
    • 处理塔包括完全填充有颗粒状处理材料床的处理区域。 正常的处理操作包括使待处理的流体沿向下的方向通过处理材料床,从而处理流体。 悬浮在流体中的固体颗粒被处理材料床的上部除去并保留在其中。 床的再生在处理塔内以逆流方向实现。 通过从处理塔周期性地除去床的上部并将这样的上部转移到单独的洗涤塔上,将床的部分清洁和洗涤,从床的上部除去保留的固体颗粒。 然后将如此清洁和洗涤的处理材料返回到处理塔内的处理区的上部,以补充床。