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    • 61. 发明授权
    • Waste water treatment method
    • 废水处理方法
    • US07510656B2
    • 2009-03-31
    • US11685663
    • 2007-03-13
    • Lee L. ShaferJohn W. JamesRichard D. RathJesse Eubank
    • Lee L. ShaferJohn W. JamesRichard D. RathJesse Eubank
    • C02F3/00
    • C02F9/00C02F1/001C02F1/24C02F1/42C02F1/441C02F3/1268C02F3/30C02F2103/365Y02W10/15
    • Systems and methods have been developed for reclaiming water contaminated with the expected range of contaminants typically associated with produced water, including water contaminated with slick water, methanol and boron. The system includes anaerobically digesting the contaminated water, followed by aerating the water to enhance biological digestion. After aeration, the water is separated using a flotation operation that effectively removes the spent friction reducing agents and allows the treated water to be reclaimed and reused as fracturing water, even though it retains levels of contaminants, including boron and methanol, that would prevent its discharge to the environment under existing standards. The treated water may further be treated by removing the methanol via biological digestion in a bioreactor, separating a majority of the contaminants from the water by reverse osmosis and removing the boron that passes through the reverse osmosis system with a boron-removing ion exchange resin.
    • 已经开发了系统和方法,用于回收被生产水所包含的污染物的预期范围污染的水,包括被光滑的水,甲醇和硼污染的水。 该系统包括厌氧消化污染的水,然后充气水以增强生物消化。 曝气后,使用浮选操作分离水分,该浮选操作有效地除去废摩擦还原剂,并允许处理后的水回收再利用作为压裂水,即使其保留了包括硼和甲醇在内的污染物含量,防止其 在现有标准下排放到环境中。 处理过的水可以通过生物反应器中的生物消化除去甲醇来进一步处理,通过反渗透将大部分污染物从水中分离出来,并用去除硼的离子交换树脂除去通过反渗透系统的硼。
    • 63. 发明申请
    • INTERMITTENT ANAEROBIC BIOLOGICAL TREATMENTS OF RAINFALL-INDUCED SEWERAGE
    • 干扰诱导的海洋生物的干扰生物处理
    • US20090008324A1
    • 2009-01-08
    • US12061330
    • 2008-04-02
    • Dennis J. LongJeffrey M. Lauria
    • Dennis J. LongJeffrey M. Lauria
    • C02F3/30
    • C02F3/30C02F2103/001
    • The present invention relates to the application of the biological adsorption and biological oxidation ability of both conventional wastewater treatment biological selection technology and, if desired, chemically-enhanced wastewater treatment biological selection technology to remove pollutants from precipitation-generated flows collected by a combined sanitary sewer system, a separate sanitary sewer system, and/or a combination of both systems for: (1) the biological adsorption and oxidation of suspended and dissolved pollutants as measured by standard methods tests for carbonaceous biochemical oxygen demand, and/or (2) the biological adsorption of all other dissolved non-conservative and conservative pollutants as measured by all other standard methods tests for such pollutants.
    • 本发明涉及常规废水处理生物选择技术的生物吸附和生物氧化能力的应用,并且如果需要,化学增强废水处理生物选择技术,以从组合卫生下水道收集的沉淀产生的流中除去污染物 系统,单独的卫生下水道系统和/或两种系统的组合,用于:(1)通过标准方法测定的碳质生化需氧量的悬浮和溶解污染物的生物吸附和氧化,和/或(2) 所有其他溶解的非保守和保守污染物的生物吸附通过所有其他标准方法测试这些污染物测量。
    • 64. 发明授权
    • Waste effluent treatment system
    • 废水处理系统
    • US07445707B2
    • 2008-11-04
    • US10908428
    • 2005-05-11
    • Thomas MenkeDavid Ricke
    • Thomas MenkeDavid Ricke
    • C02F3/00
    • C02F3/00C02F3/30
    • A waste treatment system that removes as much of the inorganic and organic solids as possible prior to treating the collected waste material in treatment lagoons. First, inorganic solids, such as sand, are removed, if needed. Then coarse solids are removed, including manure and other organic material such as straw. After removal of inorganic and coarse solids, additional fine solids are removed through two settling basins. For example, after coarse solids separation and fine solids separation, the solids concentration has been reduced by over 80%. Preferably, the coarse solids separation and fine solids separation has reduced size requirements of the treatment lagoons to accommodate an organic loading, as total volatile solids, between 0.00253 lb/ft3 of lagoon volume/day×K and 0.0105 lb/ft3 of lagoon volume/day×K, where K varies from about 0.4 to about 1.2. Finally, the remaining liquid is treated in the treatment lagoons.
    • 废物处理系统在处理处理泻湖内收集的废料之前,尽可能地去除无机和有机固体。 首先,如果需要,除去无机固体,如沙子。 然后除去粗固体,包括粪便和其他有机材料如稻草。 除去无机和粗固体后,通过两个沉淀池除去另外的细小固体。 例如,粗固体分离和细分固体分离后,固体浓度降低了80%以上。 优选地,粗固体分离和细固体分离对处理泻湖的尺寸要求减小,以适应作为总挥发性固体的有机负荷,其为盐水湖体积/ dayxK的0.00253磅/平方英尺和0.0105磅 / ft 3的泻湖体积/ dayxK,其中K从约0.4变化到约1.2。 最后,在处理泻湖处理剩余的液体。
    • 66. 发明申请
    • Method and Arrangement for Processing Nitrogen-Concentrated Effluents in a Sequential Fractionated Cycle Biological Reactor
    • 在连续分馏循环生物反应器中加工氮浓缩流出物的方法和装置
    • US20080223784A1
    • 2008-09-18
    • US11997337
    • 2006-07-27
    • Samuel MartinAdriana Gonzalez Ospina
    • Samuel MartinAdriana Gonzalez Ospina
    • C02F3/30C12M1/34C12M1/36
    • C02F1/008C02F3/1263C02F3/30C02F2101/16C02F2103/06C02F2103/18Y02W10/15Y10S210/903
    • The invention relates to a method for processing nitrogen-concentrated effluents by ammonia oxidation into nitrites followed by nitrite denitritation in a gaseous nitrogen in a sequential biological reactor (1) consisting in pouring a processable effluent volume in to the reactor by successive volume fractions, in dividing the entire processing cycle into successive sub cycles, wherein each sub-cycle comprises a feeding phase, an aeration phase for nitrification and an anoxia phase along which a carbon-containing source is introduced into the reactor for converting nitrites into nitrogen. The inventive method also consists in evaluating a nitrogenous volume charge in the effluent to be processed, mainly by measuring the effluent conductivity (X) and the flow rate (Q) and in determining the number of feeding phases of the entire cycle according to nitrogenous charge and to a minimum volume of liquid in the reactor in such a way that an injected nitrogen concentration is diluted in the liquid volume, wherein the volume phase nitrogenous charge is however sufficient for producing a single shot or peak of the ammonia charge favourable for a nitrating biomass formation in the reactor.
    • 本发明涉及一种通过氨氧化将氮浓缩废水加工成亚硝酸盐,然后在连续生物反应器(1)中的气态氮中进行亚硝酸盐脱硝处理的方法,该方法包括将连续体积分数的可加工出水体积倒入反应器中, 将整个处理循环分成连续的子循环,其中每个子循环包括进料阶段,用于硝化的通气阶段和缺氧阶段,将含碳源引入反应器中以将亚硝酸盐转化为氮气。 本发明的方法还包括评估待处理流出物中的含氮体积电荷,主要通过测量流出物导电率(X)和流速(Q)以及根据含氮电荷确定整个循环的进料阶段数 并且以这样的方式使反应器中的最小体积的液体以注入的氮浓度在液体体积中稀释,其中,体积相含氮电荷足以产生有利于硝化的氨充电的单次或峰值 反应器中生物质的形成。