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公开(公告)号：EP2603464A4
公开(公告)日：2016-09-07
申请号：EP11815975
申请日：2011-08-12
申请人： ANAERGIA INC
IPC分类号： C02F11/04 , C02F3/28 , C02F3/30 , C02F103/20 , C02F103/22 , C02F103/32
CPC分类号： C02F11/04 , C02F1/28 , C02F1/52 , C02F3/006 , C02F3/1268 , C02F3/1273 , C02F3/208 , C02F3/28 , C02F3/2826 , C02F3/2833 , C02F3/2846 , C02F3/286 , C02F3/2873 , C02F3/302 , C02F3/307 , C02F3/308 , C02F3/34 , C02F9/00 , C02F2101/16 , C02F2209/08 , C02F2209/10 , C02F2209/225 , C02F2303/02 , C02F2303/20 , C02F2303/24 , Y02E50/343 , Y02W10/12 , Y02W10/15 , Y02W10/23
摘要： Low strength wastewater such as municipal sewage is treated using an anaerobic digester. In some examples, a wastewater stream is separated into a solids rich portion and a solids lean portion. The solids lean portion is treated, for example to remove nitrogen. The solids rich portion is treated in an anaerobic digester, preferably with influent or recuperative thickening. In another example, the wastewater stream is fed to an anaerobic digester and solid-liquid separation stages downstream of the digester return active bacteria and undigested organics to the digester. Both cases may use a process train comprising treatment in an anoxic tank followed by a nitritation tank with a portion of the effluent from the nitritation tank recirculated to the anoxic tank to provide nitritation and denitritation.
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公开(公告)号：EP2788290A4
公开(公告)日：2015-07-29
申请号：EP12856462
申请日：2012-12-04
申请人： ANAERGIA INC
CPC分类号： C02F3/12 , B01D33/06 , B01D33/48 , C02F1/52 , C02F3/006 , C02F3/1215 , C02F3/30 , C02F2209/42 , C02F2303/24 , Y02W10/15
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公开(公告)号：EP2807123A1
公开(公告)日：2014-12-03
申请号：EP13740592.4
申请日：2013-01-21
申请人： Anaergia Inc.
IPC分类号： C02F11/04 , B01D53/84 , C01B3/02 , C01B3/22 , C02F11/10 , C02F3/00 , C10J3/72 , C12M1/04 , C12P5/02
CPC分类号： C12P5/023 , C02F3/12 , C02F3/28 , C02F3/2893 , C02F11/04 , C02F11/10 , C02F11/12 , C02F11/121 , C02F2203/00 , C05D9/00 , C05F11/00 , C10B53/00 , C10B53/02 , C10K1/04 , Y02E50/14 , Y02E50/343 , Y02P20/145 , Y02W10/40 , Y02W30/47 , Y10T137/85978
摘要： An anaerobic digester is fed a feedstock, for example sludge from a municipal wastewater treatment plant, and produces a digestate. The digestate is dewatered into a cake. The cake may be dried further, for example in a thermal drier. The cake is treated in a pyrolysis system to produce a synthesis gas and biochar. The gas is sent to the same or another digester to increase its methane production. The char may be used as a soil enhancer.
摘要翻译： 向厌氧消化器供给原料，例如来自市政污水处理厂的污泥，并且产生消化物。 消化液被脱水成蛋糕。 例如可以在热干燥器中进一步干燥滤饼。 该饼在热解系统中处理以产生合成气和生物炭。 气体被送到同一个或另一个沼气池以增加其沼气产量。 炭可以用作土壤增强剂。
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公开(公告)号：EP2398743A1
公开(公告)日：2011-12-28
申请号：EP10743360.9
申请日：2010-02-18
申请人： Anaergia Inc.
发明人： BENEDEK, Andrew
CPC分类号： C02F11/04 , B01D61/145 , B01D61/147 , B01D61/18 , B01D2311/04 , B01D2311/25 , B01D2311/2642 , B01D2311/2649 , B01D2315/06 , C02F3/2853 , C02F11/121 , C02F2103/20 , C02F2203/004 , C12M21/04 , C12M33/00 , C12P5/023 , Y02E50/343
摘要： A process and apparatus for the anaerobic digestion of organic wastes, preferably to also produce a useful biogas, is described. The waste may have a total solids (TS) concentration of 6% or less while a digester is operated at a higher solids concentration, for example with a feed TS concentration of 8- 12%. One or more separation stages downstream of the digester separate active bacteria and undigested orgaπics from the digestate, and return separated matter to the digester. Optionally, a feed thickening apparatus and step may be provided upstream of the digester. The upstream thickener and recycle form the downstream separation stages are operated such that the TS of the combined inputs to the digester is within a desired range.
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公开(公告)号：EP3215464A1
公开(公告)日：2017-09-13
申请号：EP15857098.6
申请日：2015-11-06
申请人： Anaergia Inc.
CPC分类号： C02F1/20 , B01D19/0015 , C02F1/02 , C02F3/28 , C02F2101/16 , C02F2201/002
摘要： An ammonia stripper has an aerator and heat exchanger tubing in a tank. The aerator and coil are preferably attached to a frame to form a removable cassette. The cassette may also include a lid for the tank. The tank is preferably rectangular and optionally can be made with the dimensions of a standard shipping container. In a process, water flows through the tank while air bubbles are produced through the aerator. A heating medium such as water flows through the heat exchanger tubing. A gas containing ammonia is withdrawn from a headspace of the tank.
摘要翻译： 氨汽提器在罐中具有充气器和热交换器管。 充气器和线圈优选地连接到框架以形成可移除的盒。 盒子还可以包括用于罐的盖子。 该罐优选是矩形的并且可选地可以用标准运输容器的尺寸制造。 在一个过程中，当气泡通过曝气器产生时，水流过水箱。 诸如水之类的加热介质流过热交换器管道。 含有氨的气体从罐的顶部空间排出。
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公开(公告)号：EP2807123A4
公开(公告)日：2015-08-26
申请号：EP13740592
申请日：2013-01-21
申请人： ANAERGIA INC
发明人： JOSSE JUAN CARLOS , BENEDEK ANDREW
IPC分类号： C02F11/04 , B01D53/84 , C01B3/02 , C01B3/22 , C02F3/00 , C02F11/10 , C10J3/72 , C12M1/04 , C12P5/02
CPC分类号： C12P5/023 , C02F3/12 , C02F3/28 , C02F3/2893 , C02F11/04 , C02F11/10 , C02F11/12 , C02F11/121 , C02F2203/00 , C05D9/00 , C05F11/00 , C10B53/00 , C10B53/02 , C10K1/04 , Y02E50/14 , Y02E50/343 , Y02P20/145 , Y02W10/40 , Y02W30/47 , Y10T137/85978
摘要： An anaerobic digester is fed a feedstock, for example sludge from a municipal wastewater treatment plant, and produces a digestate. The digestate is dewatered into a cake. The cake may be dried further, for example in a thermal drier. The cake is treated in a pyrolysis system to produce a synthesis gas and biochar. The gas is sent to the same or another digester to increase its methane production. The char may be used as a soil enhancer.
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