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公开(公告)号：US11286507B2
公开(公告)日：2022-03-29
申请号：US14903904
申请日：2014-07-11
Applicant: ANAERGIA INC.
Inventor： Juan Carlos Josse , Andrew Benedek , Michael David Theodoulou
IPC: C12P5/02 , C10B53/02 , C02F11/04 , C02F11/10 , C10K1/06 , C12M1/107 , C12M1/00 , C10K1/04 , C10B47/44
Abstract: 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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公开(公告)号：US20170073261A1
公开(公告)日：2017-03-16
申请号：US15360574
申请日：2016-11-23
Applicant: Anaergia Inc.
Inventor： Juan Carlos Josse , Andrew Benedek , Michael David Thedoulou , Zachary Scott
CPC classification number: C02F9/00 , B01D19/0036 , C02F1/02 , C02F1/20 , C02F3/12 , C02F3/30 , C02F11/04 , C02F11/12 , C02F2101/16 , C02F2103/005 , C05C11/00 , C05F7/00 , C05F17/0018 , C05F17/0027 , C05F17/0045 , Y02A40/213 , Y02P20/145 , Y02W10/15 , Y02W10/23 , Y02W30/43 , Y02W30/47
Abstract: Sludge from an anaerobic digester is treated to recover one or more of fibers, or solids or liquids with a high nutrient content. The solids or liquids can be used as a fertilizer. The fibers can be used in a plant growing medium. Solids are separated from liquids in the sludge and dried. The solids may be dried to produce a flake or pellet. Ammonia in the liquids is recovered and used to produce a concentrated acidic ammonium salt solution. This solution may be mixed with the solids to produce a nitrogen enhanced solid. The fibers and solids or liquids can also be used in combination to produce an enhanced plant growing medium. A device and process for removing ammonia from a liquid can be used in the system or separately.
Abstract translation: 处理来自厌氧消化器的污泥以回收一种或多种具有高营养成分的纤维，或固体或液体。 固体或液体可以用作肥料。 纤维可用于植物生长培养基中。 将固体与污泥中的液体分离并干燥。 固体可以被干燥以产生薄片或颗粒。 回收液体中的氨并用于产生浓缩的酸性铵盐溶液。 该溶液可以与固体混合以产生氮增强的固体。 纤维和固体或液体也可以组合使用以产生增强的植物生长培养基。 用于从液体中除去氨的装置和方法可以在系统中使用或分开使用。
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公开(公告)号：US11787720B2
公开(公告)日：2023-10-17
申请号：US16966569
申请日：2019-02-20
Applicant: ANAERGIA INC.
Inventor： Andrew Benedek , Juan Carlos Josse
IPC: C02F11/04 , B09B3/00 , C02F11/12 , C02F11/125 , C02F101/30
CPC classification number: C02F11/04 , B09B3/00 , C02F11/125 , C02F2101/30 , C02F2303/06 , C02F2303/26
Abstract: Organic solid waste is pressed at a high pressure to separate the solid waste into a dry fraction and a wet fraction. The wet fraction is diluted and floatables (i.e. pieces of plastic and/or paper) in the wet fraction are comminuted. The wet fraction is then de-gritted before being sent to an anaerobic digester. Digestate is withdrawn from the digester from a free liquid surface of the digester. The digestate is filtered to extract comminuted floatables. The resulting filtrate is then composted or directly applied to land. A corresponding system comprises a press, a grinder, a hydrocyclone, an anaerobic digester, a filter and a dewaterer.
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公开(公告)号：US10239776B2
公开(公告)日：2019-03-26
申请号：US15360574
申请日：2016-11-23
Applicant: Anaergia Inc.
Inventor： Juan Carlos Josse , Andrew Benedek , Michael David Thedoulou , Zachary Scott
IPC: C02F9/00 , C02F1/20 , C02F3/12 , C02F7/00 , C02F11/04 , C05F17/00 , C02F3/30 , C02F11/12 , C05C11/00 , C02F1/02 , C05F7/00 , B01D19/00 , C02F101/16 , C02F103/00
Abstract: Sludge from an anaerobic digester is treated to recover one or more of fibers, or solids or liquids with a high nutrient content. The solids or liquids can be used as a fertilizer. The fibers can be used in a plant growing medium. Solids are separated from liquids in the sludge and dried. The solids may be dried to produce a flake or pellet. Ammonia in the liquids is recovered and used to produce a concentrated acidic ammonium salt solution. This solution may be mixed with the solids to produce a nitrogen enhanced solid. The fibers and solids or liquids can also be used in combination to produce an enhanced plant growing medium. A device and process for removing ammonia from a liquid can be used in the system or separately.
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公开(公告)号：US10774470B2
公开(公告)日：2020-09-15
申请号：US15867224
申请日：2018-01-10
Applicant: ANAERGIA INC.
Inventor： Andrew Benedek , Yaniv D. Scherson , Hans Frederick Ouellet , Juan Carlos Josse
Abstract: This specification describes a system and process for treating waste, for example municipal solid waste (MSW) or post-recycling municipal solid waste. The system includes a press and a pulper. The press is adapted to provide a wet fraction of the waste suitable for anaerobic digestion and rejects. The pulper is adapted to receive the rejects and produce pulp. The pulper may be, for example, a drum pulper. In the process, waste is separated into a press into an organic fraction and rejects. The organic fraction is treated by way of anaerobic digestion. The rejects are separated, optionally in a drum pulper, to produce a fraction containing pulp. The pulp can be re-used to make paper or other products. In some case, 70% or more or 80% or more of MSW can be diverted from landfill.
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Patent Agency Ranking
公开(公告)号：US20150027179A1
公开(公告)日：2015-01-29
申请号：US14373714
申请日：2013-01-21
Applicant: ANAERGIA INC.
Inventor： Juan Carlos Josse , Andrew Benedek
CPC classification number: 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
Abstract: 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.
Abstract translation: 为厌氧消化器供给原料，例如来自市政废水处理厂的污泥，并产生消化物。 消化液脱水成蛋糕。 蛋糕可以进一步干燥，例如在热干燥器中。 将蛋糕在热解系统中处理以产生合成气和生物炭。 气体被送到相同或另一个蒸煮器以增加其甲烷产量。 炭可用作土壤增强剂。
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公开(公告)号：US11898308B2
公开(公告)日：2024-02-13
申请号：US16985654
申请日：2020-08-05
Applicant: ANAERGIA INC.
Inventor： Andrew Benedek , Yaniv D. Scherson , Hans Frederick Ouellet , Juan Carlos Josse
CPC classification number: D21B1/345 , B09B3/00 , B09B5/00 , D21B1/026 , D21B1/32 , D21H11/14 , Y02W30/64
Abstract: This specification describes a system and process for treating waste, for example municipal solid waste (MSW) or post-recycling municipal solid waste. The system includes a press and a pulper. The press is adapted to provide a wet fraction of the waste suitable for anaerobic digestion and rejects. The pulper is adapted to receive the rejects and produce pulp. The pulper may be, for example, a drum pulper. In the process, waste is separated into a press into an organic fraction and rejects. The organic fraction is treated by way of anaerobic digestion. The rejects are separated, optionally in a drum pulper, to produce a fraction containing pulp. The pulp can be re-used to make paper or other products. In some case, 70% or more or 80% or more of MSW can be diverted from landfill.
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公开(公告)号：US11890656B2
公开(公告)日：2024-02-06
申请号：US16497407
申请日：2018-03-23
Applicant: ANAERGIA INC.
Inventor： Juan Carlos Josse , Andrew Benedek
Abstract: A system and process for separating organic material from solid waste such as material recovery facility (MRF) fines is disclosed. The fines are treated in a press, in which the fines are compressed against a wall having a set of holes. The fines are mixed with a substantial amount of water before being pressed. The water increases the amount of organic matter that is recovered from the fines. A wet fraction, extruded through the holes of the press, may be treated in an anaerobic digester.
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公开(公告)号：US11613484B2
公开(公告)日：2023-03-28
申请号：US15167324
申请日：2016-05-27
Applicant: ANAERGIA INC.
Inventor： Juan Carlos Josse , Andrew Benedek , Yaniv D. Scherson
IPC: B02C21/00 , B02C13/00 , B30B9/02 , C05F9/04 , C05F7/00 , C02F11/122 , C02F3/28 , B30B9/12 , C02F11/04 , C02F11/125 , B03B9/06
Abstract: Solid waste, for example source separated organics (SSO) or commercial and industrial (C&I) waste or both, are treated by first pressurizing the waste against a screen to produce a solids fraction and a liquid fraction. The liquid fraction can be treated in an anaerobic digester. The solids fraction is pulverized or milled, for example with a hammer mill, preferably after being diluted. The pulverized or milled waste is separated again to provide a second solids faction and a second liquid fraction. The liquid fraction can be treated in an anaerobic digester. The solids fraction is primarily inert and can be landfilled, preferably after being washed.
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公开(公告)号：US09845260B2
公开(公告)日：2017-12-19
申请号：US14877223
申请日：2015-10-07
Applicant: Anaergia Inc.
Inventor： Juan Carlos Josse , Andrew Benedek , Diana Mourato-Benedek
IPC: C02F11/04 , C02F3/28 , C02F9/00 , C02F3/34 , C02F1/28 , C02F1/52 , C02F3/00 , C02F3/12 , C02F3/20 , C02F3/30 , C02F101/16
CPC classification number: 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
Abstract: 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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