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公开(公告)号:US3589313A
公开(公告)日:1971-06-29
申请号:US3589313D
申请日:1968-08-30
Applicant: US HEALTH EDUCATION & WELFARE
Inventor: SMITH RICHARD D , FURLONG DALE A , KINSEY RONALD D
CPC classification number: F23G5/027 , B03B9/06 , F23G5/30 , F23G5/46 , F23G2201/10 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23G2201/80 , F23G2202/30 , F23G2206/20 , F23G2206/203 , F23G2900/54601 , F23J2217/102 , F23J2217/40 , Y02E20/12 , Y02W30/521 , Y02W30/527
Abstract: A solid waste disposal system is described with a storage and receiving carousel, a shredder, a dryer, a compressor-turbine assembly for compressing air for combustion of waste and for receiving hot gasses produced in the combustion process. Two combustion systems, a fluid bed reactor and a gasifying pyrolyzer, are described. Particulate matter harmful to the turbine and also causing air pollution is removed from the hot high pressure gas upstream of the turbine. The malodorous air from the waste storage, shredding and drying is compressed and used for combustion and the part of the hot exhaust gases from the turbine are used in the dryer.
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公开(公告)号:US20240353099A1
公开(公告)日:2024-10-24
申请号:US18434709
申请日:2024-02-06
Applicant: Bernardo del Campo
Inventor: Bernardo del Campo
IPC: F23G5/46 , C10J3/00 , C10J3/82 , F23G5/00 , F23G5/027 , F23G5/04 , F23G5/16 , F23G5/44 , F23G7/00
CPC classification number: F23G5/46 , C10J3/002 , C10J3/82 , F23G5/006 , F23G5/0273 , F23G5/04 , F23G5/16 , F23G5/444 , C10J2200/09 , C10J2200/15 , C10J2300/0909 , C10J2300/0916 , C10J2300/1606 , C10J2300/1671 , F23G5/0276 , F23G7/001 , F23G2201/10 , F23G2201/301 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23G2205/121 , F23G2206/10 , F23G2206/203 , F23G2209/26 , F23G2900/50201 , Y02E20/12 , Y02P20/145
Abstract: A thermochemical system & method may be configured to convert an organic feedstock to various products. A thermochemical system may include a solid material feed module, a reactor module, an afterburner module, and a solid product finishing module. The various operational parameters (temperature, pressure, etc.) of the various modules may vary depending on the desired products. The product streams may be gaseous, vaporous, liquid, and/or solid.
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公开(公告)号:US11892163B2
公开(公告)日:2024-02-06
申请号:US17165843
申请日:2021-02-02
Applicant: Bernardo del Campo
Inventor: Bernardo del Campo
IPC: F23G5/46 , C10J3/82 , F23G5/00 , F23G5/04 , F23G5/44 , C10J3/00 , F23G5/027 , F23G5/16 , F23G7/00
CPC classification number: F23G5/46 , C10J3/002 , C10J3/82 , F23G5/006 , F23G5/0273 , F23G5/04 , F23G5/16 , F23G5/444 , C10J2200/09 , C10J2200/15 , C10J2300/0909 , C10J2300/0916 , C10J2300/1606 , C10J2300/1671 , F23G5/0276 , F23G7/001 , F23G2201/10 , F23G2201/301 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23G2205/121 , F23G2206/10 , F23G2206/203 , F23G2209/26 , F23G2900/50201 , Y02E20/12 , Y02P20/145
Abstract: A thermochemical system & method may be configured to convert an organic feedstock to various products. A thermochemical system may include a solid material feed module, a reactor module, an afterburner module, and a solid product finishing module. The various operational parameters (temperature, pressure, etc.) of the various modules may vary depending on the desired products. The product streams may be gaseous, vaporous, liquid, and/or solid.
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公开(公告)号:US09951946B2
公开(公告)日:2018-04-24
申请号:US14346683
申请日:2012-09-21
Applicant: Weiqi Liu
Inventor: Weiqi Liu
CPC classification number: F23G5/38 , F23G5/0276 , F23G5/04 , F23G5/16 , F23G5/46 , F23G7/10 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23G2202/101 , F23G2202/60 , F23G2206/10 , F23G2206/203 , F23G2209/26 , F23G2900/50002 , Y02E20/12 , Y02E20/344
Abstract: A high-efficiency clean burning method of a macromolecular substance, wherein the macromolecular substance comprises biomass and solid organic waste; the method comprises the following steps: generating a first gaseous substance and a red-hot carbon residue layer from biomass carbon residue or charcoal or coke or a mixture thereof by anoxic combustion; leading the heat generated by anoxic combustion to the macromolecular substance, preheating and drying the macromolecular substance and carrying out pyrolysis gasification, so as to generate a second gaseous substance; taking red-hot carbon residue as a pyrolysis catalyst, leading the second gaseous substance to the red-hot carbon residue layer to carry out oxygen catalytic cracking, so as to generate a third gaseous substance; leading the third gaseous substance and the first gaseous substance to an oxygen-enriched combustion zone in a heat preservation manner to carry out oxygen-enriched combustion, so as to achieve substantial complete combustion of all gasification products, wherein a tar wastewater is not generated, and pollution of smoke tar is not generated. A device capable of achieving the method comprises four categories of a plurality of devices. Thus, zero emission of “dioxin” can be achieved when the device is applied to waste incineration disposal.
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公开(公告)号:US09648808B2
公开(公告)日:2017-05-16
申请号:US14866971
申请日:2015-09-27
Applicant: Jason Force
Inventor: Jason Force
IPC: C10L5/40 , A01D43/00 , F23G5/027 , F23G5/40 , F23G7/10 , A01D34/00 , A01D43/06 , A01D43/08 , A01D34/04 , A01D43/063 , A01D43/10
CPC classification number: A01D43/006 , A01D34/008 , A01D34/04 , A01D43/00 , A01D43/003 , A01D43/06 , A01D43/063 , A01D43/0633 , A01D43/08 , A01D43/086 , A01D43/10 , A01D61/008 , F23G5/027 , F23G5/40 , F23G7/10 , F23G2201/303 , F23G2203/601 , F23G2206/202 , F23G2206/203 , F23G2209/262 , Y02E20/12 , Y02E50/30 , Y10S901/01
Abstract: A mobile platform biomass harvester has a header, a biomass processor, a storage container, a guidance system, an engine, an electric generator, and a guidance system. The header harvests biomass. The biomass processor includes a shredder, a press, a dryer, and a densifier. The densifier compacts the biomass into a multitude of compressed biomass pieces. The storage container receives compressed biomass pieces from the biomass processor. The guidance system guides the mobile platform at a speed determined by the operating capacity of the mobile platform. The engine generates shaft power. The electrical generator converts the shaft power to electricity to power the guidance system.
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公开(公告)号:US09551277B2
公开(公告)日:2017-01-24
申请号:US13825120
申请日:2011-09-19
Applicant: James C. Juranitch
Inventor: James C. Juranitch
IPC: F02C3/20 , B01D53/10 , F23G5/00 , C10J3/18 , F23J15/00 , C10J3/84 , F23G5/46 , F22B1/18 , F22B37/00
CPC classification number: F02C3/20 , B01D53/10 , B01D2257/2045 , B01D2257/302 , B01D2257/404 , B01D2257/602 , B01D2258/0283 , C10J3/18 , C10J3/84 , C10J2200/12 , C10J2300/0946 , C10J2300/0996 , C10J2300/1238 , C10J2300/1606 , C10J2300/1653 , C10J2300/1869 , C10J2300/1876 , F02C6/18 , F02C9/20 , F05D2220/32 , F05D2220/72 , F22B1/18 , F22B37/008 , F23G5/006 , F23G5/46 , F23G2201/303 , F23G2201/40 , F23G2201/701 , F23G2201/80 , F23G2202/106 , F23G2204/201 , F23G2206/202 , F23G2206/203 , F23J15/006 , F23J15/025 , F23J2215/10 , F23J2215/20 , F23J2217/104 , F23J2219/60 , Y02E20/12 , Y02E20/16 , Y02E20/18 , Y02P20/129 , Y02P20/13 , Y02P20/133
Abstract: A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into to a feedwater energy transfer system. The feedstock can be any organic material, or fossil fuel. The energy transferred in the feedwater is converted into steam which is then injected into the low turbine of a combined cycle power plant. Heat is extracted from gas product issued by a gassifier and delivered to a power plant via its feedwater system. The gassifier is a plasma gassifier and the gas product is syngas. In a further embodiment, prior to performing the step of extracting heat energy, there is provided the further step of combusting the syngas in an afterburner. An air flow, and/or EGR flow is provided to the afterburner at a rate that is varied in response to an operating characteristic of the afterburner. The air flow to the afterburner is heated.
Abstract translation: 一种用于使用热等离子体或其它类型的放气器将原料成本有效地转化为给水能量转移系统的方法和系统。 原料可以是任何有机材料或化石燃料。 在给水中转移的能量被转化为蒸汽,然后将其注入到联合循环发电厂的低涡轮机中。 热气从放气器发出的气体产品中提取,并通过其给水系统输送到发电厂。 放气器是等离子体放气器,气体产物是合成气。 在另一个实施方案中,在进行提取热能的步骤之前,提供了在加力燃烧器中燃烧合成气的另外的步骤。 空气流和/或EGR流以响应加力燃烧器的操作特性而变化的速率提供给加力燃烧器。 加热到加力燃烧器的空气流。
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公开(公告)号:US09534510B2
公开(公告)日:2017-01-03
申请号:US13161257
申请日:2011-06-15
Applicant: Donald F. Kerr , Jonathan D. Kerr , Roger L. Kolb , C. Lloyd Mahaffey, Jr.
Inventor: Donald F. Kerr , Jonathan D. Kerr , Roger L. Kolb , C. Lloyd Mahaffey, Jr.
CPC classification number: F23G5/165 , F01K13/00 , F01K25/10 , F23G5/0276 , F23G5/16 , F23G5/46 , F23G5/50 , F23G2201/303 , F23G2201/701 , F23G2203/107 , F23G2203/20 , F23G2203/30 , F23G2203/60 , F23G2203/601 , F23G2205/122 , F23G2206/203 , F23G2207/20 , F23G2207/30 , F23G2900/55006 , F23G2900/55008 , Y02E20/12
Abstract: A waste-to-energy conversion apparatus comprising a primary combustion chamber capable of holding a load of waste, and the primary combustion chamber further comprises a heat source to heat the waste and generate a syn gas stream, grates, within the primary chamber, capable of supporting the load of waste during heating, a mixing chamber wherein the syn gas is mixed with additional combustion gas, a multi-chambered secondary combustion chamber for combusting the mixture of syn gas and additional combustion gas, and an energy extraction system for extracting the heat energy generated by the combustion of the mixture of syn gas and additional combustion gas.
Abstract translation: 一种废能转换装置,包括能够保持废物负载的初级燃烧室,并且所述主燃烧室还包括热源以加热废物并在所述主室内产生合流气流,所述合流气流能够 在加热期间支撑废物的负荷,混合室,其中合成气与另外的燃烧气体混合,多室二次燃烧室,用于燃烧合成气和其它燃烧气体的混合物;以及能量提取系统,用于提取 由合成气和其他燃烧气体的混合物的燃烧产生的热能。
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公开(公告)号:US20160304786A1
公开(公告)日:2016-10-20
申请号:US15196645
申请日:2016-06-29
Applicant: Frank Reed
Inventor: Frank Reed
CPC classification number: C10B53/07 , C01B3/02 , C10B7/10 , C10B21/12 , C10B27/06 , C10B47/44 , C10K3/06 , F01K5/02 , F23G5/0276 , F23G7/12 , F23G2201/301 , F23G2201/303 , F23G2203/8013 , F23G2209/281 , F23J1/06 , Y02P20/143
Abstract: Systems and methods are disclosed for pyrolysis of waste feed material. Some systems include a main retort and a secondary retort. Syngas is produced by pyrolysis in the main retort, and is then mixed with combustion air and ignited, in some cases to produce energy. Carbon char travels to the secondary retort and is exhausted from the system through an airlock.
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公开(公告)号:US09422478B2
公开(公告)日:2016-08-23
申请号:US13810405
申请日:2011-07-08
Applicant: Paolo Palmas , Paul A. Sechrist , Sid Kulprathipanja , Stanley J. Frey , Barry Freel , Daniel N. Myers , Vincenza Myers
Inventor: Paolo Palmas , Paul A. Sechrist , Sid Kulprathipanja , Stanley J. Frey , Barry Freel , Daniel N. Myers
IPC: F23B90/00 , C10B23/00 , C10B49/22 , C10B53/02 , C10C5/00 , C10K1/02 , F23G5/027 , F23G5/30 , F23G5/46 , F23G5/50 , F23G7/10
CPC classification number: C10B23/00 , C10B49/22 , C10B53/02 , C10C5/00 , C10K1/026 , F23G5/0273 , F23G5/30 , F23G5/46 , F23G5/50 , F23G7/10 , F23G2201/303 , F23G2201/304 , F23G2201/601 , F23G2206/10 , F23G2900/50205 , Y02E50/14 , Y02P20/133 , Y02P20/145 , Y02P30/20
Abstract: Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.
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公开(公告)号:US09394484B2
公开(公告)日:2016-07-19
申请号:US14105832
申请日:2013-12-13
Applicant: Frank Reed
Inventor: Frank Reed
CPC classification number: C10B53/07 , C01B3/02 , C10B7/10 , C10B21/12 , C10B27/06 , C10B47/44 , C10K3/06 , F01K5/02 , F23G5/0276 , F23G7/12 , F23G2201/301 , F23G2201/303 , F23G2203/8013 , F23G2209/281 , F23J1/06 , Y02P20/143
Abstract: Systems and methods are disclosed for pyrolysis of waste feed material. Some systems include a main retort and a secondary retort. Syngas is produced by pyrolysis in the main retort, and is then mixed with combustion air and ignited, in some cases to produce energy. Carbon char travels to the secondary retort and is exhausted from the system through an airlock.
Abstract translation: 公开了用于废料进料的热解的系统和方法。 一些系统包括主蒸馏器和次蒸馏器。 合成气通过主蒸馏器中的热解产生,然后与燃烧空气混合并点燃,在某些情况下产生能量。 碳炭运送到二级蒸馏器,并通过气闸从系统中排出。
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