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公开(公告)号：EP4405443A1
公开(公告)日：2024-07-31
申请号：EP22873443.0
申请日：2022-09-16
Applicant: Eastman Chemical Company
Inventor： POLASEK, Michael, Gary , BITTING, Daryl , WU, Xianchun , SLIVENSKY, David, Eugene , ANDERSON, Avery, L.
IPC: C10G1/10 , F23G5/027 , F23G5/46 , B09B3/40 , B09B101/75
CPC classification number: Y02P20/143 , B09B2101/7520220101 , B09B3/40 , C10G1/10 , F23G5/027 , C10G1/002 , C10G9/36 , F23G5/006 , F23G2209/2820130101
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公开(公告)号：EP2706296A3
公开(公告)日：2018-06-27
申请号：EP13184015.9
申请日：2013-09-11
Applicant: VT Innovations Limited
Inventor： Finnin, Gerard
CPC classification number: F23G5/006 , F23G5/02 , F23G5/46 , F23G2201/303 , F23G2201/304 , F23G2201/601 , F23G2201/603 , F23G2206/202 , F23G2206/203 , Y02E20/12
Abstract: The present invention is directed towards an apparatus and method for harnessing energy from waste materials (102) using a pyrolysis assembly, whereby the pyrolysis assembly comprises a pre-pyrolysis treatment plant (104), a pyrolysis plant (120), and, a fuel-based energy plant(136). Waste materials having at least 30% biomass by weight are fed into the pre-pyrolysis treatment plant and the biomass is separated from the waste materials in the pre-pyrolysis treatment plant. The biomass is chemically cracked into at least a char and a gas in the pyrolysis plant and this char and gas is used by the fuel-based energy plant to harness energy from the waste materials. Problems associated with the efficiency of pre-pyrolysis treatment plants and safety of the parts used in the pre-pyrolysis treatment plants is addressed in the current invention
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公开(公告)号：EP2870221B1
公开(公告)日：2017-12-20
申请号：EP13813352.5
申请日：2013-07-05
Applicant: Teknologian tutkimuskeskus VTT Oy , Valmet Technologies Oy
Inventor： LEHTO, Jani
CPC classification number: C10B21/18 , C10B27/00 , C10B49/22 , C10B53/02 , C10B57/06 , C10K1/026 , C10K1/04 , F23G5/006 , F23G5/027 , F23G5/16 , F23G5/30 , F23G7/10 , F23G2201/303 , F23G2201/304 , Y02E50/14
Abstract: The invention relates to a method and apparatus for producing a pyrolysis product, in which raw material are fed to the pyrolysis reactor and gaseous pyrolysis product fractions and by-product fractions are formed from raw material by pyrolysis in a pyrolysis reactor. According to the invention the method comprising steps: combusting at least one by-product fraction from the pyrolysis reactor in at least two combustors, and recovering energy formed in the combustor.
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公开(公告)号：EP3245016A1
公开(公告)日：2017-11-22
申请号：EP16737744.9
申请日：2016-01-12
Applicant: Aemerge LLC
Inventor： BEHRENS, Scott , MILLER, Landon C.G.
CPC classification number: B02C19/0075 , B02C18/2241 , B09B3/0075 , B09B3/0083 , C22B7/001 , C22B11/025 , C22B59/00 , F23G5/006 , F23G5/02 , F23G5/033 , F23G5/448 , F23G5/48 , F23G2201/00 , F23G2201/80 , F23G2205/122 , F23G2205/18 , F23G2209/20 , F23G2900/50001 , Y02P10/214 , Y02P10/238
Abstract: A system for treating infectious waste is provided that employs a medical waste handling and shredding sub-system that feeds partially processed waste to an oxidizer to eliminate potential airborne infectious waste prior to transforming the medical waste into useful co-products. Medical waste is transformed into value added products including hydrocarbon based gases, hydrocarbon-based liquids, carbonized material, and recovered precious metals and rare earth materials in a system having as its transformative element an anerobic, negative pressure, or carbonization system. With medical waste as a feedstock for the production of valuable products, an economically viable and environmentally more responsible alternative to traditional methods of medical waste treatment is realized.
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公开(公告)号：EP3030841B1
公开(公告)日：2017-06-07
申请号：EP14796255.9
申请日：2014-08-08
Applicant: Ronda Engineering S.r.l
Inventor： RONDA, Gianantonio
CPC classification number: F23G5/006 , F23G5/0276 , F23G5/04 , F23G5/46 , F23G2201/303 , F23G2201/40 , F23G2206/10 , F23G2206/203 , Y02E20/12
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Patent Agency Ranking6.发明授权
公开(公告)号：EP2687782B1
公开(公告)日：2017-05-10
申请号：EP12183661.3
申请日：2012-09-10
Applicant: Bak, Tadeusz
Inventor： Bak, Tadeusz , Wysocki, Michal , Wysocki, Zygmunt
CPC classification number: F23G5/006 , F23G5/20 , F23G2201/702 , F23G2900/55011 , Y02E20/12
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7.发明授权Combined plant and process for obtaining electrical energy from municipal solid waste 有权甲联合发电设备和方法，用于从城市废物产生电能
公开(公告)号：EP1479455B1
公开(公告)日：2016-03-16
申请号：EP04011839.0
申请日：2004-05-19
Applicant: A2A Ambiente S.P.A.
Inventor： Natta, Giuseppe , Donati, Gianni
CPC classification number: F22B31/045 , B03B9/06 , B09B3/00 , F23G5/006 , F23G5/027 , F23G5/46 , F23G7/065 , F23G2201/303 , F23G2201/304 , F23G2201/40 , F23G2202/103 , F23G2203/50 , F23G2206/203 , F23J2217/10 , Y02E20/12
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公开(公告)号：EP2833062A4
公开(公告)日：2015-11-25
申请号：EP13767908
申请日：2013-03-26
Inventor： ZHANG ZHIBING , CHEN JINMING , XIONG YONGSHENG
IPC: F23G5/033 , B01D50/00 , C10B53/00 , C10J3/20 , F23G5/00 , F23G5/027 , F23G5/16 , F23G5/44 , F23G5/46 , F23J15/00
CPC classification number: F23G5/027 , B01D2257/40 , B01D2258/0291 , C10B53/00 , F23G5/006 , F23G5/033 , F23G5/16 , F23G5/444 , F23G5/46 , F23G2201/303 , F23G2201/40 , F23G2900/70401 , F23J15/006 , Y02E20/12 , Y02P20/129
Abstract: A process system for treating and recycling MSW, characterized in that, comprising 8 Subsystems: a piling Stack and Storage Subsystem A, Crushing and Roughing Subsystem B, Pyrolysis and Gasification Subsystem C, Time-extended Combustion Subsystem D, Thermal Power Generation Subsystem E, Waste Heat Recovery and Recycling Subsystem F, Flue Gas Comprehensive Treatment Subsystem G, as well as Solid Residue Recovery and Reclamation Subsystem H, respectively, which requires no pretreatment of waste classification, differs from landfill which occupies a large area of land and emits various toxic, hazardous and greenhouse gases to the air during waste degradation, and also varies from the current incineration or the existing pyrolysis and gasification technology, leads to a super low emission of dioxin and other hazardous substances.
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9.发明公开
公开(公告)号：EP2687782A3
公开(公告)日：2015-10-07
申请号：EP12183661.3
申请日：2012-09-10
Applicant: Bak, Tadeusz
Inventor： Bak, Tadeusz , Wysocki, Michal , Wysocki, Zygmunt
CPC classification number: F23G5/006 , F23G5/20 , F23G2201/702 , F23G2900/55011 , Y02E20/12
Abstract: A method for production of electricity and heat in a process of thermal conversion of different types of wastes in an integrated installation, wherein different types of wastes (101-109) are segregated to separate wastes destined for thermal disposal (124, 132, 133, 134, 135), which are then processed in at least two mineralisers (139, 140, 141), each having a form of an isolated, longitudinal, rotatable and inclined tube (200) with vanes (205-210) arranged on its internal walls to scatter the material during the rotation of the tube (200), characterized by performing periodic measurements to determine calorific value, moisture content and composition structure of the wastes intended for thermal disposal (124, 132, 133, 134, 135) by using analysers (114, 118, 122, 127, 129, 131). Using rotary mineralisers (139, 140, 141) that comprise in the mineralisation zone (230) vanes (205-210) with adjustable angle of inclination to the longitudinal axis of the mineraliser tube (200), so that during the operation of mineraliser, for larger inclination angles of vanes (205-210) the batch material passes faster through the mineralisation zone than for smaller inclination angles of vanes (205-210). By using mixers (136, 137, 138) assigned to the mineralisers (139, 140, 141), the wastes (124, 132, 133, 134, 135) are mixed with each other in proportions dependent on the predetermined amount of chemical energy of the batch material and on the inclination angle of vanes (205-210) set in the particular mineraliser (139, 140, 141), so that for a mineraliser (139, 140, 141) having a larger inclination angle of vanes (205-210) a mixture with a higher calorific value is selected than the calorific value of mixture for a mineraliser (139, 140, 141) having a smaller inclination angle of vanes(205-210). The rotational speed of each mineraliser (139, 140, 141) is adjusted according to the moisture content of the mixture provided to the particular mineraliser (139, 140, 141).
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10.发明公开
公开(公告)号：EP2687782A2
公开(公告)日：2014-01-22
申请号：EP12183661.3
申请日：2012-09-10
Applicant: Bak, Tadeusz
Inventor： Wysocki, Zygmunt , Wysocki, Michal
CPC classification number: F23G5/006 , F23G5/20 , F23G2201/702 , F23G2900/55011 , Y02E20/12
Abstract: A method for production of electricity and heat in a process of thermal conversion of different types of wastes in an integrated installation, wherein different types of wastes (101-109) are segregated to separate wastes destined for thermal disposal (124, 132, 133, 134, 135), which are then processed in at least two mineralisers (139, 140, 141), each having a form of an isolated, longitudinal, rotatable and inclined tube (200) with vanes (205-210) arranged on its internal walls to scatter the material during the rotation of the tube (200), characterized by performing periodic measurements to determine calorific value, moisture content and composition structure of the wastes intended for thermal disposal (124, 132, 133, 134, 135) by using analysers (114, 118, 122, 127, 129, 131). Using rotary mineralisers (139, 140, 141) that comprise in the mineralisation zone (230) vanes (205-210) with adjustable angle of inclination to the longitudinal axis of the mineraliser tube (200), so that during the operation of mineraliser, for larger inclination angles of vanes (205-210) the batch material passes faster through the mineralisation zone than for smaller inclination angles of vanes (205-210). By using mixers (136, 137, 138) assigned to the mineralisers (139, 140, 141), the wastes (124, 132, 133, 134, 135) are mixed with each other in proportions dependent on the predetermined amount of chemical energy of the batch material and on the inclination angle of vanes (205-210) set in the particular mineraliser (139, 140, 141), so that for a mineraliser (139, 140, 141) having a larger inclination angle of vanes (205-210) a mixture with a higher calorific value is selected than the calorific value of mixture for a mineraliser (139, 140, 141) having a smaller inclination angle of vanes(205-210). The rotational speed of each mineraliser (139, 140, 141) is adjusted according to the moisture content of the mixture provided to the particular mineraliser (139, 140, 141).
Abstract translation: 一种用于生产在废物集成安装不同类型的废物的热转化的方法电和热的方法，worin不同类型的（101-109）被隔离，以目的地为热处置（124，132，133分离的废物， 134，135），然后将其在至少两个矿化（139，140，141）处理的，每一个都具有分离的，纵向地可旋转的基座和斜管（200的叶片）布置在其内部的形状）（205-210 壁，以通过执行周期性测量以确定矿热值，水分含量和旨在用于热处置废物的组成结构（124，132，133，134，135），其特征在管（200）的通过使用旋转期间散射材料 分析仪（114，118，122，127，129，131）。 用旋转矿化（139，140，141），没包括在矿化区（230）叶片（205-210）与倾斜到管矿化剂（200）的纵向轴线的角度可调，矿化剂的手术过程中也是如此， 对于叶片的更大的倾斜角（205-210）的批料材料通过矿化区快于叶片的更小的倾斜角（205-210）。 通过使用废物混合器（136，137，138）分配给所述矿化（139，140，141）时，（124，132，133，134，135）与在海誓山盟依赖于化学能的预定量的比例混合 批料材料的以及在特定的矿化剂（139，140，141）设置，作为具有叶片的较大的倾斜角矿化（139，140，141）做的叶片的倾斜角度（205-210）（205 -210）具有较高热值的混合物被选择比混合物的具有叶片的较小的倾斜角（205-210）一个矿化（139，140，141）的热值。 每个矿化剂（139，140，141）的旋转速度被雅丁于提供给特定的矿化剂（139，140，141）将所述混合物的水分含量调整。
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