公开(公告)号：US09719679B2

公开(公告)日：2017-08-01

申请号：US14766290

申请日：2014-02-13

Applicant: Areva NC

Inventor： Roger Boen ,  Patrice Charvin

IPC: B09C1/06 ,  F23G5/027 ,  G21F1/06 ,  G21F5/005 ,  G21F9/14 ,  G21F9/32 ,  F23G5/44 ,  B09B3/00 ,  B65D1/38 ,  B65D13/02

CPC classification number: F23G5/027 ,  B09B3/0025 ,  B09B3/0083 ,  B65D1/38 ,  B65D13/02 ,  F23G5/448 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2203/40 ,  G21F1/06 ,  G21F5/005 ,  G21F9/14 ,  G21F9/32

Abstract: A basket for incinerating waste inside an incinerator for a duration longer than fifteen minutes with no need for waste to be molten earlier, particularly when waste is introduced inside the incinerator. The basket includes mainly of a glass fiber envelope: it is preferably stiffened by a lightweight metal structure located inside or outside the envelope or built into it. A gripping handle is installed on top of the assembly that is stiffened at the top by a metal tube to which a lightweight metal structure is fixed and by a base formed from a drip pan fixed to the base of the lightweight metal structure.

公开(公告)号：US09714766B2

公开(公告)日：2017-07-25

申请号：US13155482

申请日：2011-06-08

Applicant: Wiley Benjamin Bunting, Jr. ,  David C. Mayer ,  Seba Leonard Allen

Inventor： Wiley Benjamin Bunting, Jr. ,  David C. Mayer ,  Seba Leonard Allen

IPC: F23G5/12 ,  F23L13/06 ,  F23M5/00 ,  F23N3/00 ,  F23N3/04 ,  F23G5/027 ,  F23G5/14 ,  F23G5/48

CPC classification number: F23L13/06 ,  F23G5/0273 ,  F23G5/14 ,  F23G5/48 ,  F23G2201/303 ,  F23G2201/304 ,  F23M5/00 ,  F23M2900/05004 ,  F23N3/007 ,  F23N3/045

Abstract: A gasifier for disposing of biomass and other waste materials through a gasification and combustion process. The gasifier includes a primary chamber for receiving and holding biomass or a selected waste product. A heat transfer chamber is disposed adjacent the primary chamber. A burner is associated with the gasifier for generating heat and heating the gasifier during various phases or portions of the gasification and combustion process. In the gasification process, the heat transfer chamber is heated and the heat is transferred to the primary chamber where the biomass is heated. During the gasification process, biomass material is volatized generating fumes and gases that later react and release heat through exothermic reactions. Once the gasification process has been concluded, the process enters a combustion phase where the biomass is actually burned. During the gasification-combustion phases, the amount of heat supplied by the burner will vary. Generally the amount of energy or heat supplied by the burner will decrease throughout the process because the biomass itself will supply substantial amounts of heat through exothermic reactions.

公开(公告)号：US09657941B2

公开(公告)日：2017-05-23

申请号：US13264986

申请日：2010-04-19

Applicant: Panayotis Tsantrizos ,  Stephan Lavigne

Inventor： Panayotis Tsantrizos ,  Stephan Lavigne

IPC: F27D19/00 ,  F23G5/027 ,  F23G5/50 ,  F23J15/06 ,  F23L7/00 ,  F23N5/00 ,  C10J3/02 ,  B01D53/62 ,  C10J3/72 ,  B01D53/78

CPC classification number: F23G5/027 ,  B01D53/62 ,  B01D53/78 ,  B01D2251/304 ,  B01D2257/504 ,  B01D2258/0291 ,  C10J3/02 ,  C10J3/726 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1215 ,  C10J2300/1246 ,  F23G5/0273 ,  F23G5/50 ,  F23G2201/303 ,  F23G2207/101 ,  F23G2207/103 ,  F23G2207/30 ,  F23G2207/50 ,  F23J15/06 ,  F23L7/002 ,  F23N5/006 ,  Y02C10/04 ,  Y02E20/326 ,  Y02E20/363 ,  Y02E50/32 ,  Y02P20/152

Abstract: The gasifier operates to mix a start up heat source with crude syngas combustion for driving gasification of waste. Combustion flue gas can be maintained above 650° C. until reaching a quench to prevent formation of dioxins. Excess heat is liberated through a heat recovery unit. The gasifier can operate in a batch mode to process small batches of waste efficiently for small installations, such as ships, apartment buildings, hospitals and residences.

公开(公告)号：US20160333271A1

公开(公告)日：2016-11-17

申请号：US15221713

申请日：2016-07-28

Applicant: PYROWAVE INC.

Inventor： Jocelyn DOUCET ,  Jamal CHAOUKI ,  Amr SOBHY

IPC: C10B53/07 ,  C10B47/18 ,  C10G1/10 ,  C10G1/02 ,  C10G1/00 ,  C10B19/00 ,  C10B27/06

CPC classification number: C10B53/07 ,  B01J21/18 ,  C10B19/00 ,  C10B27/06 ,  C10B47/18 ,  C10B53/00 ,  C10B53/02 ,  C10G1/002 ,  C10G1/02 ,  C10G1/10 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10K1/024 ,  C10K3/02 ,  C10L9/083 ,  F23G5/0276 ,  F23G2201/303 ,  F23G2204/203 ,  F23G2900/50202 ,  Y02E50/14 ,  Y02E50/15

Abstract: The present document describes a catalyst to initiate microwave pyrolysis of waste, a process for the microwave pyrolysis of waste using the catalyst, as well as a microwave pyrolysis system.

Abstract translation: 本文件描述了引发废物的微波热解的催化剂，使用催化剂的废物微波热解的方法以及微波热解系统。

公开(公告)号：US20160018107A1

公开(公告)日：2016-01-21

申请号：US14802509

申请日：2015-07-17

Applicant: MAGNEGAS CORPORATION

Inventor： Ermanno Santilli

IPC: F23G5/027 ,  F23G7/10

CPC classification number: F23G5/0276 ,  F23G5/12 ,  F23G5/16 ,  F23G7/065 ,  F23G7/10 ,  F23G2201/303 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2204/103 ,  F23G2209/26 ,  Y02E20/12

Abstract: A system for generating energy from biomass uses an arc-produced gas, either in the primary burn process to achieve higher burning temperatures, in a secondary after-burn process to reduce pollutants, or in both the primary burn process and after-burn process. The use of arc-produced gas results in increased efficiency, reduced emissions, and additional heat energy. Heat produced is used, for example, to generate electricity. In some embodiments, the arc-produced gas is combined with another fuel such as oil or natural gas for desired burn characteristics and/or for economic reasons.

Abstract translation: 生物质发电的系统使用电弧产生的气体，无论是在初级燃烧过程中，以实现更高的燃烧温度，二次后燃烧过程中，以减少污染物，或者在初级燃烧过程和后燃烧过程中。 使用电弧产生的气体可以提高效率，减少排放和额外的热能。 所产生的热量例如用于发电。 在一些实施例中，电弧产生的气体与另一种燃料（例如石油或天然气）组合以达到期望的燃烧特性和/或出于经济原因。

公开(公告)号：US09170019B2

公开(公告)日：2015-10-27

申请号：US13060096

申请日：2009-08-28

Applicant: Jens Dall Bentzen

Inventor： Jens Dall Bentzen

IPC: C10B1/00 ,  C10B31/02 ,  F23G5/24 ,  C10J3/34 ,  C10J3/72 ,  C10J3/80 ,  C10K1/10 ,  F23G5/027 ,  F23G5/50 ,  F23L7/00

CPC classification number: F23G5/24 ,  C10J3/34 ,  C10J3/723 ,  C10J3/80 ,  C10J2200/09 ,  C10J2200/154 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/101 ,  F23G5/027 ,  F23G5/50 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23L7/007 ,  F23L2900/00001 ,  Y02E20/12 ,  Y02E20/344

Abstract: Solid fuel can be converted into a clean hot flue gas with a low content of volatile organic compounds (VOC's), NOx and dust, and clean ash with a low carbon content by means of a stage-divided thermal reactor, where the conversion process of the solid fuel is in separate vertical stages (from below and up): ash burn-out, char oxidation and gasification, pyrolysis, drying, and a gas combustion stage where gas from the gasifier is combusted.

Abstract translation: 固体燃料可以通过分段热分解反应器转化为具有低含量挥发性有机化合物（VOC），NOx和粉尘以及低碳含量的清洁灰分的干净的热烟气，其中转化过程 固体燃料处于分开的垂直阶段（从下到上）：灰分燃烧，焦炭氧化和气化，热解，干燥以及来自气化器的气体燃烧的气体燃烧阶段。

公开(公告)号：US20150240170A1

公开(公告)日：2015-08-27

申请号：US14439937

申请日：2013-10-09

Applicant: TEKNOLOGIAN TUTKIMUSKESKUS VTT OY

Inventor： Esa Kurkela ,  Matti Nieminen

IPC: C10J3/52 ,  G21F9/00 ,  C10J3/72 ,  C10L3/00 ,  C10J3/48 ,  C10J3/46 ,  G21F9/30 ,  G21F9/02

CPC classification number: C10J3/523 ,  C10J3/463 ,  C10J3/482 ,  C10J3/72 ,  C10J3/723 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1246 ,  C10J2300/1606 ,  C10J2300/1615 ,  C10J2300/1618 ,  C10J2300/1628 ,  C10J2300/1846 ,  C10K1/024 ,  C10K1/101 ,  C10L3/00 ,  C10L2200/0461 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/545 ,  C10L2290/58 ,  F23G5/027 ,  F23G7/001 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2209/18 ,  F23J15/025 ,  F23J15/06 ,  F23J2217/104 ,  G21F9/001 ,  G21F9/02 ,  G21F9/30 ,  G21F9/32 ,  G21F9/34 ,  Y02E20/363

Abstract: A method and apparatus for treating waste material having organic components and radioactive agents. The method including the steps of gasifying the waste material at temperature between 600-950° C. in a reactor to form a gaseous material. The gaseous material is cooled to a temperature between 300-500° C., after the cooling the solid fraction including the radioactive agents are removed.

Abstract translation: 一种用于处理具有有机成分和放射性试剂的废料的方法和装置。 该方法包括在反应器中在600-950℃的温度下气化废料以形成气态物质的步骤。 将气态物质冷却至300-500℃之间的温度，冷却后除去包括放射性试剂的固体部分。

公开(公告)号：US20150166911A1

公开(公告)日：2015-06-18

申请号：US14105832

申请日：2013-12-13

Applicant: Frank Reed

Inventor： Frank Reed

IPC: C10J3/82

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。

公开(公告)号：US20150107496A1

公开(公告)日：2015-04-23

申请号：US14513496

申请日：2014-10-14

Applicant: KRISHNA KUMAR BINDINGNAVALE RANGA

Inventor： KRISHNA KUMAR BINDINGNAVALE RANGA

IPC: F23K1/00 ,  F23J11/00

CPC classification number: F23G5/0276 ,  F23G5/04 ,  F23G5/46 ,  F23G7/10 ,  F23G2201/303 ,  F23G2202/101 ,  F23G2202/103 ,  F23G2206/10 ,  F23G2206/203 ,  F23G2207/30 ,  F23G2209/261 ,  F23G2209/262 ,  F23G2900/50002 ,  F23G2900/7012 ,  F23M9/08 ,  Y02E20/12

Abstract: The various embodiments herein provide an improved biomass based down draft gasifier for producing electrical energy. The gasifier comprises a reactor with double walled construction having an annular space between outer and inner shells. The annular space houses multiple helical guide vanes welded to the inner shell. The reactor is covered with a top cover assembly. An air inlet manifold is provided for directing the controlled air into the reactor through the air inlet nozzles. An automatic start system is provided for controlling the combustion of inlet fuel done with a spark plug. The gasifier comprises a throat which permits the ashes and charcoal of burnt fuel to drop into the bottom of the reactor. The gas separation holes are provided at the bottom of the reactor to separate the product gas from the charcoal. The product gas is taken out from an output pipe.

Abstract translation: 本文的各种实施方案提供了用于产生电能的改进的基于生物质的下流气化器。 气化器包括具有双壁结构的反应器，其在外壳和内壳之间具有环形空间。 环形空间容纳多个螺旋导叶，焊接在内壳上。 反应器被顶盖组件覆盖。 空气入口歧管被设置用于通过空气入口喷嘴将受控空气引导到反应器中。 提供一种自动启动系统，用于控制用火花塞完成的入口燃料的燃烧。 气化器包括一个允许燃烧燃料的灰分和木炭落入反应器底部的喉部。 气体分离孔设置在反应器的底部，以将产物气体与木炭分离。 产品气体从输出管中取出。

公开(公告)号：US20140259926A1

公开(公告)日：2014-09-18

申请号：US14293961

申请日：2014-06-02

Applicant: POWER WASTE GASIFICATION, LLC

Inventor： Sergey Y. Strizhak

IPC: C10J3/86

CPC classification number: C10J3/86 ,  B01J8/087 ,  B01J8/12 ,  B01J2208/00212 ,  B01J2208/0053 ,  C10J3/26 ,  C10J3/34 ,  C10J3/42 ,  C10J2200/09 ,  C10J2200/154 ,  C10J2300/0903 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1671 ,  C10J2300/1693 ,  C10J2300/1884 ,  C10K1/026 ,  C10K1/32 ,  F23G5/0276 ,  F23G2201/303 ,  F23G2900/50804 ,  F23L7/005

Abstract: The invention relates to chemical technology and equipment, in particular to apparatuses of processing of solid household and industrial waste, as well as other carbon-containing feedstock into combustible gasification gas and methods for pyrolysis and downdraft gasification process.

Abstract translation: 本发明涉及化学技术和设备，特别涉及固体家庭和工业废物的处理设备，以及其它含碳原料转化为可燃气化气体的方法以及用于热解和向下气化过程的方法。