公开(公告)号：US20030192234A1

公开(公告)日：2003-10-16

申请号：US10441116

申请日：2003-05-20

Inventor： Terry J. Logan ,  Ervin L. Faulmann

IPC: C10L005/00

CPC classification number: C05F11/00 ,  C10L5/42 ,  C10L5/44 ,  C10L5/46 ,  C10L5/48 ,  F23G5/02 ,  F23G7/001 ,  F23G2201/10 ,  F23G2201/701 ,  F23G2201/702 ,  F23G2204/101 ,  F23G2209/22 ,  F23G2209/26 ,  F23G2900/7003 ,  Y02E20/12 ,  Y02E50/10 ,  Y02E50/30 ,  Y02P20/129 ,  Y02P20/145

Abstract: Processes and systems are provided that include introducing ammonia liberated from organic waste to a coal burner in a coal burning power plant, preferably for NOx removal at the power plant. The ammonia is preferably either ammonia liberated upon drying a mixture of organic waste and coal combustion byproducts or ammonia liberated when organic waste is mixed with coal combustion by-products and one or more alkaline additives. Also provided are processes and systems of fueling a coal burner of a power plant with coal and either a dried mixture of organic waste and coal combustion by-products, or a mixture of organic waste, coal combustion by-products and one or more alkaline additives. The present invention is further directed to mixtures of either organic waste and coal combustion by-products, or mixtures of organic waste, coal combustion by-products and alkaline additives made by the processes of the present invention.

Abstract translation: 提供的方法和系统包括将从有机废物中释放出的氨引入燃煤发电厂的煤燃烧器，优选在发电厂中除去NO <下标x 。 氨优选是在干燥有机废物和煤燃烧副产物的混合物时释放的氨或当有机废物与煤燃烧副产物和一种或多种碱性添加剂混合时释放的氨。 还提供了用燃煤加燃煤的煤燃烧器和有机废物和煤燃烧副产物的干混合物或有机废物，煤燃烧副产物和一种或多种碱性添加剂的混合物的方法和系统 。 本发明还涉及有机废物和煤燃烧副产物，或有机废物的混合物，煤燃烧副产物和通过本发明的方法制备的碱性添加剂的混合物。

公开(公告)号：US06521365B1

公开(公告)日：2003-02-18

申请号：US09643878

申请日：2000-08-23

Applicant: Seok Mok Song

Inventor： Seok Mok Song

IPC: C01B3120

CPC classification number: F23G7/07 ,  C01B3/323 ,  C01B3/38 ,  C01B32/50 ,  C01B2203/0233 ,  C01B2203/1211 ,  C05C9/00 ,  F23G5/006 ,  F23G5/16 ,  F23G2201/10 ,  F23G2201/701 ,  F23G2202/104 ,  F23J15/003 ,  F23J15/025 ,  F23J2219/10 ,  F23J2219/30 ,  F23J2219/40 ,  F23L7/00 ,  F23L2900/07002 ,  F23L2900/07005 ,  F23L2900/07008 ,  F23L2900/07009 ,  Y02A50/2328 ,  Y02E20/12 ,  Y02E20/326 ,  Y02E20/344 ,  Y02E50/30

Abstract: A waste renewal process in which waste material is burned without causing pollution, while exhaust products are renewed by converting them to useful by-products. The process is implemented in a furnace which has evaporation, thermal decomposition, combustion, and melting zones, and the thermal decomposition exhaust gases are converted to CO2 and synthesis gas, which may be re-utilized to produce a variety of products.

Abstract translation: 在废物更新过程中，废物被燃烧而不产生污染，而废气产品通过将废物转化为有用的副产物而被更新。 该方法在具有蒸发，热分解，燃烧和熔融区的炉中实现，并且热分解废气转化为CO 2和合成气，其可以再利用以生产各种产物。

公开(公告)号：US20020195031A1

公开(公告)日：2002-12-26

申请号：US09887995

申请日：2001-06-20

Inventor： William C. Walker

IPC: F23G005/12 ,  F23B007/00

CPC classification number: F23G5/444 ,  F23G5/027 ,  F23G5/446 ,  F23G5/46 ,  F23G2201/10 ,  F23G2201/303 ,  F23G2201/80 ,  F23G2203/8013

Abstract: An apparatus for treating waste material that comprises four major cooperating subsystems, namely a pyrolytic converter, a two-stage thermal oxidizer, a steam generator and a steam turbine driven by steam generated by the steam generator. In operation, the pyrolytic converter is uniquely heated without any flame impinging on the reactor component and the waste material to be pyrolyzed is transported through the reaction chamber of the pyrolytic converter by a pair of longitudinally extending, side-by-side material transfer mechanisms. Each of the transfer mechanisms includes a first screw conveyor section made up of a plurality of helical flights for conveying the heavier waste and a second paddle conveyor section interconnected with the first section for conveying the partially pyrolyzed waste, the second section comprising a plurality of paddle flights. Once operating, the apparatus is substantially self-sustaining and requires a minimum use of outside energy sources for pyrolyzing the waste materials.

Abstract translation: 一种用于处理废物的装置，包括四个主要协同子系统，即热解转化器，二级热氧化器，蒸汽发生器和由蒸汽发生器产生的蒸汽驱动的蒸汽轮机。 在操作中，热解转化器被独特地加热而没有任何火焰撞击在反应器部件上，待热解的废料通过一对纵向延伸的并排材料转移机构被输送通过热解转化器的反应室。 每个传送机构包括由用于传送较重废物的多个螺旋形叶片组成的第一螺旋输送机部分和与第一部分互连以输送部分热解的废物的第二桨式输送机部分，第二部分包括多个桨叶 航班。 一旦操作，该设备基本上是自我维持的，并且需要最少使用外部能源来热解废料。

公开(公告)号：US06365038B1

公开(公告)日：2002-04-02

申请号：US08511999

申请日：1995-08-07

Applicant: Benjamin Doron

Inventor： Benjamin Doron

IPC: C10B5300

CPC classification number: C01F11/464 ,  C10L1/1233 ,  C10L10/02 ,  C10L10/04 ,  F23C1/00 ,  F23G5/006 ,  F23G5/027 ,  F23G7/05 ,  F23G2201/10 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2205/121 ,  F23G2206/10 ,  F23G2206/202 ,  F23G2209/102 ,  F23G2900/7013 ,  F23K3/00 ,  Y02P20/129

Abstract: Asphaltene and oil shale are pyrolyzed at substantially atmospheric pressure for producing combustible products and carbonaceous material. A combustor combusts the carbonaceous material and produces flue gases which are supplied to a utilization device, and hot ash which is fed back to the pyrolyzer.

Abstract translation: 沥青质和油页岩在大气压下热解生产可燃产物和含碳材料。 燃烧器燃烧碳质材料并产生供应给利用装置的烟气，以及反馈给热解器的热灰。

公开(公告)号：US06182584B2

公开(公告)日：2001-02-06

申请号：US09448022

申请日：1999-11-23

Applicant: Craig T. Gaudio

Inventor： Craig T. Gaudio

IPC: F23G512

CPC classification number: C10B51/00 ,  C10B53/02 ,  F23G5/0276 ,  F23G5/04 ,  F23G7/10 ,  F23G2201/10 ,  F23G2201/30 ,  F23G2201/60 ,  F23G2201/80 ,  F23G2202/30 ,  F23G2207/103 ,  F23J15/022 ,  F23J15/025 ,  F23J2215/20 ,  Y02E50/14

Abstract: A system and process to provide integrated control for the pyrolytic composition of organic (biomass) waste products especially for municipal solid waste systems. The system includes integrated control that monitors biomass waste stream throughout the entire system and the products produced therefrom and includes presorting, controlling the amount of material processed in a continuous manner, shredding, removing moisture in a continuous process that is controlled and providing the waste stream to the distillation unit for pyrolytic action where it is converted into gaseous fuel and a char residue. The gaseous fuel is scrubbed clean and monitored and stored and reused to provide heat to the system. The entire system may be self-sustaining and continuous with very little or no human intervention. An integrated real time computer control system includes sensors and measuring devices with all the major components to ensure integrated efficiency.

Abstract translation: 为有机（生物质）废物的热解组合物特别是城市固体废物系统提供综合控制的系统和方法。 该系统包括综合控制，监测整个系统中的生物质废物流以及由此产生的产品，包括预先分配，控制以连续方式处理的材料的量，粉碎，在被控制的连续过程中除去水分并提供废物流 到用于热解作用的蒸馏单元，其中它被转化为气体燃料和焦炭残余物。 清洁气体燃料并进行监测和储存并重复使用以向系统提供热量。 整个系统可能是自我维持和持续的，很少或没有人为干预。 集成的实时计算机控制系统包括具有所有主要组件的传感器和测量设备，以确保集成效率。

公开(公告)号：US06167636A

公开(公告)日：2001-01-02

申请号：US09315199

申请日：1999-05-19

Applicant: Leopold Werner Kepplinger ,  Dieter Pelz ,  Gerald Zanker

Inventor： Leopold Werner Kepplinger ,  Dieter Pelz ,  Gerald Zanker

IPC: F26B334

CPC classification number: F23G5/027 ,  F23G5/04 ,  F23G5/46 ,  F23G7/10 ,  F23G2201/10 ,  F23G2201/20 ,  F23G2201/40

Abstract: In a process for thermally utilizing wet spent grains (1), the wet spent grains (1) are mechanically predried in a first drying stage (2), thermally dried in a further drying stage (4) and finally thermally utilized by burning or gasification. In order to be able to realize a process of this kind economically, the mechanically dehydrated spent grains (15) in the further drying stage (4) are heated by the aid of a smoke gas occurring within the energy system of a brewery.

Abstract translation: 在热利用湿废晶粒（1）的方法中，将湿废晶粒（1）在第一干燥阶段（2）中机械预干燥，在进一步的干燥阶段（4）中热干燥，最后通过燃烧或气化热利用 为了能够经济地实现这种方法，在进一步的干燥阶段（4）中的机械脱水的废料（15）借助于在啤酒厂的能量系统内发生的烟雾气体被加热。

公开(公告)号：US5595483A

公开(公告)日：1997-01-21

申请号：US406625

申请日：1995-03-20

Applicant: Albrecht Melber ,  Erwin Wanetzky ,  Dieter Uschkoreit

Inventor： Albrecht Melber ,  Erwin Wanetzky ,  Dieter Uschkoreit

IPC: B01J3/00 ,  B01J19/18 ,  C10B7/00 ,  C10B53/00 ,  F23G5/00 ,  F23G5/027 ,  F23G5/033 ,  F23G5/16 ,  F27D7/06 ,  F27B5/04

CPC classification number: C10B53/00 ,  B01J19/1862 ,  B01J3/006 ,  C10B7/00 ,  F23G5/006 ,  F23G5/0276 ,  F23G5/16 ,  B01J2219/00103 ,  B01J2219/00108 ,  B01J2219/00132 ,  B01J2219/00157 ,  B01J2219/00162 ,  F23G2201/10 ,  F23G2201/80 ,  F23G2206/10 ,  F23G2900/50214 ,  F23L2900/07005 ,  Y02E20/344

Abstract: Materials containing vaporizable substances are exposed successively in at least two treatment chambers (10, 13, 14), which can be closed off with respect to each other, to a series of decreasing pressures and increasing temperatures. The vaporizable substances are exhausted separately from each treatment chamber (10, 13, 14) and at least partially condensed and collected. The solid materials are discharged from the last treatment chamber (14). The treatment chambers (10, 13, 14) can be closed off against each other, against the atmosphere, and against any other units which may be connected to them downline (17, 18) by vacuum valves (11, 12, 115, 16) and are connected to vacuum lines (10a, 13a, 14a) in which condensers (10b, 13b, 14b) and vacuum pumps (10c, 13c, 14c) are installed.

Abstract translation: 含有可汽化物质的材料在至少两个相对于彼此封闭的处理室（10,13,14）中相继暴露于一系列降低的压力和升高的温度。 可蒸发物质与每个处理室（10,13,14）分开排出并且至少部分地冷凝和收集。 固体材料从最后一个处理室（14）排出。 处理室（10,13,14）可以相对于大气封闭，并且可以与可通过真空阀（11,12,151,16）连接到它们下线（17,18）的任何其它单元 ）连接到其中安装有冷凝器（10b，13b，14b）和真空泵（10c，13c，14c）的真空管线（10a，13a，14a）。

公开(公告)号：US5501160A

公开(公告)日：1996-03-26

申请号：US274575

申请日：1994-07-13

Applicant: Daniel Goldman ,  Boris Siniakevith ,  Benjamin Doron ,  Lucien Y. Bronicki ,  Eli Yaffe

Inventor： Daniel Goldman ,  Boris Siniakevith ,  Benjamin Doron ,  Lucien Y. Bronicki ,  Eli Yaffe

IPC: C10B49/16 ,  C10B49/18 ,  C10B53/06 ,  C10J3/46 ,  C10J3/58 ,  C10L9/08 ,  C10L9/10 ,  F23G5/00 ,  F23G5/12

CPC classification number: F23G5/006 ,  F23G2201/10 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2206/10 ,  F23G2209/102 ,  Y02E20/12

Abstract: A portion of solid fuel is pyrolyzed in a pyrolyzer to produce combustible gases and carbonaceous material, the carbonaceous material being supplied from the pyrolyzer to a furnace. A further portion of the solid fuel is added to a furnace and is combusted with the carbonaceous material therein to produce combustion products that include hot flue gases and ash particulate. The combustion products are separated into a plurality of streams, one of which contains coarse ash and another of which contains flue gases and fine ash. A portion of the coarse ash is directed into the pyrolyzer while a further portion is disposed of, preferably by being used to heat air entering the furnace.

Abstract translation: 固体燃料的一部分在热解器中热解以产生可燃气体和含碳材料，碳质材料从热解器供应到炉中。 将另一部分固体燃料加入到炉中并与其中的碳质材料一起燃烧以产生包括热烟道气和灰分颗粒的燃烧产物。 燃烧产物被分离成多个流，其中一个流含有粗灰，另一个含有烟道气和细灰。 粗灰分的一部分被引导进入热解器，而另一部分被排出，优选地用于加热进入炉的空气。

公开(公告)号：US4615867A

公开(公告)日：1986-10-07

申请号：US604601

申请日：1984-04-27

Applicant: Emile A. Heckmann

Inventor： Emile A. Heckmann

IPC: A23K1/10 ,  A23L3/16 ,  A23L3/18 ,  A23L3/40 ,  B09B3/00 ,  C02F11/12 ,  F26B11/14 ,  F26B23/02 ,  F26B3/06

CPC classification number: C02F11/12 ,  A23K10/26 ,  A23L3/16 ,  A23L3/18 ,  A23L3/40 ,  B09B3/00 ,  F26B11/14 ,  F26B23/022 ,  F23G2201/10 ,  F23G2209/14

Abstract: Apparatus for cooking-dehydration and sterilization-drying of organic wastes, comprises a chamber (1) heated by a double walled enclosure (2) that communicates with fire tubes (3), the enclosure (2) receiving hot gases from a firebox (4). The hot gases pass through conduits (5) to diffusion nozzles (6) immersed in the products (7) to be dried. Some of the combustion gases are recycled by a ventilator (8) via a conduit (9) and a cyclone (10) to the firebox (4). The ventilator (8) draws in fresh air through a preheating heat exchanger (11) that is heated by the combustion gases which are then vented.

Abstract translation: 用于烹饪 - 有机废物的脱水和灭菌 - 干燥的设备包括通过与火管（3）连通的双壁围墙（2）加热的室（1），所述外壳（2）从火炉（4）接收热气体 ）。 热气体通过导管（5）到浸没在待干燥的产品（7）中的扩散喷嘴（6）。 一些燃烧气体通过通气机（8）通过导管（9）和旋风分离器（10）再循环到火箱（4）。 通风机（8）通过预热热交换器（11）吸入新鲜空气，预热热交换器（11）被燃烧气体加热，然后排出。

公开(公告)号：US4244779A

公开(公告)日：1981-01-13

申请号：US970457

申请日：1978-12-18

Applicant: Jorma J. Nieminen ,  Folke Engstrom

Inventor： Jorma J. Nieminen ,  Folke Engstrom

IPC: B01J8/32 ,  C02F11/12 ,  C10B49/16 ,  D21C11/00 ,  D21C11/12

CPC classification number: D21C11/0092 ,  B01J8/32 ,  C02F11/12 ,  C10B49/16 ,  F23G2201/10 ,  F23G2203/501

Abstract: A method of treating materials in a fluidized bed reactor, wherein the material to be treated is brought into contact with hot particles removed from the flue gases coming from the fluidized bed reactor to bring about chemical and/or thermal reactions in the material before it is introduced into the fluidized bed reactor together with recycled particles. Useful components may be recovered in the form of gases, solids or liquids in connection with this treatment.

Abstract translation: 一种在流化床反应器中处理材料的方法，其中待处理的材料与从流化床反应器的烟道气中除去的热颗粒接触，在材料之前引起化学和/或热反应 与再循环的颗粒一起引入流化床反应器。 有用的组分可以以与该处理相关的气体，固体或液体的形式回收。