公开(公告)号：US20040134395A1

公开(公告)日：2004-07-15

申请号：US10744636

申请日：2003-12-23

Inventor： Claus Eberhardt ,  Bernd Ruediger Kipper ,  Ulrich Stegmann ,  Jochen Zingelmann

IPC: F23B007/00

CPC classification number: C10J3/721 ,  B03B9/06 ,  C10J3/16 ,  C10J3/24 ,  C10J3/723 ,  C10J2200/09 ,  C10J2200/156 ,  C10J2300/0903 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/1606 ,  C10J2300/1646 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/169 ,  F23G5/006 ,  F23G5/02 ,  F23G5/027 ,  F23G5/033 ,  F23G5/05 ,  F23G5/12 ,  F23G5/24 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/10 ,  F23G2201/40 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/702 ,  F23G2206/203 ,  F23G2207/101 ,  F23G2207/102 ,  F23G2900/50209 ,  F23J15/025 ,  F23L7/00 ,  F23L2900/07005 ,  F23L2900/07009 ,  Y02E20/12 ,  Y02E20/344 ,  Y02E50/10 ,  Y02E50/30 ,  Y02P20/129 ,  Y02W30/523

Abstract: A method and an apparatus for treating and utilizing waste materials and mixtures thereof in multiple steps resulting in a high-yield utilization particularly of organic components of the waste for generating kinetically useful energy. The waste materials are sorted by classes, principally between organic and non-organic, e.g. metallic and ceramic, substances. The organic substances are briquetted and gasified, the produced gas being utilized for the direct and indirect generation of electricity and heat.

Abstract translation: 一种用于以多个步骤处理和利用废物及其混合物的方法和装置，其导致高产率利用，特别是用于产生动力学有用能量的废物的有机组分。 废物按类别分类，主要在有机和非有机之间，例如， 金属和陶瓷，物质。 有机物料被压块和气化，产生的气体用于直接和间接地产生电力和热量。

公开(公告)号：US5771822A

公开(公告)日：1998-06-30

申请号：US561649

申请日：1995-11-22

Applicant: John Rizzon

Inventor： John Rizzon

IPC: B09B3/00 ,  C03B3/00 ,  C03B5/00 ,  C03B5/12 ,  F23G5/00 ,  F23G5/08 ,  F23J1/00 ,  F23J15/00

CPC classification number: F23J15/003 ,  B09B3/0066 ,  C03B3/00 ,  C03B5/005 ,  C03B5/12 ,  F23G5/006 ,  F23G5/085 ,  F23G2201/301 ,  F23G2201/302 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/602 ,  F23G2201/70 ,  F23G2201/80 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/20 ,  F23G2203/212 ,  F23G2205/14 ,  F23G2205/18 ,  F23G2209/12 ,  F23G2209/28 ,  F23G2900/50002 ,  F23J2219/10 ,  F23J2219/80 ,  F23L2900/07005 ,  Y02E20/344 ,  Y02P40/55

Abstract: The present invention describes a process for the disposal of residual substances from waste incineration plants as well as activated coke and/or activated carbon. For this purpose the residual substance as well as activated coke and/or activated carbon is introduced into the annular shaft (3) of the primary chamber (2) of the furnace (1). In the primary chamber (2) a temperature of 1250.degree. C. to 1500.degree. C. is set. The molten material flowing off leaves the primary chamber (2) together with the flue gases through the central outlet (4). The molten material is passed through the secondary chamber (5) and is discharged as slag. The present invention furthermore describes an apparatus for such process, where in the furnace roof (10) of the primary chamber (2) of the furnace (1) one or several burners (7) are disposed and at one or several points (22) of the furnace roof (10) secondary air is introduced into the primary chamber (2) and at one or several points (23) of the furnace roof (10) tertiary air is introduced into the primary chamber (2).

Abstract translation: 本发明描述了用于处理来自废物焚化厂以及活性焦炭和/或活性炭的残余物质的方法。 为此，残留物质以及活性焦炭和/或活性炭被引入到炉（1）的主室（2）的环形轴（3）中。 在初级室（2）中，设定1250℃至1500℃的温度。 流出的熔融材料通过中心出口（4）与烟道气一起离开主室（2）。 熔融材料通过次级室（5）并作为渣排出。 本发明还描述了一种用于这种方法的装置，其中在炉（1）的主室（2）的炉顶（10）中设置一个或多个燃烧器（7）并且在一个或多个点（22）处， 炉顶（10）的二次空气被引入主室（2）中并且在炉顶（10）的一个或多个点（23）处，三次空气被引入主室（2）。

公开(公告)号：US5133297A

公开(公告)日：1992-07-28

申请号：US689336

申请日：1991-04-22

Applicant: Momtaz N. Mansour

Inventor： Momtaz N. Mansour

IPC: F23C10/04 ,  B01J8/40 ,  F22B1/02 ,  F22B31/00 ,  F23C10/00 ,  F23C10/18 ,  F23C15/00 ,  F23G5/30 ,  F26B3/092 ,  F26B23/02 ,  F27B15/00 ,  F27B15/14

CPC classification number: F23C15/00 ,  B01J8/40 ,  F22B31/0023 ,  F23C10/002 ,  F23G5/30 ,  F26B23/026 ,  F26B3/0926 ,  F23G2201/602 ,  F23G2202/40 ,  F23G2209/20 ,  F23G2900/50001

Abstract: A pulsed atmospheric fluidized bed reactor system is disclosed and claimed along with a process for utilization of same for the combustion of, e.g. high sulfur content coal. The system affords a economical, ecologically acceptable alternative to oil and gas fired combustors. The apparatus may also be employed for endothermic reaction, combustion of waste products, e.g. organic and medical waste, drying, calcining and the like.

Abstract translation: 公开和要求的脉冲大气流化床反应器系统以及用于燃烧例如燃料的方法。 高硫含量煤。 该系统为油气燃烧器提供了经济，生态可接受的替代方案。 该装置还可以用于吸热反应，废物的燃烧，例如， 有机废物和医疗废物，干燥，煅烧等。

公开(公告)号：US4015546A

公开(公告)日：1977-04-05

申请号：US620962

申请日：1975-10-09

Applicant: Eugene H. Paules

Inventor： Eugene H. Paules

IPC: F23G5/00 ,  F23G5/02 ,  F23G5/16 ,  F23G5/32 ,  F23G5/50 ,  F23N3/04 ,  F23G5/04

CPC classification number: F23G5/50 ,  F23G5/006 ,  F23G5/02 ,  F23G5/16 ,  F23G5/32 ,  F23N3/042 ,  F23G2201/10 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2206/203 ,  F23G2207/101 ,  F23G2207/30 ,  F23N2035/06 ,  F23N2035/10 ,  F23N2037/16 ,  Y02E20/12

Abstract: The preferred embodiment of the invention disclosed herein includes apparatus for and the steps of separating glass, metal and other generally non-combustible material from refuse to provide a volume of generally combustible refuse, shreddingthe volume of combustible refuse into relatively small particles and mixing the particles with primary combustion air, which is used to convey the particles to a combustion chamber. Auxiliary burners are used to heat the combustion chamber to a predetermined temperature above which the particles are self-igniting and use of the burners is thereafter discontinued unless the temperature falls below the predetermined temperature. The particles are separated as they are injected into the combustion chamber with a cyclonic motion. In the combustion chamber the mixture is ignited and converted to combustion gases which flow through the chamber. The flow of secondary air is regulated to provide maximum combustion temperature for the particles and negative pressure is maintained in the chamber to control the flow rate of the gases and to assure that the gases are generally completely combusted. The combusted gases are exhausted to an associated device such as a steam boiler or other device using the heat energy and thereafter are exhausted to the atmosphere.

Abstract translation: 本文公开的本发明的优选实施例包括用于分离玻璃，金属和其它通常不可燃材料与垃圾的装置，以提供一定体积的可燃垃圾，将可燃垃圾的体积粉碎成相对较小的颗粒并混合颗粒 主燃烧空气用于将颗粒输送到燃烧室。 辅助燃烧器用于将燃烧室加热到预定的温度以上，颗粒自燃以上，此后不再使用燃烧器，除非温度低于预定温度。 当颗粒被喷射到具有气旋运动的燃烧室中时，颗粒被分离。 在燃烧室中，混合物被点燃并转化成流过室的燃烧气体。 调节二次空气的流动以为颗粒提供最大的燃烧温度，并且在室中保持负压以控制气体的流速并确保气体通常完全燃烧。 燃烧的气体被排放到相关设备，例如蒸汽锅炉或使用热能的其它设备，然后被排放到大气中。

公开(公告)号：US09580246B2

公开(公告)日：2017-02-28

申请号：US13638784

申请日：2011-04-01

Applicant: Perttu Laakkonen ,  Juha Palokangas

Inventor： Perttu Laakkonen ,  Juha Palokangas

IPC: B07C5/04 ,  B65G1/137 ,  F23G5/02 ,  F23G5/50 ,  F23G7/10 ,  B07C5/14

CPC classification number: B65G1/137 ,  B07C5/04 ,  B07C5/14 ,  F23G5/02 ,  F23G5/50 ,  F23G7/10 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2207/20 ,  F23G2900/50214 ,  F23G2900/55006 ,  F23G2900/55007 ,  F23G2900/55011 ,  F23N2021/10

Abstract: A method for processing material that contains biomass. The material is led onto a conveyor. The conveyor conveys the material to an apparatus for mechanical processing and/or to a further processing plant. The moisture content is measured and/or the size of pieces of non-combustible material and/or the content of non-combustible material in the material flow is measured in connection with the conveyor. Based on at least one of the measurements, material is conveyed to the material to be conveyed for further processing and/or to the apparatus for mechanical processing, or to at least one material to be conveyed elsewhere than to the further processing plant or the apparatus for mechanical processing. Also a system for processing material that contains biomass.

Abstract translation: 一种处理含有生物质的材料的方法。 材料被引导到输送机上。 输送机将材料输送到用于机械加工的设备和/或进一步处理设备。 测量水分含量和/或材料流中的不可燃材料块和/或不燃材料的含量与输送机相关的尺寸。 基于至少一个测量，将材料输送到待运送的材料用于进一步的处理和/或用于机械加工的设备，或至少一种待传送到另外的处理设备或设备的材料 用于机械加工。 还有一种用于处理含有生物质的材料的系统。

公开(公告)号：US20140182491A1

公开(公告)日：2014-07-03

申请号：US13731648

申请日：2012-12-31

Applicant: Air Liquide, Societe Anonyme pour Etude et Exploitation des Procedes Georges Claude

Inventor： Yuan XUE ,  Remi Pierre TSIAVA ,  Sebastian DE LIMON

IPC: F23L7/00 ,  F23G5/02 ,  F23G5/14 ,  F23G7/10

CPC classification number: F23L7/007 ,  F23D1/00 ,  F23G5/02 ,  F23G5/14 ,  F23G7/10 ,  F23G2201/602 ,  F23G2205/14 ,  F23G2209/26 ,  F23L2900/07005 ,  Y02E20/344

Abstract: Improved combustion of biomass is achieved by injected first and second streams of biomass from a burner where the first stream of biomass has a median particle size larger than the biomass of the second stream and oxygen is injected with the first stream to provide an oxygen-enriched environment around the larger median sized particles. The oxygen-enriched environment is achieved either by injecting the oxygen directly into the first stream or by premixing the oxygen with the conveying air of the first stream.

Abstract translation: 通过从燃烧器注入第一和第二生物量流来实现生物质的改善燃烧，其中第一生物质流的中值粒径大于第二流的生物量，氧注入第一流以提供富氧 周围环境较大的中等大小的颗粒。 通过将氧直接注入第一流或通过将氧与第一流的输送空气预混合来实现富氧环境。

公开(公告)号：US20130055934A1

公开(公告)日：2013-03-07

申请号：US13697610

申请日：2011-05-12

Applicant: Kazuhiro Takeuchi ,  Takuichiro Daimaru ,  Masaaki Kinoshita ,  Yoshiki Yamaguchi ,  Norichika Kai

Inventor： Kazuhiro Takeuchi ,  Takuichiro Daimaru ,  Masaaki Kinoshita ,  Yoshiki Yamaguchi ,  Norichika Kai

IPC: B02C23/26 ,  F23G5/033 ,  B02C15/00

CPC classification number: F23G5/033 ,  B02C15/007 ,  B02C23/24 ,  B02C2015/002 ,  C10L5/04 ,  C10L5/366 ,  C10L5/44 ,  F23C2900/01001 ,  F23G7/10 ,  F23G2201/60 ,  F23G2201/602 ,  F23K1/00 ,  F23K1/04 ,  F23K2201/10 ,  F23K2201/103 ,  F23K2201/30 ,  F23K2201/501 ,  Y02E50/10 ,  Y02E50/30

Abstract: A biomass pulverizing apparatus includes a pulverizing apparatus body including a feedstock supply pipe, the pulverizing apparatus body for supplying biomass feedstock from above in a vertical axial direction, a pulverizing table for placing the biomass feedstock, a drive section for rotationally driving the pulverizing table, a pulverizing roller for pulverizing the biomass feedstock by a pressing force, the pulverizing roller being operated in conjunction with the rotation of the pulverizing table, a blower unit for forming an upward flow upward from below on the outer peripheral side of the pulverizing table so as to jet conveying gas for conveying the pulverized biomass powder in an air stream, a classifier, the classifier for classifying the biomass powder accompanied with the conveying gas, and a blowing gas introduction section.

Abstract translation: 一种生物质粉碎装置，包括：粉碎装置主体，包括原料供给管，用于从上方沿垂直轴向供给生物质原料的粉碎装置主体;用于放置生物质原料的粉碎台;旋转驱动粉碎台的驱动部; 用于通过按压力粉碎生物质原料的粉碎辊，粉碎辊与粉碎台的旋转一起操作;鼓风机单元，用于在粉碎台的外周侧从下方向上流动，以便 用于将用于输送空气流中的粉碎生物质粉末的输送气体，分选机，用于分选伴随输送气体的生物质粉末的分选机和吹送气体导入部。

公开(公告)号：US20130000532A1

公开(公告)日：2013-01-03

申请号：US13173237

申请日：2011-06-30

Applicant: Yuriy RABINER

Inventor： Yuriy RABINER

IPC: F23G5/02

CPC classification number: F23G5/02 ,  F23G5/006 ,  F23G7/006 ,  F23G2201/10 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80

Abstract: A municipal or like refuse is crushing, separating ferrous metals, mixing with crushed limestone, drying up and loading in furnace of pyrolysis. An electronic and electric scrap is crushing, drying up from surface water and warming on 2-4° C. above temperature of transporting air, divide into concoction nonferrous and precious metals and dielectric fraction, which go in furnace of pyrolysis by specified air, cleaned from dust and moistened up to 100% moisture by water. At mixing with dielectric fraction temperature of the air increases, relative moisture falls down to level, excluding condensation of moisture and spark formation in system. Pyrolysis is carried out under simultaneous neutralization of allocated hydrogen chloride by limestone with reception of calcium chloride. Gas allocated at pyrolysis condensing and dividing to water and organic phases (liquid fuel). Solid products of pyrolysis together with ash and slag supplied from landfill blade of heat power station, washing by specified water phase for dissolving of calcium chloride and extracting ions of heavy metals, then centrifuging. Filtrate and washing water cleanse from heavy metals. Solid products of pyrolysis move for incineration in combustion chamber. Combustion chamber slag, cleanse from heavy metals and not burned-out fuel in slag of heat power station, cool by air, which is then used in combustion chamber. Slag concrete products expose by the thermohumid processing by part of humid chimney gases after drying the calcium chloride, the other part gas is going to production of the carbonic acid.

Abstract translation: 一个市政或类似的垃圾是破碎的，分离黑色金属，与粉碎的石灰石混合，干燥和加热炉中的热解。 电子和电动废料粉碎，从地表水中干燥并在高于运输空气温度的2-4℃下变暖，分为混合有色金属和贵金属和介电分数，通过特定空气进行热解炉 从灰尘中吸水至100％。 在混合空气的介电分数温度升高时，相对湿度下降到水平，不包括系统中水分和火花形成的结露。 在石灰石中接受氯化钙同时中和所分配的氯化氢进行热解。 在热解冷凝中分配的气体，分为水和有机相（液体燃料）。 固体产物与热电厂垃圾填埋场灰渣和渣混合，用特定的水相洗涤，溶解氯化钙并提取重金属离子，然后离心。 从重金属中过滤并清洗水。 热解固体产物在燃烧室内焚化。 燃烧室炉渣，从重金属清洗，不会在发电厂炉渣中燃烧燃料，空气冷却，然后用于燃烧室。 炉渣混凝土产品在干燥氯化钙之后，通过部分潮湿的烟囱气体进行热湿机处理，另一部分气体将生产碳酸。

公开(公告)号：US07878131B2

公开(公告)日：2011-02-01

申请号：US11919039

申请日：2006-04-28

Applicant: Francesco Becchetti ,  Franz-Eicke Von Christen

Inventor： Francesco Becchetti ,  Franz-Eicke Von Christen

IPC: F23G5/02 ,  F23B90/00 ,  B02C21/00

CPC classification number: C10J3/66 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0956 ,  F23G5/0273 ,  F23G5/033 ,  F23G5/04 ,  F23G5/20 ,  F23G5/46 ,  F23G2201/101 ,  F23G2201/30 ,  F23G2201/40 ,  F23G2201/602 ,  F23G2201/80 ,  F23G2206/203 ,  F23J15/025 ,  F23J2215/60 ,  F23J2217/101 ,  F23J2217/102 ,  F23J2219/30 ,  F23J2219/80 ,  Y02E20/12 ,  Y02P20/125 ,  Y02P20/129

Abstract: Process for solid waste treatment, and particularly municipal solid waste, with recovery of the thermal energy, which is based on the general pyrolysis process modified in order to improve, on the one hand, the energy yield and, on the other, to reduce the quantity of unusable solid residues to be sent to the waste disposal, the unusable solid waste being limited to 10-15% of the total weight of the initial residue. The process and relative plant include a boosted treatment of the incoming waste, with a preliminary separation into three solid fractions, the first one of which is separately subjected to a preliminary drying step and the third one undergoes further shredding. The process and relative plant also include a section for recovering energy from the pyrolysis coke, wherein the latter is subjected to a thermochemical treatment with the production of a further quantity of synthesis gas.

Abstract translation: 固体废物处理方法，特别是城市固体废物，回收热能，这是基于改进的一般热解过程，一方面提高能量产出，另一方面减少 数量的不可用的固体残余物被送到废物处理中，不可用的固体废物被限制在初始残留物总重量的10-15％。 该方法和相关设备包括对进入的废物进行加强处理，初步分离成三个固体馏分，其中第一个单独进行预干燥步骤，第三个进行进一步粉碎。 该方法和相关工厂还包括用于从热解焦炭中回收能量的部分，其中后者通过再生产合成气进行热化学处理。

公开(公告)号：US20070251433A1

公开(公告)日：2007-11-01

申请号：US11393195

申请日：2006-03-30

Applicant: Yuriy Rabiner

Inventor： Yuriy Rabiner

IPC: F23G5/00

CPC classification number: F23G5/006 ,  B09B3/00 ,  C10B47/30 ,  C10B53/00 ,  C10J3/00 ,  C10J3/84 ,  C10J2300/0906 ,  C10J2300/0996 ,  F23G5/027 ,  F23G5/04 ,  F23G5/16 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/602 ,  F23G2201/701 ,  F23G2202/104 ,  F23G2206/10 ,  F23G2900/00001 ,  F23G2900/50205 ,  F23G2900/50401 ,  Y02E20/12 ,  Y02P20/129

Abstract: A municipal or like refuse is crushing, mixing with crushed limestone, dry up in two stages—by hot air and by part of solid products of pyrolysis which other part goes on washing out and filtration. Pyrolysis is carried out in two stages—due to heat of the specified part of solid products of pyrolysis and simultaneous neutralization of allocated hydrogen chloride by limestone with reception of calcium chloride, and then due to heat of final chimney gases of the combustion chamber, where in three stages the washed solid products of pyrolysis preliminary drained by a part of combustion chamber slag are burnt together with liquid and gaseous products of pyrolysis. Gas allocated at pyrolysis condense and divide on organic, which is liquid fuel and water phases. Air after a dryer moves to blowing away of light organic substances from the specified water phase, is heated up due to heat of slag and moves in combustion chamber. Washing water goes on allocation of salts of heavy metals and calcium chloride, and slag after molding of a concrete mixture goes to the chamber of thermohumid processing of the slag concrete by a part of damp chimney gases after drying calcium chloride, other part of gases moves to manufacture of liquid carbon dioxide.

Abstract translation: 市政或类似的垃圾粉碎，与粉碎的石灰石混合，分两个阶段干燥 - 热空气和部分热解固体产物，其他部分进行清洗和过滤。 热分解由两个阶段进行 - 由于特定部分的热解固体产物的热量，并且由接收氯化钙的石灰石同时中和所分配的氯化氢，然后由于燃烧室的最终烟囱气体的热量，其中 在三个阶段中，通过一部分燃烧室炉渣预先排出的经过热分解的洗涤固体产物与热解的液体和气体产物一起燃烧。 在热解过程中分配的气体有机分解，分为液体燃料和水相。 干燥器之后的空气移动以从指定的水相吹走轻质有机物质，由于炉渣的热量而被加热并在燃烧室中移动。 洗涤水分配重金属和氯化钙的盐，混凝土混合物成型后的炉渣在干燥氯化钙后，通过一部分潮湿的烟囱气体进入炉渣混合物的热湿机加工室，其他部分气体移动 制造液态二氧化碳。