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：US5713195A

公开(公告)日：1998-02-03

申请号：US689492

申请日：1996-08-07

Applicant: Lucien Y. Bronicki ,  Joseph Sinai ,  Benjamin Doron ,  Uri Kaplan

Inventor： Lucien Y. Bronicki ,  Joseph Sinai ,  Benjamin Doron ,  Uri Kaplan

IPC: F01K23/06 ,  F02C3/20 ,  F02C3/28 ,  F23G5/027 ,  F02C6/18

CPC classification number: F23G5/027 ,  F01K23/061 ,  F01K23/067 ,  F02C3/205 ,  F02C3/28 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2203/50 ,  F23G2206/203 ,  F23G2900/7013 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18

Abstract: A power plant includes a gas turbine unit having a compressor for compressing ambient air, a burner for burning fuel and heating air compressed by said compressor, and a turbine for expanding air heated by said burner to drive said compressor and produce hot exhaust gases. The plant further includes a combustor for containing particles of solid fuel which are fluidized by the exhaust gases from the turbine to produce hot products of combustion that include coarse ash particulate. Apparatus is provided for generating power from the hot products of combustion.

Abstract translation: 发电厂包括具有用于压缩环境空气的压缩机的燃气轮机单元，用于燃烧燃料的燃烧器和由所述压缩机压缩的加热空气的燃气轮机，以及用于膨胀由所述燃烧器加热的空气以驱动所述压缩机并产生热废气的涡轮机。 该设备还包括用于容纳固体燃料颗粒的燃烧器，其由来自涡轮机的废气流化以产生包括粗灰分颗粒的热的燃烧产物。 提供了用于从热燃烧产物发电的装置。

公开(公告)号：US5550312A

公开(公告)日：1996-08-27

申请号：US384696

申请日：1995-02-06

Applicant: Manfred Schingnitz ,  Peter Gohler ,  Heinz Martin

Inventor： Manfred Schingnitz ,  Peter Gohler ,  Heinz Martin

IPC: C10J3/46 ,  C10J3/66 ,  C21B5/02 ,  F23G5/027 ,  B09B3/00 ,  A62D3/00 ,  C02F1/00 ,  C22B7/00

CPC classification number: F23G5/0273 ,  C10J3/005 ,  C10J3/466 ,  C10J3/526 ,  C10J3/66 ,  C10J3/84 ,  C10K1/002 ,  C10K1/004 ,  C10K1/101 ,  C21B5/026 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/1223 ,  C10J2300/1246 ,  C10J2300/1631 ,  C10J2300/1884 ,  F23G2201/301 ,  F23G2201/302 ,  F23G2201/303 ,  F23G2201/304 ,  Y02P10/212 ,  Y10S423/18

Abstract: A method for the thermal utilization of combustible components of waste materials of different properties and origin, independently of the degree of contamination with heavy metals and toxic organic compounds or organic chlorine-containing compounds. The waste materials are subjected to the method steps of pyrolysis, comminution, classification, gasification and gas purification in order to produce a clean gas which can be used for various purposes and as a source of energy and an elution-proof, mineral, solid residue which can be easily disposed of.

Abstract translation: 用于不同性质和来源的废料可燃组分的热利用方法，与重金属和有机有机化合物或有机含氯化合物的污染程度无关。 废料经受热解，粉碎，分级，气化和气体净化的方法步骤，以产生可用于各种目的的清洁气体，作为能量来源和耐洗脱的矿物，固体残余物 这可以很容易地处理。

公开(公告)号：US5302118A

公开(公告)日：1994-04-12

申请号：US14767

申请日：1993-02-08

Applicant: James G. Renegar ,  Malcolm L. Swanson

Inventor： James G. Renegar ,  Malcolm L. Swanson

IPC: B09C1/06 ,  F23G5/027 ,  F23G7/14 ,  F26B11/02 ,  F27B7/00

CPC classification number: B09C1/06 ,  F23G5/027 ,  F23G7/14 ,  F26B11/026 ,  F26B11/028 ,  F23G2201/301 ,  F23G2201/50

Abstract: An apparatus and method for decontaminating petroleum contaminated soil and the like, and which comprises a rotary drum dryer which is adapted to convey the soil therethrough, and which includes a burner at one end for generating a heated gas stream which passes through the dryer to heat the soil to a temperature sufficient to volatilize the contaminates. A fixed enclosure is mounted to surround the discharge end of the dryer and the enclosure receives the heated soil as it is discharged from the dryer. Any entrained dust particles which are withdrawn with the exhaust gas stream from the dryer, and which may remain contaminated, are separated from the gas stream and returned to the enclosure. In the enclosure, the returned dust is mixed with the heated soil so as to cause the dust to be heated and to release its volatile contaminates, without risk of the returned dust being again entrained in the gas stream flowing through the dryer. Also, the volatilized contaminates released from the dust will be drawn back into the gas stream passing through the dryer and a significant portion thereof will be oxidized by the burner flame.

Abstract translation: 一种用于净化石油污染的土壤等的装置和方法，其包括适于输送土壤的旋转滚筒干燥器，其一端包括燃烧器，用于产生通过干燥器加热的加热气流 土壤达到足以挥发污染物的温度。 安装固定的外壳以围绕干燥器的排出端，并且外壳在从干燥器排出时接收加热的土壤。 与来自干燥器的废气流一起排出且可能被污染的任何夹带的尘埃颗粒与气流分离并返回到外壳。 在外壳中，返回的灰尘与加热的土壤混合，以使灰尘被加热并释放其挥发性污染物，而不会将返回的灰尘再次夹带在流过干燥器的气流中。 此外，从灰尘释放的挥发的污染物将被吸回到通过干燥器的气流中，其显着部分将被燃烧器火焰氧化。

公开(公告)号：US4206186A

公开(公告)日：1980-06-03

申请号：US869147

申请日：1978-01-13

Applicant: Heinz Holter ,  Heinz Gresch ,  Heinrich Igelbuscher

Inventor： Heinz Holter ,  Heinz Gresch ,  Heinrich Igelbuscher

IPC: B01D53/02 ,  B01D53/34 ,  B01D53/60 ,  B01D53/62 ,  B01D53/72 ,  C10B47/28 ,  C10B53/00 ,  C10K1/02 ,  C10K1/18 ,  C10K1/20 ,  F23G5/027

CPC classification number: C10G49/007 ,  B01D53/02 ,  B01D53/34 ,  B01D53/60 ,  B01D53/62 ,  B01D53/72 ,  C10B47/28 ,  C10B53/00 ,  C10K1/02 ,  C10K1/18 ,  C10K1/20 ,  F23G5/0273 ,  F23G2201/301 ,  F23G2201/303 ,  Y10S423/18

Abstract: Organic refuse is pyrolyzed to form disposable solids and gas. The gas is washed at a temperature well above 100.degree. C. with wash oil, which is recirculated. Spent wash oil is pyrolyzed with contaminants and further organic refuse. The washed gas is filtered through sorption means to remove acid and or other noxious gases therefrom before being cooled well below 100.degree. C. to condense water vapor and other constituents having boiling points within the range of from, e.g., 75.degree. to 150.degree. C. After separating the resulting condensate, thus-purified combustion gas is used, e.g., as a fuel source for the organic-refuse pyrolysis.

Abstract translation: 有机垃圾被热解以形成一次性固体和气体。 气体在高于100℃的温度下用洗涤油进行洗涤，再循环。 废洗油被污染物和进一步的有机垃圾热解。 洗涤过的气体通过吸附装置过滤，以在冷却到100℃以下以冷凝水蒸气和沸点在例如75℃至150℃范围内的其它组分，从而除去酸和其它有害气体 在分离所得的冷凝物之后，使用如此纯化的燃烧气体，例如用作有机 - 垃圾热解的燃料源。

公开(公告)号：US3859933A

公开(公告)日：1975-01-14

申请号：US39041173

申请日：1973-08-22

Applicant: MANNESMANN AG

Inventor： VON KLENCK JURGEN

IPC: C02F11/10 ,  F23G5/00 ,  F23G5/027 ,  F23G5/20 ,  F23G7/00

CPC classification number: C02F11/10 ,  F23G5/006 ,  F23G5/0273 ,  F23G2201/301 ,  F23G2201/302 ,  Y02W10/40

Abstract: In a method for the combined processing for disposal of industrial, problem waste, of problem free waste and of slush as resulting from sewage treatment, wherein the problem waste is pyrolytically carbonized on a continuous, revolving basis, and wherein the resulting coke is mixed with heated acidized slush, filtered and drained. The gas developed during carbonization is washed and used as heating agent; the mixture is then mixed with problem free waste to obtain a coke-slush waste mixture and the said latter mixture is burnt.

Abstract translation: 在处理工业废弃物，问题浪费，无污染废物和由污水处理引起的泥沙的组合处理方法中，其中问题浪费在连续，循环的基础上被热解碳化，并且其中将所得焦炭与 加热酸化的泥浆，过滤并排干。 在碳化过程中发生的气体被洗涤并用作加热剂; 然后将混合物与无问题的废物混合以获得焦炭废料混合物，并将所述后者混合物燃烧。

公开(公告)号：US3639111A

公开(公告)日：1972-02-01

申请号：US3639111D

申请日：1969-01-30

Applicant: UNIV CALIFORNIA

Inventor： BRINK DAVID L ,  THOMAS JEROME F

IPC: B01D53/52 ,  C10B53/00 ,  C10J3/00 ,  F23G5/027 ,  F23G7/04 ,  C10J3/10 ,  C10J3/14 ,  C10J3/20

CPC classification number: F23G5/027 ,  B01D53/523 ,  C10B53/00 ,  C10J3/00 ,  C10J3/26 ,  C10J3/721 ,  C10J3/723 ,  C10J3/74 ,  C10J3/84 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0996 ,  C10J2300/1253 ,  C10J2300/1869 ,  C10J2300/1884 ,  C10J2300/1892 ,  F23G7/04 ,  F23G2201/101 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2206/203 ,  Y02E20/12

Abstract: Organic material, such as kraft black liquor, organic fuels, garbage and organic wastes, is destructively distilled and pyrolyzed at an elevated temperature and for a time sufficient to break down the material to noncombustible solids and to a stable gaseous clean burning fuel. The temperature is maintained to preclude recombination of intermediate products formed during the pyrolysis and which would otherwise pollute the atmosphere. A controlled amount of oxygen is continuously introduced during the cracking to provide energy by exothermic oxidative reactions but the oxygen is insufficient to effect stoichiometric or in other words complete combustion.

Abstract translation: 诸如牛皮纸黑液，有机燃料，垃圾和有机废物的有机材料在高温下被破坏性地蒸馏和热解，并且足以将材料分解成不可燃固体和稳定的气体清洁燃烧燃料的时间。 保持温度以排除在热解期间形成的中间产物的重组，否则会污染大气。 在裂化期间连续引入受控量的氧以通过放热氧化反应提供能量，但氧不足以实现化学计量或换句话说完全燃烧。

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.

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.

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

IPC: C10B53/07 ,  C01B3/02 ,  C10K3/06 ,  C10B27/06 ,  C10B7/10

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.