公开(公告)号：US20120145051A1

公开(公告)日：2012-06-14

申请号：US13261112

申请日：2010-06-29

Applicant: John Gerard Sweeney

Inventor： John Gerard Sweeney

IPC: F23G5/04

CPC classification number: F23G5/027 ,  F23G5/04 ,  F23G5/16 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/603 ,  F23G2202/103 ,  Y02E20/12

Abstract: A system and method of integrated waste management having a source of a combustible waste material, a separator for separating the combustible waste material from a recyclable material, an airless drier for drying the combustible waste material to generate a pyrolysis feedstock, and a pyrolyser for pyrolysing the pyrolysis feedstock to form char and pyrogas. The system and method for power generation may also use an oxidiser for the high-temperature oxidation of syngas generated from the pyrolysis feedstock to generate heat for power production.

Abstract translation: 一种具有可燃废料来源的综合废物管理系统和方法，用于从可回收材料中分离可燃废料的分离器，用于干燥可燃废料以产生热解原料的无空气干燥器，以及用于热解的热解器 热解原料形成焦炭和焦糖。 用于发电的系统和方法还可以使用氧化剂用于从热解原料产生的合成气的高温氧化，以产生用于发电的热量。

公开(公告)号：US20120124960A1

公开(公告)日：2012-05-24

申请号：US13363904

申请日：2012-02-01

Applicant: Chris Chapman ,  David Ovens ,  David Deegan ,  Saeed Ismail

Inventor： Chris Chapman ,  David Ovens ,  David Deegan ,  Saeed Ismail

IPC: F02C6/00 ,  C10B49/02 ,  C10B57/18 ,  C10B57/00

CPC classification number: F23G5/027 ,  F23G5/006 ,  F23G5/02 ,  F23G5/085 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/50 ,  F23G2204/201 ,  F23G2206/203 ,  F23G2900/50208 ,  Y02E20/12

Abstract: A process for the treatment of waste, the process comprising either a gasification step or a pyrolysis step to produce an offgas and a non-airborne, solid char material; followed by a a plasma treatment step. An associated apparatus having a plasma treatment unit which is separate from the gasification unit or pyrolysis unit.

Abstract translation: 用于处理废物的方法，该方法包括气化步骤或热解步骤以产生废气和非空气传播的固体炭材料; 然后进行等离子体处理步骤。 具有与气化单元或热解单元分离的等离子体处理单元的相关装置。

公开(公告)号：US20120122046A1

公开(公告)日：2012-05-17

申请号：US13264986

申请日：2010-04-19

Applicant: Panayotis Tsantrizos ,  Stephan Lavigne

Inventor： Panayotis Tsantrizos ,  Stephan Lavigne

IPC: F27D19/00 ,  F27D21/00

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.

Abstract translation: 气化器用于将启动热源与粗合成气燃烧混合以驱动废物的气化。 燃烧烟气可以保持在650℃以上，直到达到骤冷以防止形成二恶英。 过热通过热回收单元释放。 气化炉可以以批量方式运行，以便对小型设施（如船舶，公寓，医院和住宅）进行有效处理小批量的废物。

公开(公告)号：US20120079970A1

公开(公告)日：2012-04-05

申请号：US13244180

申请日：2011-09-23

Applicant: Masamoto Kaneko

Inventor： Masamoto Kaneko

IPC: F23G5/027

CPC classification number: F23G5/027 ,  F23G5/16 ,  F23G5/50 ,  F23G2201/303 ,  F23G2201/40 ,  F23G2206/202 ,  F23G2207/101 ,  F23G2207/30 ,  F23L2900/07005 ,  F23L2900/07006 ,  Y02E20/344 ,  Y02E50/30

Abstract: Provided is a dry distillation and gasification typed incinerator capable of saving time and fuels required for combustion aid. In a first phase when a waste material A stored in a dry distillation furnace 1 is ignited till a fire bed is formed, the dry distillation and gasification typed incinerator supplies air to the dry distillation furnace 1 through an air supply passage 13. When the waste material A is in a continuous combustion state (a second phase), the oxygen supply to the dry distillation furnace 1 is switched from the air supply by the air supply passage 13 to the concentrated oxygen supply by an oxygen supply passage 15.

Abstract translation: 提供了能够节省燃烧助剂所需的时间和燃料的干馏和气化式焚烧炉。 在第一阶段，当储存在干馏炉1中的废料A被点燃直到形成火床时，干馏和气化型焚化炉通过供气通道13向干馏炉1供应空气。当废物 材料A处于连续燃烧状态（第二阶段），将供给到干馏炉1的供氧通过供气通道13从供气通道13供给到供氧通道15的浓氧供给。

公开(公告)号：US20120073185A1

公开(公告)日：2012-03-29

申请号：US13375351

申请日：2010-06-01

Applicant: Pekka Jokela ,  Lehto Jani

Inventor： Pekka Jokela ,  Lehto Jani

IPC: C10L1/00 ,  C10L5/00

CPC classification number: C10B49/22 ,  C10B49/10 ,  C10B49/16 ,  C10B53/00 ,  C10B53/02 ,  C10B55/10 ,  C10B57/10 ,  C10G1/02 ,  C10G9/32 ,  F23C10/002 ,  F23G2201/303 ,  F23G2203/501 ,  F23G2203/504 ,  F23G2206/10 ,  Y02E50/14

Abstract: The invention relates to a method of carrying out pyrolysis process in a pyrolysis reactor (4) for solid fuel to produce pyrolysis oil. The method comprises supplying solid fuel into a drying zone in the pyrolysis reactor (4) for removing moisture containing gases, drying the solid fuel in the drying zone and extracting the moisture containing gases re-moved from the solid fuel out of the pyrolysis reactor (4), passing the dried solid fuel from the drying zone to the pyrolysis zone of the pyrolysis reactor (4), pyrolyzing the dried solid fuel for separating pyrolysis gases from the dried solid fuel and conducting the pyrolysis gases from the pyrolysis reactor (4) to a condenser (8) for producing pyrolysis oil.

Abstract translation: 本发明涉及在用于固体燃料的热解反应器（4）中进行热解过程以产生热解油的方法。 该方法包括将固体燃料供应到热解反应器（4）中的干燥区中，用于除去含湿气体，干燥干燥区中的固体燃料并将从固体燃料中重新移出的含水气体从热解反应器中提取出来 4），将干燥的固体燃料从干燥区传送到热解反应器（4）的热解区，热解干燥的固体燃料以从干燥的固体燃料中分离热解气体并将热解气体从热解反应器（4）导入， 到用于产生热解油的冷凝器（8）。

公开(公告)号：US20110303134A1

公开(公告)日：2011-12-15

申请号：US13138436

申请日：2010-03-10

Applicant: Ivan A. Lim ,  Roderick Sison Dayot ,  Rodolfo Akol Dayot

Inventor： Ivan A. Lim ,  Roderick Sison Dayot ,  Rodolfo Akol Dayot

IPC: F23G5/00

CPC classification number: C10J3/66 ,  C10J2300/0916 ,  C10J2300/1807 ,  F23G5/027 ,  F23G7/12 ,  F23G2201/303 ,  F23G2206/10 ,  F23G2209/26 ,  F23G2209/28 ,  Y02P20/145

Abstract: Waste burning means, gas treating means in communication with said waste burning means and gas separating means in communication with said gas treating means and waste burning means, said waste burning means includes a burning chamber and pressurized pyrolysis chamber, wherein burning chamber is being made such that it is capable of burning completely organic wastes thereof, whereby gas products of combustion are produced, and said pyrolysis chamber being made such that it is capable of converting plastic wastes into synthesis gases through utilization of heat from the burning chamber, heat exchanging means disposed within the burning chamber being arranged in a manner wherein water from a water source is capable of conversion into steam thereof through utilization of heat in the burning chamber, said gas treating means includes a secondary treatment chamber in communication with the burning chamber, wherein high temperature gas products of combustion coming from the burning chamber is capable of mixing with low temperature steam, said gas separating means being arranged such that the gas products mixed with steam coming from the gas treating means is capable of swirling cyclonic motion thereof, thereby allowing the lighter gases to be discharged to the atmosphere and be separated from particulates and heavier gases which are subsequently recycled and feed back into the burning chamber, and steam and synthesis gas lines provided in the waste burning means being arranged such that it is capable of introduction to the burning chamber the steam produced by the heat exchanging means and synthesis gas coming from the pyrolysis chamber.

Abstract translation: 废燃烧装置，与所述废燃烧装置连通的气体处理装置和与所述气体处理装置和废气燃烧装置连通的气体分离装置，所述废燃烧装置包括燃烧室和加压热解室，其中燃烧室正在被制成 其能够完全燃烧其有机废物，由此产生燃烧气体产物，并且所述热解室被制成使得能够通过利用来自燃烧室的热量将塑料废物转化为合成气体，设置热交换装置 在燃烧室内以这样一种方式布置，其中来自水源的水能够通过在燃烧室中的热量转化为蒸汽，所述气体处理装置包括与燃烧室连通的二级处理室，其中高温 来自燃烧室的燃烧气体产品是 能够与低温蒸汽混合，所述气体分离装置被布置成使得与来自气体处理装置的蒸汽混合的气体产物能够旋转其旋风运动，从而允许较轻的气体排放到大气中并分离 来自颗粒和较重的气体，其随后被再循环并进入燃烧室，并且设置在废燃烧装置中的蒸汽和合成气管线被布置成使得其能够将由热交换装置产生的蒸汽引入燃烧室 和来自热解室的合成气。

公开(公告)号：US08069581B2

公开(公告)日：2011-12-06

申请号：US12190953

申请日：2008-08-13

Applicant: Sang Ahn Ha ,  Hyuk Mok Choi

Inventor： Sang Ahn Ha ,  Hyuk Mok Choi

IPC: F26B17/00 ,  F26B23/08

CPC classification number: B09C1/06 ,  B09C1/00 ,  F23G5/0273 ,  F23G5/20 ,  F23G7/14 ,  F23G2201/303 ,  F23G2204/203 ,  F23G2900/50205 ,  F26B23/022

Abstract: Disclosed herein is a system for purifying contaminated soil, which restores soil contaminated by a variety of pollutants to the condition before the contamination, and which itself provides the driving source required for the purification. The system includes: a dryer which dries contaminated soil, separates waste gas generated during the drying from the contaminated soil, and discharges the waste gas; a pyrolysis apparatus which indirectly heats the dried contaminated soil in a hermetic condition to divide the contaminated soil into purified soil and pyrolysis gas, and separately discharges the purified soil and the pyrolysis gas; a transfer fan for forcibly transferring the discharged pyrolysis gas; a burner for oxidizing the waste gas discharged from the dryer and the pyrolysis gas forcibly transferred by the transfer fan, to heat the pyrolysis apparatus; and a cooling facility for directly spraying cooling water on the discharged purified soil to cool the purified soil.

Abstract translation: 本文公开了一种净化污染土壤的系统，其将污染了各种污染物的土壤恢复到污染前的状态，并且其本身提供净化所需的驱动源。 该系统包括：干燥污染土壤的干燥器，将干燥过程中产生的废气与污染土壤分离，排放废气; 一种热解装置，以密封状态间接加热干燥的污染土壤，将污染土壤分解成纯净土壤和热解气，并分离排出纯化土壤和热解气体; 用于强制转移排出的热解气体的转移风扇; 用于氧化从干燥器排出的废气的燃烧器和由传送风扇强制转移的热解气体，以加热该热解装置; 以及用于在排出的净化土壤上直接喷洒冷却水以冷却纯化的土壤的冷却设备。

公开(公告)号：US20110271882A1

公开(公告)日：2011-11-10

申请号：US13081749

申请日：2011-04-07

Applicant: Cameron Cole ,  Toby L. Cole ,  Dan Watts ,  Raul de la Torres ,  Michael Scott Sorrell

Inventor： Cameron Cole ,  Toby L. Cole ,  Dan Watts ,  Raul de la Torres ,  Michael Scott Sorrell

IPC: F23G5/00

CPC classification number: F23G5/027 ,  F23G5/12 ,  F23G5/16 ,  F23G2201/303

Abstract: A waste treatment system is disclosed having: (1) a pyrolyzer comprising an inner and outer chamber, wherein the inner chamber further comprises a syngas outlet; (2) a thermal oxidizer comprising an elongated combustion chamber; (3) an exhaust gas transfer duct fluidly coupled to the combustion chamber of the thermal oxidizer and the outer chamber of the pyrolyzer; and (4) a particulate separator for removing particulates from the syngas. In preferred embodiments the pyrolyzer and the thermal oxidizer are aligned in piggybacked configuration, such that the hot exhaust gases from the thermal oxidizer are shunted back to the outer chamber of the pyrolyzer. Preferred thermal oxidizer and the exhaust gas transfer duct are configured to allow a three second residence time of the syngas, such that the system operates at an efficiency of at least 15 therms (thm) per ton of municipal waste.

Abstract translation: 公开了一种废物处理系统，其具有：（1）包括内室和外室的热解器，其中所述内室还包括合成气出口; （2）热氧化器，其包括细长的燃烧室; （3）流体耦合到所述热氧化剂的燃烧室和所述热解器的外部室的废气输送管道; 和（4）用于从合成气中除去微粒的颗粒分离器。 在优选的实施方案中，热解器和热氧化剂以搭载的构型对准，使得来自热氧化器的热废气被分流回到热解器的外部室。 优选的热氧化剂和废气输送管道被配置为允许合成气的三秒停留时间，使得系统以每吨城市废物至少15个硫酸盐（thm）的效率运行。

公开(公告)号：US08020499B2

公开(公告)日：2011-09-20

申请号：US11937996

申请日：2007-11-09

Applicant: Wai Tak Chu ,  Chi Wai Hui ,  Bai Ru He ,  Zhi Qiang Wu ,  King Lung Lee ,  Chin Man Lee

Inventor： Wai Tak Chu ,  Chi Wai Hui ,  Bai Ru He ,  Zhi Qiang Wu ,  King Lung Lee ,  Chin Man Lee

IPC: F23G5/12

CPC classification number: F23G5/006 ,  F23G5/0276 ,  F23G5/12 ,  F23G5/46 ,  F23G7/12 ,  F23G2201/301 ,  F23G2201/302 ,  F23G2201/303 ,  F23G2201/80 ,  F23G2205/121 ,  F23G2205/18 ,  F23G2206/10 ,  F23G2209/281

Abstract: A reactor (107) for pyrolysis of carbonizable plastic and rubber materials is disclosed including at least an earlier stage reaction chamber (401) and a later stage reaction chamber (105), in which the earlier stage reaction chamber receives the materials for pyrolysis, and the later stage reaction chamber receives treated materials from the earlier stage reaction chamber for subsequent pyrolysis, and the reactor (107) includes a three-way valve (407) for directing the gaseous pyrolysis products from the later stage reaction chamber to one of three pathways, each to a different destination.

Abstract translation: 公开了一种用于碳化塑料和橡胶材料的热解的反应器（107），其包括至少较早阶段的反应室（401）和较后阶段的反应室（105），其中较早阶段的反应室容纳用于热解的材料，以及 后期反应室接收来自较早阶段反应室的经处理的材料用于随后的热解，并且反应器（107）包括用于将气态热解产物从后期反应室引导至三个通路之一的三通阀（407） ，每个到不同的目的地。

公开(公告)号：US20110030590A1

公开(公告)日：2011-02-10

申请号：US12856046

申请日：2010-08-13

Applicant: Kenneth Davison ,  Neal Stroulger ,  Dave Berner

Inventor： Kenneth Davison ,  Neal Stroulger ,  Dave Berner

IPC: F23G5/12

CPC classification number: F23B90/06 ,  C10J3/22 ,  C10J3/34 ,  C10J3/36 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/152 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/1876 ,  F23G5/0276 ,  F23G5/46 ,  F23G7/10 ,  F23G2201/303

Abstract: An apparatus for gasifying solid organic fuel includes a refractory-lined oxidation chamber, fuel storage, a transfer connecting the fuel storage with an inlet into the oxidation chamber for transferring in an upwardly inclined direction the solid fuel from the fuel storage into the inlet to form an upwardly mounded fuel bed. An oxidant is supplied into the fuel bed to gasify the organic materials in the fuel to produce a gaseous effluent from the fuel bed, thereby leaving a residue of the fuel. The residue drops through an opening under the oxidation chamber onto a residue removal transfer. The oxidant is supplied through a plurality of perforated air distribution members extending across the fuel bed cavity in the oxidation chamber so as to introduce air into the interior of the fuel bed to thereby promote evenly distributed gasification, evenly distributed through the fuel bed.

Abstract translation: 用于气化固体有机燃料的装置包括耐火材料衬里的氧化室，燃料储存器，将燃料储存器与入口连接到氧化室中的转移装置，用于沿向上倾斜的方向将固体燃料从燃料储存器转移到入口中以形成 一个向上堆积的燃料床。 将氧化剂供入到燃料床中以气化燃料中的有机材料以产生来自燃料床的气态流出物，从而留下燃料残余物。 残留物通过氧化室下面的开口滴落到残留物去除转移物上。 氧化剂通过穿过氧化室中的燃料床腔延伸的多个穿孔空气分配构件供应，以将空气引入燃料床的内部，从而促进均匀分布的气化，均匀分布在燃料床上。