公开(公告)号：US08419902B2

公开(公告)日：2013-04-16

申请号：US12454502

申请日：2009-05-19

Applicant: Arkady Feerer ,  Marat Hasbulatovich Kulakov ,  Denis Zagorsky

Inventor： Arkady Feerer ,  Marat Hasbulatovich Kulakov ,  Denis Zagorsky

IPC: C10B1/00 ,  C10B7/10

CPC classification number: C10K1/12 ,  C10B47/44 ,  C10B53/00 ,  C10K1/101 ,  C10K1/103 ,  F02C3/28 ,  F05D2220/75 ,  F23G5/006 ,  F23G5/02 ,  F23G2201/10 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2205/121 ,  F23G2206/202 ,  F23G2206/203 ,  Y02E20/12 ,  Y02E50/12

Abstract: Proposed are a system and method for wasteless pyrolytic processing and complete utilization of municipal and domestic wastes. The wastes are sequentially passed through units of sorting, grinding, drying, accumulating, and sending to a pyrolysis reactor for pyrolytic treatment. The syngas produced in the pyrolysis is passed through dry cleaning, dust catching, a first wet cleaning with water, a second wet cleaning with alkali, and a floatation unit for separation of water which is purified to an extent sufficient for technical use. The purified syngas is also passed through an absorber and is then used as a working medium for a power generation unit such as a gas turbine co-generator that generates electricity. Solid products of the pyrolysis reaction, such as coke, are returned to the reactor for afterburning, and the heat of the reaction can be utilized in a dryer, or the like.

Abstract translation: 提出了无废热解热处理和完全利用城市和家庭废物的系统和方法。 废物依次通过分选，研磨，干燥，积聚和送到热解反应器进行热解处理。 在热解中产生的合成气通过干洗，吸尘，用水进行第一次湿式清洗，第二次用碱洗涤，以及用于分离水的漂浮单元，其被纯化至足以用于技术用途的程度。 纯化的合成气也通过吸收器，然后用作发电单元（例如发电的燃气轮机共发电机）的工作介质。 将热解反应的固体产物（如焦炭）返回反应器进行后燃，反应热可用于干燥器等中。

公开(公告)号：US20120312026A9

公开(公告)日：2012-12-13

申请号：US13135379

申请日：2011-07-01

Applicant: Robert G. Graham

Inventor： Robert G. Graham

IPC: F02C3/28 ,  F23G5/00 ,  F02G1/00 ,  F23L5/04 ,  F23G5/027

CPC classification number: C10J3/30 ,  C10J3/20 ,  C10J3/34 ,  C10J3/723 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1687 ,  C10J2300/1876 ,  F23G5/027 ,  F23G5/24 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/303 ,  F23G2206/10 ,  F23G2206/202 ,  F23G2207/101 ,  Y02E20/12 ,  Y02E50/12 ,  Y02E50/14 ,  Y02P20/124 ,  Y02P20/129

Abstract: Pyrolyzing gasification system and method of use including primary combustion of non-uniform solid fuels such as biomass and solid wastes within a refractory lined gasifier, secondary combustion of primary combustion gas within a staged, cyclonic, refractory lined oxidizer, and heat energy recovery from the oxidized flue gas within an indirect air-to-air all-ceramic heat exchanger or external combustion engine. Primary combustion occurs at low substoichoimetric air percentages of 10-30 percent and at temperatures below 1000 degrees F. Secondary combustion is staged and controlled for low NOx formation and prevention of formation of CO, hydrocarbons, and VOCs. The gasifier includes a furnace bed segmented into individual cells, each cell is independently monitored using a ramp temperature probe, and provided with controlled air injection. Gasifier air injection includes tuyere arrays, lances, or both. The oxidizer includes three serially aligned stages separated by air injecting baffles, and ability to adjust the exit air temperature.

Abstract translation: 热解气化系统和使用方法，包括在耐火材料衬里气化器内的非均匀固体燃料如生物质和固体废物的初级燃烧，分级，旋风，耐火衬里氧化剂中的一级燃烧气体的二次燃烧和从 间接空气 - 空气全陶瓷换热器或外燃机中的氧化烟气。 初级燃烧发生在10-30％低于1000°F的低次光气空气百分比下，二级燃烧分级和控制，用于低NOx形成和防止CO，烃和VOC的形成。 气化器包括分段成单个电池的炉床，每个电池使用斜坡温度探头独立监测，并提供受控空气注入。 气化器空气注入包括风口阵列，喷枪或两者。 氧化剂包括由空气注入隔板分开的三个串联排列的阶段，以及调节出口空气温度的能力。

公开(公告)号：US20120036778A1

公开(公告)日：2012-02-16

申请号：US13042220

申请日：2011-03-07

Applicant: Sergii Y. Stryzhak

Inventor： Sergii Y. Stryzhak

IPC: B01J7/00 ,  C10L3/00

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加工装置，以及其它含碳原料转化为可燃气化气体的方法和用于热解和向下气化过程的方法。

公开(公告)号：US20110265489A1

公开(公告)日：2011-11-03

申请号：US13135379

申请日：2011-07-01

Applicant: Robert G. Graham

Inventor： Robert G. Graham

IPC: F02C3/28 ,  F23G5/00 ,  F02G1/00 ,  F23L5/04 ,  F23G5/027

CPC classification number: C10J3/30 ,  C10J3/20 ,  C10J3/34 ,  C10J3/723 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1687 ,  C10J2300/1876 ,  F23G5/027 ,  F23G5/24 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/303 ,  F23G2206/10 ,  F23G2206/202 ,  F23G2207/101 ,  Y02E20/12 ,  Y02E50/12 ,  Y02E50/14 ,  Y02P20/124 ,  Y02P20/129

Abstract: Pyrolyzing gasification system and method of use including primary combustion of non-uniform solid fuels such as biomass and solid wastes within a refractory lined gasifier, secondary combustion of primary combustion gas within a staged, cyclonic, refractory lined oxidizer, and heat energy recovery from the oxidized flue gas within an indirect air-to-air all-ceramic heat exchanger or external combustion engine. Primary combustion occurs at low substoichoimetric air percentages of 10-30 percent and at temperatures below 1000 degrees F. Secondary combustion is staged and controlled for low NOx formation and prevention of formation of CO, hydrocarbons, and VOCs. The gasifier includes a furnace bed segmented into individual cells, each cell is independently monitored using a ramp temperature probe, and provided with controlled air injection. Gasifier air injection includes tuyere arrays, lances, or both. The oxidizer includes three serially aligned stages separated by air injecting baffles, and ability to adjust the exit air temperature.

Abstract translation: 热解气化系统和使用方法，包括在耐火材料衬里气化器内的非均匀固体燃料如生物质和固体废物的初级燃烧，分级，旋风，耐火衬里氧化剂中的一级燃烧气体的二次燃烧和从 间接空气 - 空气全陶瓷换热器或外燃机中的氧化烟气。 初级燃烧发生在10-30％低于1000°F的低次光气空气百分比下，二级燃烧分级和控制，用于低NOx形成和防止CO，烃和VOC的形成。 气化器包括分段成单个电池的炉床，每个电池使用斜坡温度探头独立监测，并提供受控空气注入。 气化器空气注入包括风口阵列，喷枪或两者。 氧化剂包括由空气注入隔板分开的三个串联排列的阶段，以及调节出口空气温度的能力。

公开(公告)号：US08001912B2

公开(公告)日：2011-08-23

申请号：US12459318

申请日：2009-06-30

Applicant: Robert G. Graham

Inventor： Robert G. Graham

IPC: F23B10/00 ,  F23B90/00 ,  F23G5/027

CPC classification number: C10J3/30 ,  C10J3/20 ,  C10J3/34 ,  C10J3/723 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1687 ,  C10J2300/1876 ,  F23G5/027 ,  F23G5/24 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/303 ,  F23G2206/10 ,  F23G2206/202 ,  F23G2207/101 ,  Y02E20/12 ,  Y02E50/12 ,  Y02E50/14 ,  Y02P20/124 ,  Y02P20/129

Abstract: Pyrolyzing gasification system and method of use including primary combustion of non-uniform solid fuels such as biomass and solid wastes within a refractory lined gasifier, secondary combustion of primary combustion gas within a staged, cyclonic, refractory lined oxidizer, and heat energy recovery from the oxidized flue gas within an indirect air-to-air all-ceramic heat exchanger or external combustion engine. Primary combustion occurs at low substoichiometric air percentages of 10-30 percent and at temperatures below 1000 degrees F. Secondary combustion is staged and controlled for low NOx formation and prevention of formation of CO, hydrocarbons, and VOCs. The gasifier includes a furnace bed segmented into individual cells, each cell is independently monitored using a ramp temperature probe, and provided with controlled air injection. Gasifier air injection includes tuyere arrays, lances, or both. The oxidizer includes three serially aligned stages separated by air injecting baffles, and ability to adjust the exit air temperature.

Abstract translation: 热解气化系统和使用方法，包括在耐火材料衬里气化器内的非均匀固体燃料如生物质和固体废物的初级燃烧，分级，旋风，耐火衬里氧化剂中的一级燃烧气体的二次燃烧和从 间接空气 - 空气全陶瓷换热器或外燃机中的氧化烟气。 初级燃烧发生在10-30％的低亚化学计量空气百分比和低于1000华氏度的温度下。二次燃烧分级和控制，用于低NOx形成和防止CO，烃和VOC的形成。 气化器包括分段成单个电池的炉床，每个电池使用斜坡温度探头独立监测，并提供受控空气注入。 气化器空气注入包括风口阵列，喷枪或两者。 氧化剂包括由空气注入隔板分开的三个串联排列的阶段，以及调节出口空气温度的能力。

公开(公告)号：US20110036280A1

公开(公告)日：2011-02-17

申请号：US12848451

申请日：2010-08-02

Applicant: Bruce Toase ,  David Sweeting ,  Scott Edmondson

Inventor： Bruce Toase ,  David Sweeting ,  Scott Edmondson

IPC: F23G5/00

CPC classification number: F23G5/027 ,  F23G5/033 ,  F23G5/46 ,  F23G5/50 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2206/10 ,  F23G2206/202 ,  F23G2206/203 ,  F23G2900/50209 ,  Y02E20/12

Abstract: A small scale integrated waste processing system for the thermal destructions of waste. The system comprises a compactor (12) for densifying waste and expressing air, a pyrolyzer (13) to receive waste delivered from the compactor, a gasifier (14) with an ash vessel (23) that receives dried waste, and an oxidizer (15) receiving gas from the gasifier to be combusted. Heat energy from the oxidizer can be routed back to the pyrolyzer.

Abstract translation: 一种用于浪费热量的小型综合废物处理系统。 该系统包括用于致密化废物和表达空气的压实机（12），用于接收从压实机输送的废物的热解器（13），具有接收干燥废物的灰分容器（23）的气化器（14）和氧化剂 ）接收来自要燃烧的气化器的气体。 来自氧化剂的热能可以返回到热解器。

公开(公告)号：US20100293956A1

公开(公告)日：2010-11-25

申请号：US12470293

申请日：2009-05-21

Applicant: Vaibhav Nadkarni

Inventor： Vaibhav Nadkarni

IPC: F02C7/22

CPC classification number: F23R3/286 ,  F23C2900/07001 ,  F23C2900/99011 ,  F23G5/027 ,  F23G2201/303 ,  F23G2201/40 ,  F23G2206/202 ,  F23G2206/203 ,  F23R2900/00002 ,  Y02E20/12

Abstract: A fuel nozzle auxiliary vane comprising a vane mountable base comprising a fuel inlet, wherein the vane mountable base is configured to mount to a surface of a main vane disposed in an airflow path of a fuel nozzle. The fuel nozzle auxiliary vane also includes a body extending from the vane mountable base, wherein the body comprises a fuel passage that turns from the fuel inlet to a fuel outlet, and the fuel outlet has a fuel outlet direction generally crosswise to a fuel inlet direction through the fuel inlet.

Abstract translation: 一种燃料喷嘴辅助叶片，包括具有燃料入口的叶片安装座，其中所述叶片可安装基座构造成安装到设置在燃料喷嘴的气流路径中的主叶片的表面。 燃料喷嘴辅助叶片还包括从叶片可安装基座延伸的主体，其中主体包括从燃料入口转向燃料出口的燃料通道，并且燃料出口具有大体上与燃料入口方向交叉的燃料出口方向 通过燃油进口。

公开(公告)号：US20100293853A1

公开(公告)日：2010-11-25

申请号：US12454502

申请日：2009-05-19

Applicant: Arkady Feerer ,  Marat Hasbulatovich Kulakov ,  Denis Zagorsky

Inventor： Arkady Feerer ,  Marat Hasbulatovich Kulakov ,  Denis Zagorsky

IPC: C10J3/68 ,  C10J3/00

CPC classification number: C10K1/12 ,  C10B47/44 ,  C10B53/00 ,  C10K1/101 ,  C10K1/103 ,  F02C3/28 ,  F05D2220/75 ,  F23G5/006 ,  F23G5/02 ,  F23G2201/10 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2205/121 ,  F23G2206/202 ,  F23G2206/203 ,  Y02E20/12 ,  Y02E50/12

Abstract: Proposed are a system and method for wasteless pyrolytic processing and complete utilization of municipal and domestic wastes. The wastes are sequentially passed through units of sorting, grinding, drying, accumulating, and sending to a pyrolysis reactor for pyrolytic treatment. The syngas produced in the pyrolysis is passed through dry cleaning, dust catching, a first wet cleaning with water, a second wet cleaning with alkali, and a floatation unit for separation of water which is purified to an extent sufficient for technical use. The purified syngas is also passed through an absorber and is then used as a working medium for a power generation unit such as a gas turbine co-generator that generates electricity. Solid products of the pyrolysis reaction, such as coke, are returned to the reactor for afterburning, and the heat of the reaction can be utilized in a dryer, or the like.

Abstract translation: 提出了无废热解热处理和完全利用城市和家庭废物的系统和方法。 废物依次通过分选，研磨，干燥，积聚和送到热解反应器进行热解处理。 在热解中产生的合成气通过干洗，吸尘，用水进行第一次湿式清洗，第二次用碱洗涤，以及用于分离水的漂浮单元，其被纯化至足以用于技术用途的程度。 纯化的合成气也通过吸收器，然后用作发电单元（例如发电的燃气轮机共发电机）的工作介质。 将热解反应的固体产物（如焦炭）返回反应器进行后燃，反应热可用于干燥器等中。

公开(公告)号：US20100288173A1

公开(公告)日：2010-11-18

申请号：US12782558

申请日：2010-05-18

Applicant: Ron Broglio ,  Hanwei Zhang ,  Robert Lees Barker ,  Stephen Paul Goff

Inventor： Ron Broglio ,  Hanwei Zhang ,  Robert Lees Barker ,  Stephen Paul Goff

IPC: F23G5/027 ,  F23G5/14

CPC classification number: F23G5/027 ,  F23C9/00 ,  F23G5/04 ,  F23G5/16 ,  F23G5/50 ,  F23G2201/10 ,  F23G2201/303 ,  F23G2202/106 ,  F23G2205/00 ,  F23G2206/10 ,  F23G2207/104 ,  F23G2207/20 ,  F23N3/00 ,  F23N5/02

Abstract: A two stage refuse gasification combustion system for processing refuse is disclosed. The system may contain features such as an advancer, a first and second gasifier, a drier, a gas regulator, and a post combustor. Additionally, methods for regulating gas and advancing refuse through a two stage refuse gasification combustion system are disclosed.

Abstract translation: 公开了一种用于加工垃圾的两级垃圾气化燃烧系统。 该系统可以包含诸如推进器，第一和第二气化器，干燥器，气体调节器和后燃烧器的特征。 此外，公开了通过两级垃圾气化燃烧系统调节气体和推进垃圾的方法。

公开(公告)号：US07819070B2

公开(公告)日：2010-10-26

申请号：US11160940

申请日：2005-07-15

Applicant: Amirali G Rehmat ,  Richard L Kao ,  Jin Soo Chung

Inventor： Amirali G Rehmat ,  Richard L Kao ,  Jin Soo Chung

IPC: F23G5/12

CPC classification number: C10J3/26 ,  C10J3/723 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/152 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0973 ,  C10K1/024 ,  C10K1/101 ,  F23G5/006 ,  F23G5/008 ,  F23G5/027 ,  F23G7/12 ,  F23G2201/303 ,  F23G2201/40 ,  F23G2209/281 ,  F23J15/006 ,  Y02P20/145

Abstract: The present application discloses an apparatus for gasification of solid, liquid and gaseous organic feed materials having a fuel value into synthesis gas. The apparatus comprises: a gasification reactor vessel having a tapered interior with a minimum of four zones for introducing reaction gas mixtures, a central perforated diffuser pipe, a solid and liquid material inlet at the upper end of the uppermost zone, a solid and gas discharge outlet at the lower end of the bottom zone, wherein the reactor vessel defining a sequence of reaction zones from the material inlet to the material outlet including drying, pyrolysis, combustion and gasification zones, and confining downwardly moving the column of the feed materials within the zones, gas feed inlet pipes for introducing reaction gas into the zones, a synthesis gas discharge pipe below the zones, and a heat exchanger below the zones.

Abstract translation: 本申请公开了一种用于将具有燃料值的固体，液体和气体有机进料气化的气体的装置，用于合成气体。 该装置包括：具有锥形内部的气化反应器容器，其具有至少四个用于引入反应气体混合物的区域，中心穿孔扩散管，在最上部区域的上端处的固体和液体材料入口，固体和气体排放 出口在底部区域的下端，其中反应器容器限定从材料入口到材料出口的一系列反应区，包括干燥，热解，燃烧和气化区，并且限制向下移动进料材料的塔内 区域，用于将反应气体引入到区域中的气体供给入口管，在区域下方的合成气排出管，以及区域下方的热交换器。