公开(公告)号：US20150166911A1

公开(公告)日：2015-06-18

申请号：US14105832

申请日：2013-12-13

Applicant: Frank Reed

Inventor： Frank Reed

IPC: C10J3/82

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.

Abstract translation: 公开了用于废料进料的热解的系统和方法。 一些系统包括主蒸馏器和次蒸馏器。 合成气通过主蒸馏器中的热解产生，然后与燃烧空气混合并点燃，在某些情况下产生能量。 碳炭运送到二级蒸馏器，并通过气闸从系统中排出。

公开(公告)号：US20120227645A1

公开(公告)日：2012-09-13

申请号：US13496638

申请日：2010-09-20

Applicant: Howard Morgan Clarke ,  Peter Bartl ,  Christopher John House

Inventor： Howard Morgan Clarke ,  Peter Bartl ,  Christopher John House

IPC: F23G5/027 ,  F23G7/00 ,  F23G5/08

CPC classification number: F23G5/027 ,  C10B49/02 ,  C10B53/00 ,  C10J3/02 ,  C10J2300/0946 ,  C10J2300/1276 ,  C10J2300/1606 ,  C10J2300/1869 ,  F23G2201/301 ,  F23G2202/60 ,  F23G2203/207

Abstract: Waste is treated by pyrolysis at a temperature of from 400-700° C. and combustion at a temperature of at least 400° C. Off-gases are catalytically oxidized to reduce emissions. The combusting waste is periodically agitated with high-pressure air bursts to disrupt waste in the chamber and promote even and complete combustion. Air is introduced during pyrolysis to promote controlled flow of off-gas to the catalyst and air and/or water is used to dislodge accumulated ash at the end of the treatment process.

Abstract translation: 废物通过在400-700℃的温度下进行热解处理，并在至少400℃的温度下进行燃烧。废气被催化氧化以减少排放。 燃烧废物周期性地受到高压空气爆炸的搅动，以破坏室内的废物，促进均匀和完全的燃烧。 在热解过程中引入空气以促进尾气的控制流向催化剂，并且在处理过程结束时使用空气和/或水来排出积累的灰分。

公开(公告)号：US20120024204A1

公开(公告)日：2012-02-02

申请号：US12844117

申请日：2010-07-27

Applicant: Peter Rugg ,  Robert J. von Gutfeld ,  Ann Engelkemeir

Inventor： Peter Rugg ,  Robert J. von Gutfeld ,  Ann Engelkemeir

IPC: F23J15/00

CPC classification number: F23G5/027 ,  C10B47/30 ,  C10B53/02 ,  C10B53/04 ,  C10K1/04 ,  F23G5/20 ,  F23G2201/301 ,  F23G2201/40 ,  F23G2900/50205 ,  Y02E50/14

Abstract: A system and method for collecting hot coal tar gases emanating from a coal containing pyrolytic kiln are described. The hot coal tar gases, comprising a variety of different hydrocarbons as well as inorganic gases arising from the kiln thermal processing are transferred by diffusion and forced convection to a thermal duct in which the temperature is controlled to be maintained at a temperature below that of the kiln. The gaseous hydrocarbon with the highest condensation temperature is the first to liquefy. Additional useful hydrocarbons liquefy as the temperature of the gas continues to cool from the kiln temperature of ˜5000 C to one approaching the minimum duct temperature, ˜175° C. After a number of desirable hydrocarbons present in the coal tar gas have liquefied, the liquid contents are collected, either separately or as a combination of liquid hydrocarbons. The several remaining inorganic and some hydrocarbons gases with condensation temperatures below the minimum duct temperature are separately collected in gaseous form for further processing and/or safe disposal.

Abstract translation: 描述了从含煤热解窑排出的热煤焦油气体收集系统和方法。 包含各种不同的碳氢化合物以及由窑热处理产生的无机气体的热煤焦油气体通过扩散和强制对流传递到热管道，其中控制温度保持在低于 窑。 具有最高冷凝温度的气态烃首先液化。 当气体的温度从〜5000℃的窑温继续冷却到接近最小管道温度〜175℃时，另外有用的烃液化。在煤焦油气体中存在许多所需的烃已经液化后， 收集液体内容物，分别或作为液体烃的组合。 冷凝温度低于最低管道温度的几种剩余的无机物和一些碳氢化合物气体分别以气态形式收集，用于进一步处理和/或安全处置。

公开(公告)号：US20110290637A1

公开(公告)日：2011-12-01

申请号：US12790531

申请日：2010-05-28

Applicant: Aditya Kumar ,  Matthew Christian Nielsen ,  Ruijie Shi

Inventor： Aditya Kumar ,  Matthew Christian Nielsen ,  Ruijie Shi

IPC: B01J19/08 ,  H05F3/06

CPC classification number: C10J3/18 ,  C10J3/723 ,  C10J3/84 ,  C10J2200/12 ,  C10J2200/152 ,  C10J2300/0946 ,  C10J2300/1238 ,  C10J2300/1634 ,  C10J2300/169 ,  C10J2300/1884 ,  C10K1/026 ,  C10K1/101 ,  F23G2201/301 ,  F23G2201/40 ,  F23G2204/201 ,  Y02E20/16

Abstract: A plasma-assisted waste gasification system including a sensing mechanism and process for converting waste stream reaction residues into a clean synthesis gas (syngas) is disclosed. The gasification system includes a first sensor located between a gas quench unit and a heat recovery unit to measure a first temperature and first flow rate of the synthesis gas exiting the gas quench unit; a second sensor to measure a second temperature and a second flow rate of a low temperature synthesis gas entering the gas quench unit; wherein the first sensor and the second sensor are connected to an inferential sensing mechanism. The inferential sensing mechanism is capable of estimating the temperature of the synthesis gas in the reactor, based on the measured first temperature and first flow rate, and the measured second temperature and second flow rate, using a mass-energy balance relationship that is based on the measurements of the two sensors. Another aspect of the invention relates to a control unit to control the temperature of the reactor to a required operating temperature range.

Abstract translation: 公开了一种等离子体辅助废气处理系统，其包括感测机构和将废物流反应残余物转化为清洁合成气（合成气）的方法。 气化系统包括位于气体骤冷单元和热回收单元之间的第一传感器，用于测量离开气体骤冷单元的合成气的第一温度和第一流量; 用于测量进入气体骤冷单元的低温合成气的第二温度和第二流量的第二传感器; 其中所述第一传感器和所述第二传感器连接到推定感测机构。 基于所测量的第一温度和第一流量以及测量的第二温度和第二流量，使用基于以下的质量 - 能量平衡关系，推测感测机构能够估计反应器中的合成气的温度 两个传感器的测量。 本发明的另一方面涉及一种将反应器的温度控制在所需工作温度范围内的控制单元。

公开(公告)号：US08047144B2

公开(公告)日：2011-11-01

申请号：US12207153

申请日：2008-09-09

Applicant: John P. Whitney ,  Carl Wikstrom

Inventor： John P. Whitney ,  Carl Wikstrom

IPC: F23J15/04 ,  F23G5/12 ,  F23B99/00

CPC classification number: F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G2201/301 ,  F23G2201/302

Abstract: A multi-step process is provided in which waste material is processed in two or more steps. Specifically, an earlier step of the process heats the waste material at a first temperature. This results in a release of vapors for materials having a boiling point that is lower than the first temperature. A subsequent step of the process heats some or all of the remaining waste material at a second temperature, which is preferably higher than the first temperature. The subsequent heating results in a release of additional vapors for those materials having a boiling point that is lower than the second temperature. A system configured to carry out the process is also disclosed.

Abstract translation: 提供了一种多步骤处理方法，其中以两个或多个步骤处理废料。 具体地，该方法的较早步骤在第一温度下加热废料。 这导致沸点低于第一温度的材料的蒸气释放。 该方法的后续步骤在优选高于第一温度的第二温度下加热部分或全部剩余的废料。 随后的加热导致沸点低于第二温度的那些材料的附加蒸气的释放。 还公开了一种被配置为执行该过程的系统。

公开(公告)号：US20110247534A1

公开(公告)日：2011-10-13

申请号：US12756426

申请日：2010-04-08

Applicant: LI-FENG CHENG

Inventor： LI-FENG CHENG

IPC: F23G5/44

CPC classification number: C10B53/07 ,  C10B47/24 ,  C10B49/10 ,  C10G1/10 ,  C10G2300/1003 ,  C10G2300/1007 ,  F23G5/006 ,  F23G5/02 ,  F23G5/442 ,  F23G2201/301 ,  F23G2201/302 ,  F23G2201/80 ,  F23G2205/20 ,  F23G2209/102 ,  F23G2209/28 ,  F23G2900/50205 ,  Y02P20/143

Abstract: A waste recycling apparatus includes a temporary storage tank, a pyrolyzing furnace, a first blower, a material storage tank, a second blower, and a rotary valve and a magnetic device. The temporary storage tank carries a waste. The pyrolyzing furnace decomposes the waste into a non-iron material and an iron material. The first blower produces winds to blow the waste into the pyrolyzing furnace. The material storage tank stores the non-iron material and the iron material and includes an outlet. The second blower produces winds to blow the non-iron material and the iron material into the material storage tank. The rotary valve controls a discharge quantity of the non-iron material and the iron material. The magnetic device is installed on a side of the outlet, and the magnetic device attracts the iron material to separate the non-iron material and the iron material. The waste recycling apparatus can recycle wastes automatically.

Abstract translation: 废弃物回收设备包括临时储罐，热解炉，第一鼓风机，材料储罐，第二鼓风机，旋转阀和磁性装置。 临时储罐带有废物。 热解炉将废物分解成非铁材料和铁材料。 第一鼓风机产生风，将废物吹入热解炉。 材料储存罐存储非铁材料和铁材料并且包括出口。 第二鼓风机产生风，将非铁材料和铁材料吹入料仓。 旋转阀控制非铁材料和铁材料的排出量。 磁性装置安装在出口的一侧，磁性装置吸引铁材料以分离非铁材料和铁材料。 废物回收设备可以自动回收废物。

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：US20100300112A1

公开(公告)日：2010-12-02

申请号：US12599583

申请日：2008-04-28

Applicant: Frank Hannemann ,  Martin Pfund ,  Manfred Schingnitz

Inventor： Frank Hannemann ,  Martin Pfund ,  Manfred Schingnitz

IPC: F02C3/20 ,  F02C3/28 ,  F01K3/20 ,  F01K17/00

CPC classification number: F02C3/34 ,  F01K17/025 ,  F01K17/06 ,  F01K23/068 ,  F01K23/10 ,  F02C3/28 ,  F02C3/305 ,  F02C6/18 ,  F05D2220/75 ,  F23C9/00 ,  F23G5/027 ,  F23G5/46 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/40 ,  F23G2206/203 ,  F23L7/007 ,  F23L2900/07001 ,  Y02E20/12 ,  Y02E20/18 ,  Y02E20/322 ,  Y02E20/326 ,  Y02E20/344 ,  Y02E50/11 ,  Y02E50/12

Abstract: A method for producing electric energy from solid and liquid fuels is provided. The fuels are first subjected to a gasification process at high pressure, and the scrubbed gasification gas is fed to a gas and steam turbine process. The combustion of the scrubbed gasification gas in the gas turbine chamber does not occur with air, but with a mixture made of the three components oxygen, carbon dioxide and water vapor. As a result, the waste gas of the gas turbine is made only of carbon dioxide and water vapor. After the condensation thereof, technically pure carbon dioxide remains, which can be dissipated by storage in the deep substrate of the atmosphere.

Abstract translation: 提供了一种从固体和液体燃料生产电能的方法。 燃料首先在高压下进行气化过程，并将经过洗涤的气化气体进料到气体和汽轮机过程。 燃气轮机室中的洗涤气化气体的燃烧不会与空气一起发生，而是由氧，二氧化碳和水蒸汽三种组分组成的混合物。 结果，燃气轮机的废气仅由二氧化碳和水蒸气构成。 在其冷凝后，保留技术上纯的二氧化碳，其可通过储存在大气深层底物中而消散。

公开(公告)号：US20090000531A1

公开(公告)日：2009-01-01

申请号：US12207153

申请日：2008-09-09

Applicant: John P. WHITNEY ,  Carl Wikstrom

Inventor： John P. WHITNEY ,  Carl Wikstrom

IPC: F23G5/08 ,  F23B30/00

CPC classification number: F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G2201/301 ,  F23G2201/302

Abstract: A multi-step process is provided in which waste material is processed in two or more steps. Specifically, an earlier step of the process heats the waste material at a first temperature. This results in a release of vapors for materials having a boiling point that is lower than the first temperature. A subsequent step of the process heats some or all of the remaining waste material at a second temperature, which is preferably higher than the first temperature. The subsequent heating results in a release of additional vapors for those materials having a boiling point that is lower than the second temperature. A system configured to carry out the process is also disclosed.

Abstract translation: 提供了一种多步骤处理方法，其中以两个或多个步骤处理废料。 具体地，该方法的较早步骤在第一温度下加热废料。 这导致沸点低于第一温度的材料的蒸气释放。 该方法的后续步骤在优选高于第一温度的第二温度下加热部分或全部剩余的废料。 随后的加热导致沸点低于第二温度的那些材料的附加蒸气的释放。 还公开了一种被配置为执行该过程的系统。

公开(公告)号：US20080244976A1

公开(公告)日：2008-10-09

申请号：US12091038

申请日：2006-10-23

Applicant: Mark A. Paisley

Inventor： Mark A. Paisley

IPC: C01B3/44 ,  C01B3/36

CPC classification number: C07C4/04 ,  C10J3/482 ,  C10J3/84 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/0983 ,  C10J2300/1606 ,  C10J2300/1637 ,  C10J2300/165 ,  C10K3/008 ,  C10K3/04 ,  F23G2201/301 ,  F23G2201/304 ,  F23G2201/40 ,  Y02E20/16 ,  Y02P20/145

Abstract: The present invention relates to a process and system for gasifying biomass or other carbonaceous feedstocks in an indirectly heated gasifier and provides a method for the elimination of condensable organic materials (tars) from the resulting product gas with an integrated tar removal step. More specifically, this tar removal step utilizes the circulating heat carrier to crack the organics and produce additional product gas. As a benefit of the above process, and because the heat carrier circulates through alternating steam and oxidizing zones in the process, deactivation of the cracking reactions is eliminated.

Abstract translation: 本发明涉及用于在间接加热的气化器中气化生物质或其它含碳原料的方法和系统，并且提供了一种通过一体式焦油去除步骤从所得产物气体中消除可冷凝有机材料（焦油）的方法。 更具体地，该焦油去除步骤利用循环热载体来裂开有机物并产生另外的产物气体。 作为上述方法的益处，并且由于热载体在该过程中通过交替的蒸汽和氧化区循环，消除了裂化反应的失活。