公开(公告)号：US20070081930A1

公开(公告)日：2007-04-12

申请号：US11368851

申请日：2006-03-06

Applicant: Harry Menian

Inventor： Harry Menian

IPC: F28D21/00

CPC classification number: C10J3/57 ,  C10B49/14 ,  C10J2300/183 ,  C10K3/001 ,  F23G2201/303

Abstract: A unique waste processing method provides a simple solution to complex mix of waste streams using a molten sodium/potassium bath to thermalize waste. The process offers sterilization, volumetric reduction, energy or oil recovery, and complete molecular fragmentation of hazardous chemicals.

Abstract translation: 独特的废物处理方法提供了使用熔融的钠/钾浴来复杂混合的废物流的混合物以使废物热化的简单解决方案。 该过程提供灭菌，体积减少，能量或油回收，以及危险化学品的完全分子破碎。

公开(公告)号：US20060275718A1

公开(公告)日：2006-12-07

申请号：US10963051

申请日：2004-10-12

Applicant: Kenny Arnold ,  Jianhui Hong ,  Joseph Smith

Inventor： Kenny Arnold ,  Jianhui Hong ,  Joseph Smith

IPC: F23D5/12

CPC classification number: F23G5/24 ,  F23G5/0276 ,  F23G5/50 ,  F23G2201/303 ,  F23G2207/101 ,  F23G2207/103 ,  F23N3/002 ,  F23N5/006 ,  F23N5/102

Abstract: Methods and systems for measuring and controlling the percent stoichiometric oxidant in the pyrolyzing section of incinerators are provided. The methods and systems rely on measurements of the oxygen concentration and temperature of the gases within the pyrolysis section and mathematical relationships between these values and the percent stoichiometric oxidant.

Abstract translation: 提供了用于测量和控制焚烧炉热解部分化学计量氧化剂百分比的方法和系统。 方法和系统依赖于热解段内气体的氧浓度和温度的测量以及这些值与化学计量氧化剂百分比之间的数学关系。

公开(公告)号：US20060137579A1

公开(公告)日：2006-06-29

申请号：US10563434

申请日：2004-07-23

Applicant: Hiroyuki Fujimura ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Kei Matsuoka ,  Tatsuya Hasegawa

Inventor： Hiroyuki Fujimura ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Kei Matsuoka ,  Tatsuya Hasegawa

IPC: F23G5/00 ,  F23B30/00

CPC classification number: F23G5/027 ,  F23C13/08 ,  F23G5/006 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2202/101 ,  F23G2202/104 ,  F23G2203/502 ,  F23G2209/262 ,  F23J15/006 ,  F23J15/06 ,  F23J2217/50 ,  F23L2900/07002 ,  F23L2900/07005 ,  Y02E20/344 ,  Y02E20/363

Abstract: A gasification system has a gasification furnace (1) for gasifying wastes to produce a combustible gas and a combustion furnace (2) for combusting char and/or tar produced by gasification in the gasification furnace (1). The gasification system also has a return line for returning a combustion gas discharged from the combustion furnace (2) to the gasification furnace (1) and the combustion furnace (2).

Abstract translation: 气化系统具有用于气化废物以产生可燃气体的气化炉（1）和用于燃烧气化炉（1）中气化产生的焦炭和/或焦油的燃烧炉（2）。 气化系统还具有用于将从燃烧炉（2）排出的燃烧气体返回到气化炉（1）和燃烧炉（2）的回流管线。

公开(公告)号：US20060107595A1

公开(公告)日：2006-05-25

申请号：US11285145

申请日：2005-11-23

Applicant: Kenneth Davison ,  Neal Stroulger

Inventor： Kenneth Davison ,  Neal Stroulger

IPC: C01B3/32

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。

公开(公告)号：US07029635B2

公开(公告)日：2006-04-18

申请号：US10094969

申请日：2002-03-12

Applicant: Yoshiyuki Kashiwagi ,  Haruhisa Ishigaki ,  Nobuyuki Yoshioka

Inventor： Yoshiyuki Kashiwagi ,  Haruhisa Ishigaki ,  Nobuyuki Yoshioka

IPC: H62D3/00 ,  C01F5/26

CPC classification number: B01D53/508 ,  B01D53/685 ,  C10B1/10 ,  C10B47/44 ,  C10B53/00 ,  C10J3/00 ,  C10J3/005 ,  C10J3/72 ,  C10J2300/0983 ,  C10L9/10 ,  F23G5/02 ,  F23G5/027 ,  F23G5/16 ,  F23G5/20 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/701 ,  F23G2203/211 ,  F23G2204/20

Abstract: A system for treating a treatable material containing a noxious component, which comprises a mixer for mixing a treatment agent containing alkali material with the treatable material to form a mixture, at least one first heat treating furnace for producing a low oxygen concentration atmosphere, a first heating device located outside the first furnace to heat it at a first temperature at which the treatable material is decomposed to generate a substance containing the noxious component, at least one separate second heat treating furnace, and a second heating device located outside the second furnace for heating the treatable material residue at a second temperature at which carbonization of the treatable material residue takes place.

Abstract translation: 一种用于处理含有有害成分的可处理材料的系统，其包括用于将含有碱性材料的处理剂与可处理材料混合以形成混合物的混合器，至少一个用于产生低氧浓度气氛的第一热处理炉，第一 加热装置位于第一炉的外部，以在被处理材料分解的第一温度下加热，以产生含有有害成分的物质，至少一个单独的第二热处理炉和位于第二炉的外部的第二加热装置， 在可处理材料残留物发生碳化的第二温度下加热可处理材料残渣。

公开(公告)号：US06959654B2

公开(公告)日：2005-11-01

申请号：US10331559

申请日：2002-12-31

Applicant: Stan E. Abrams

Inventor： Stan E. Abrams

IPC: F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/44 ,  F23L15/00 ,  F23N1/02 ,  F23N5/00 ,  F23B7/00

CPC classification number: F23G5/0276 ,  F23G5/006 ,  F23G5/16 ,  F23G5/444 ,  F23G2201/303 ,  F23G2203/105 ,  F23G2203/8016 ,  F23G2205/122 ,  F23G2205/18 ,  F23G2206/203 ,  F23G2900/50006 ,  F23J2217/40 ,  F23J2217/50 ,  F23L15/00 ,  F23N1/02 ,  F23N5/003 ,  F23N2023/02 ,  F23N2023/08 ,  F23N2037/16 ,  Y02E20/12 ,  Y02E20/348

Abstract: A solid fuel fed combustor method having a first chamber portion with an inlet feeding a metered amount of a solid fuel to a first burner stage having a first traveling conveyor firebelt. A metered amount of air is introduced in progressively increasing proportions along the length thereof to cause endothermic reduction of the solid fuel. The first stage feeds a second burner stage having a second traveling conveyor firebelt. Air is introduced in a progressively decreasing amount along the length of the second traveling conveyor firebelt to induce exothermic combustion and decomposition of fuel. The amount of air introduced and speed of the conveyors are controlled to minimize the quantity of carbon monoxide and nitrogen oxides and other pollutants. Radiative energy generated from fuel traveling on the traveling conveyor firebelts is reflected on fuel traveling on the first firebelt.

Abstract translation: 一种固体燃料供给燃烧器方法，其具有第一室部分，其具有将计量的固体燃料供给到具有第一行进输送机防火带的第一燃烧器台的入口。 沿着其长度逐渐增加的比例引入计量的空气以引起固体燃料的吸热还原。 第一阶段进料具有第二行进输送机防火带的第二燃烧器台。 沿着第二行进输送机火带的长度逐渐减少空气，引起燃料的放热燃烧和分解。 引入的空气量和输送机的速度被控制以使一氧化碳和氮氧化物和其他污染物的量最小化。 在旅行输送机防火带上行驶的燃料产生的辐射能量反映在第一个防火带上行驶的燃料上。

公开(公告)号：US20050144844A1

公开(公告)日：2005-07-07

申请号：US11073688

申请日：2005-03-08

Applicant: Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

Inventor： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

IPC: C10J3/54 ,  C10J3/56 ,  C10B1/00

CPC classification number: C10J3/482 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/095 ,  C10J2300/0956 ,  C10J2300/0996 ,  C10J2300/1215 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1876 ,  C10J2300/1892 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2202/30 ,  F23G2203/502 ,  F23G2206/202 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

Abstract: The present invention provides a fuel gasification furnace including a gasification chamber (1) for fluidizing a high-temperature fluidizing medium therein to form a gasification chamber fluidized bed having an interface, and for gasifying a fuel in the gasification chamber fluidized bed, a char combustion chamber (2) for fluidizing a high-temperature fluidizing medium therein to form a char combustion chamber fluidized bed having an interface, and for combusting char generated by gasification in the gasification chamber (1) in the char combustion chamber fluidized bed to heat the fluidizing medium, and a first energy recovery device (109) for using gases generated by the gasification chamber (1) as a fuel. The gasification chamber (1) and the char combustion chamber (2) are integrated with each other. The gasification chamber (1) and the char combustion chamber (2) are divided from each other by a first partition wall (15) for preventing gases from flowing therebetween, and which extends vertically upward from the interfaces of the respective fluidized beds. The first partition wall (15) has a first opening (25) provided in a lower portion thereof, and the first opening (25) serves as a communication between the gasification chamber (1) and the char combustion chamber (2), for allowing the fluidizing medium heated in the char combustion chamber (2) to move from the char combustion chamber (2) via the first opening (25) into the gasification chamber (1).

Abstract translation: 本发明提供了一种燃料气化炉，其包括用于使其中的高温流化介质流化的气化室（1），以形成具有界面的气化室流化床，并且用于气化气化室流化床中的燃料，焦炭燃烧 用于使其中的高温流化介质流化以形成具有界面的焦炭燃烧室流化床的腔室（2），并且用于在焦炭燃烧室流化床中的气化室（1）中燃烧由气化产生的焦炭，以加热流化 介质和用于使用由气化室（1）产生的气体作为燃料的第一能量回收装置（109）。 气化室（1）和焦炭燃烧室（2）彼此一体化。 气化室（1）和焦炭燃烧室（2）通过第一分隔壁（15）彼此分开，用于防止气体在其间流动，并且从各流化床的界面垂直向上延伸。 第一分隔壁（15）具有设置在其下部的第一开口（25），第一开口（25）用作气化室（1）和焦炭燃烧室（2）之间的连通，以允许 在焦炭燃烧室（2）中加热的流化介质经由第一开口（25）从焦炭燃烧室（2）移动到气化室（1）中。

公开(公告)号：US20050039638A1

公开(公告)日：2005-02-24

申请号：US10203245

申请日：2001-02-05

Applicant: Ching Chiu Leung ,  Khine Aung ,  Waiman Cheung

Inventor： Ching Chiu Leung ,  Khine Aung ,  Waiman Cheung

IPC: C04B7/43 ,  C04B7/44 ,  F23G5/00 ,  F23G5/16 ,  F23G5/20 ,  F23G5/46 ,  C04B2/10 ,  C04B7/45 ,  C04B11/036

CPC classification number: C04B7/4407 ,  C04B7/43 ,  C04B2290/20 ,  F23G5/006 ,  F23G5/16 ,  F23G5/20 ,  F23G5/46 ,  F23G2201/303 ,  F23G2202/103 ,  F23G2203/20 ,  F23G2206/201 ,  F23G2900/50001 ,  F23J2219/60 ,  Y02E20/12 ,  Y02E20/363 ,  Y02P40/123

Abstract: The co-combustion process may comprise the following unit operations: routing of hot gas (10) generated in the clinker cooling process to a rotary kiln (1); use of part of the rotary kiln exhaust gas to dry solid wastes in rotary dryers; leading the gases from both the dryer and the combustion kiln to the secondary combustion chamber (2); use of additional fuel to boost up the secondary combustion chamber reaction temperature to as high as 1200° C.; primary dry gas scrubbing in a precalciner or precalciners (3, 3a); heat recovery (4) and power generation; secondary gas scrubbing (5) in a semi-dry scrubber, bag filtering after activated carbon injection and returning of all the collected ash and used carbon into the waste kiln and/or a cement kiln. Detrimental materials for cement processing generated by waste combustion can be by-passed to a scrubbing system and a cement kiln. Residue slag from waste kilns can be treated and reused.

Abstract translation: 共燃过程可以包括以下单元操作：将在熟料冷却过程中产生的热气（10）路由到回转窑（1）; 使用部分回转窑废气将旋转干燥器中的固体废物干燥; 将来自干燥器和燃烧窑的气体引导到二次燃烧室（2）; 使用额外的燃料将二次燃烧室反应温度升高到高达1200℃; 在预分解器或预煅烧器（3,3a）中进行初级干燥气体洗涤; 热回收（4）和发电; 半干洗涤器中的二次气体洗涤（5），活性炭注入后的袋过滤，并将所有收集的灰分和使用的碳返回到废窑和/或水泥窑中。 通过废物燃烧产生的水泥加工的有害材料可以被旁路到洗涤系统和水泥窑。 来自废窑的残渣可以被处理和再利用。

公开(公告)号：US06746497B1

公开(公告)日：2004-06-08

申请号：US09784448

申请日：2001-02-27

Applicant: Masamoto Kaneko

Inventor： Masamoto Kaneko

IPC: C10J300

CPC classification number: F23G5/0276 ,  F23G5/165 ,  F23G5/50 ,  F23G2201/101 ,  F23G2201/303 ,  F23G2202/101 ,  F23G2207/101 ,  F23G2207/30 ,  F23G2209/281

Abstract: A waste is dry-distilled in a gasification furnace and generated combustible gas is combusted in a combustion furnace. A temperature in the combustion furnace is set to be substantially constant at a first preset temperature or more. When the temperature in the combustion furnace is greater than the first preset temperature by combustion of other fuels, the combustible gas is introduced. When the temperature in the combustion furnace reaches a second preset temperature or more by the combustion of only the combustible gas, the combustion of the other fuels is finished. When the temperature in the combustion furnace falls below a third preset temperature the combustion of the other fuels is resumed. When the temperature in the gasification furnace falls below a fourth preset temperature, the combustion of the other fuels is finished.

Abstract translation: 在气化炉中将废物进行干馏，并在燃烧炉中产生可燃气体。 在第一预设温度或更高温度下将燃烧炉中的温度设定为基本恒定。 当燃烧炉中的温度通过其他燃料的燃烧而大于第一预设温度时，引入可燃气体。 当燃烧炉中的温度仅通过可燃气体的燃烧而达到第二预定温度以上时，其他燃料的燃烧结束。 当燃烧炉中的温度低于第三预设温度时，其它燃料的燃烧恢复。 当气化炉中的温度低于第四预设温度时，其他燃料的燃烧结束。

公开(公告)号：US06709602B2

公开(公告)日：2004-03-23

申请号：US09841058

申请日：2001-04-23

Applicant: Michael H. Spritzer ,  William S. Rickman ,  Niles W. Johanson ,  Glenn T. Hong

Inventor： Michael H. Spritzer ,  William S. Rickman ,  Niles W. Johanson ,  Glenn T. Hong

IPC: C02F120

CPC classification number: F23J7/00 ,  B09B3/00 ,  B09B3/0091 ,  C02F1/02 ,  C02F1/20 ,  C02F1/72 ,  C02F1/722 ,  C02F1/727 ,  C02F1/74 ,  C02F11/004 ,  C02F11/086 ,  C02F2103/20 ,  F23G5/027 ,  F23G5/16 ,  F23G5/50 ,  F23G2201/303 ,  F23G2202/30 ,  F23G2203/8013 ,  F23G2207/20 ,  F23J2219/80 ,  F23J2900/15061 ,  F23L2900/07009

Abstract: A system and method for treating feedstocks containing solids, sludges or slurries that contain organics includes introducing the feedstock into a desorption chamber. In the desorption chamber, the temperature and pressure of the feedstock are elevated to volatilize a portion of the feedstock and thereby separate the feedstock into a volatile portion containing organics and a residue portion. Steam, water or oxidants can be injected into the desorption chamber to aid in the volatilization process. From the desorption chamber, the volatile portion of the feedstock is transferred to a reactor for hydrothermal treatment to oxidize or reform the organics in the volatile portion. In the hydrothermal reactor, the volatile portion may be reacted with excess oxidant and auxiliary fuel at a temperature between approximately 1000° F. and approximately 1800° F. and a pressure of between approximately 20 atmospheres and approximately 200 atmospheres.

Abstract translation: 用于处理含有固体，含有有机物的淤泥或浆料的原料的系统和方法包括将原料引入解吸室。 在解吸室中，原料的温度和压力升高以挥发一部分原料，从而将原料分离成含有机物和残余物部分的挥发性部分。 可以将蒸汽，水或氧化剂注入解吸室以帮助挥发过程。 从解吸室中将原料的挥发性部分转移到用于水热处理的反应器中以氧化或改造挥发性部分中的有机物。 在水热反应器中，挥发性部分可以在约1000°F至约1800°F之间的温度和约20大气压和约200大气压之间的温度下与过量的氧化剂和辅助燃料反应。