公开(公告)号：US07302897B2

公开(公告)日：2007-12-04

申请号：US10862498

申请日：2004-06-07

Applicant: Richard B. Pallett ,  Warren Hyland

Inventor： Richard B. Pallett ,  Warren Hyland

IPC: F23B7/00

CPC classification number: F23G5/46 ,  B09B3/00 ,  F23G5/006 ,  F23G5/02 ,  F23G5/033 ,  F23G5/04 ,  F23G2201/10 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2201/80 ,  F23G2206/10 ,  F23G2206/203 ,  F23G2900/50214 ,  Y02E20/12

Abstract: A system for disposing of municipal solid waste provides commercially-available equipment that is modified to initially remove identifiable unwanted components from the waste, and then chop the waste into small pieces of a size suitable for handling, separation and combustion. The moisture content of the waste is reduced in a closed system by passing dry air through the waste in a confined space to absorb moisture and produce moist air, which is then dehumidified via refrigeration equipment. The dehumidified air is recycled through the waste repeatedly through the closed system until the water content has reached the predetermined amount. The waste is stored in a bunker for later use or is immediately combusted in a two-step process by first gasifying the dried waste to produce combustible syngas and then immediately or later combusting the gas in a gas turbine or other engine to produce electricity that is partly used to power the process and partly sold commercially.

Abstract translation: 用于处理城市固体废物的系统提供商业上可用的设备，其被修改以便最初从废物中除去可识别的不需要的组分，然后将废物切碎成适合于处理，分离和燃烧的尺寸的小块。 通过将干燥空气通过密闭空间中的废物吸收水分并产生潮湿的空气，然后通过制冷设备将其除湿，从而在封闭系统中减少废物的含水量。 除湿空气通过封闭系统反复循环使用，直到含水量达到预定的量。 废物被储存在沙坑中供以后使用，或者通过首先将干燥的废物气化以产生可燃合成气，然后立即或稍后在燃气轮机或其它发动机中燃烧气体以产生电 部分用于为过程提供动力，部分用于商业销售。

公开(公告)号：US20040221778A1

公开(公告)日：2004-11-11

申请号：US10862498

申请日：2004-06-07

Inventor： Richard B. Pallett ,  Warren Hyland

IPC: F23B007/00

CPC classification number: F23G5/46 ,  B09B3/00 ,  F23G5/006 ,  F23G5/02 ,  F23G5/033 ,  F23G5/04 ,  F23G2201/10 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2201/80 ,  F23G2206/10 ,  F23G2206/203 ,  F23G2900/50214 ,  Y02E20/12

Abstract: A system for disposing of municipal solid waste provides commercially-available equipment that is modified to initially remove identifiable unwanted components from the waste, and then chop the waste into small pieces of a size suitable for handling, separation and combustion. The moisture content of the waste is reduced in a closed system by passing dry air through the waste in a confined space to absorb moisture and produce moist air, which is then dehumidified via refrigeration equipment. The dehumidified air is recycled through the waste repeatedly through the closed system until the water content has reached the predetermined amount. The waste is stored in a bunker for later use or is immediately combusted in a two-step process by first gasifying the dried waste to produce combustible syngas and then immediately or later combusting the gas in a gas turbine or other engine to produce electricity that is partly used to power the process and partly sold commercially.

Abstract translation: 用于处理城市固体废物的系统提供商业上可用的设备，其被修改以便最初从废物中除去可识别的不需要的组分，然后将废物切碎成适合于处理，分离和燃烧的尺寸的小块。 通过将干燥空气通过密闭空间中的废物吸收水分并产生潮湿的空气，然后通过制冷设备将其除湿，从而在封闭系统中减少废物的含水量。 除湿空气通过封闭系统反复循环使用，直到含水量达到预定的量。 废物被储存在沙坑中供以后使用，或者通过首先将干燥的废物气化以产生可燃合成气，然后立即或稍后在燃气轮机或其它发动机中燃烧气体以产生电 部分用于为过程提供动力，部分用于商业销售。

公开(公告)号：US20040111958A1

公开(公告)日：2004-06-17

申请号：US10320069

申请日：2002-12-16

Inventor： David Bridson Oates ,  Alan Van Sloten ,  Jeffrey Fair ,  Trent Renfro ,  Craig Plunk

IPC: C10L005/00

CPC classification number: C10L5/361 ,  C10L5/00 ,  C10L5/04 ,  C10L5/34 ,  F23G5/02 ,  F23G2201/602 ,  Y02E20/12

Abstract: Coal ash, which also consists of fly ash, is a very fine granular solid residue obtained as a by-product of coal combustion. The invention relates to the surprising result that a fuel can be obtained from coal ash. The process involves a pneumatic separation of the coal ash at relatively low temperatures. The coal ash is separated into at least two size fractions. The size fractions obtained by the process of this invention include at least one with lower carbon and another containing increased levels of carbon in the range of 50% by weight and a heating value in the range of 4000 to 6000 Btu/lb.

Abstract translation: 煤灰也由飞灰组成，是作为煤燃烧副产物获得的非常细的颗粒状固体残渣。 本发明涉及可以从煤灰获得燃料的令人惊奇的结果。 该过程涉及在较低温度下煤灰的气动分离。 煤灰被分成至少两个尺寸的分数。 通过本发明方法获得的尺寸级分包括至少一种具有低碳，另一种含有在50重量％范围内的增加的碳含量和4000-6000Btu / lb范围内的加热值。

公开(公告)号：US06748882B2

公开(公告)日：2004-06-15

申请号：US10400722

申请日：2003-03-27

Applicant: Johannes Martin ,  Oliver Gohlke ,  Joachim Horn ,  Michael Busch

Inventor： Johannes Martin ,  Oliver Gohlke ,  Joachim Horn ,  Michael Busch

IPC: F23G700

CPC classification number: F23G5/50 ,  F23G5/006 ,  F23G2201/602 ,  F23G2202/20 ,  F23G2207/30 ,  F23G2209/30 ,  F23G2900/50206

Abstract: In a process for influencing the properties of incineration residues from an incineration plant, in particular a waste incineration plant, the incineration is controlled sot that a sintering and/or fusing of the slag takes place as earl as in the incineration bed of the main incineration zone, and as yet unsintered or unfused incineration residues are separated off at the end of the incineration operation and fed back to the incineration operation.

Abstract translation: 在影响焚化厂，特别是废物焚烧厂的焚烧残渣性质的过程中，焚烧被控制为：炉渣的烧结和/或熔化发生在主要焚化炉的焚烧床中 并且在焚烧操作结束时分离出尚未烧结或未熔化的焚烧残渣，并将其反馈回焚烧操作。

公开(公告)号：US06745706B2

公开(公告)日：2004-06-08

申请号：US10279248

申请日：2002-10-24

Applicant: Richard B. Pallett

Inventor： Richard B. Pallett

IPC: F23B700

CPC classification number: F23G5/46 ,  B09B3/00 ,  F23G5/006 ,  F23G5/02 ,  F23G5/033 ,  F23G5/04 ,  F23G2201/10 ,  F23G2201/601 ,  F23G2201/602 ,  F23G2201/80 ,  F23G2206/10 ,  F23G2206/203 ,  F23G2900/50214 ,  Y02E20/12 ,  Y02E50/30

Abstract: A system for disposing of municipal solid waste 10) provides commercially-available equipment that is modified to initially remove identifiable unwanted components from the waste (12), and then chop the waste into small pieces (16) of a size suitable for handling and combustion. The moisture content of the waste is reduced in a closed system (20) by passing dry air through the waste in a confined space (30) to absorb moisture and produce moist air, which is then dehumidified via refrigeration equipment (34). The dehumidified air is recycled (30, 40) through the waste repeatedly through the closed system (20) until the water content has reached the predetermined amount. The waste is stored in a bunker (41) for later burning, or is immediately burned in a furnace (24) to produce heat that is used to produce steam (50), which drives a generator (26) to produce electricity (52) that is partly used to power the process and partly sold commercially.

Abstract translation: 用于处理城市固体废物的系统10）提供商业上可用的设备，其被修改为从废物（12）中最初去除可识别的不需要的组分，然后将废物切碎成适合于处理和燃烧的尺寸的小块（16） 。 通过使干燥空气通过密闭空间（30）中的废物吸收水分并产生潮湿空气，然后通过制冷设备（34）对其进行除湿，从而在封闭系统（20）中减少废物的含水量。 除湿空气通过废物通过封闭系统（20）重复循环（30,40）直到含水量达到预定量。 废物被储存在沙坑（41）中以供稍后燃烧，或者立即在炉（24）中燃烧以产生用于产生蒸汽（50）的热量，该蒸汽驱动发电机（26）产生电力（52） 这部分用于为过程提供动力，并部分用于商业销售。

公开(公告)号：US20030183138A1

公开(公告)日：2003-10-02

申请号：US10400722

申请日：2003-03-27

Applicant: Martin GmbH fur Umwelt-und Energietechnik ,  Mitsubishi Heavy Industries, Ltd.

Inventor： Johannes Martin ,  Oliver Gohlke ,  Joachim Horn ,  Michael Busch

IPC: F23G007/00 ,  F23G005/00

CPC classification number: F23G5/50 ,  F23G5/006 ,  F23G2201/602 ,  F23G2202/20 ,  F23G2207/30 ,  F23G2209/30 ,  F23G2900/50206

Abstract: The process for influencing the properties of incineration residues from an incineration plant, in particular a waste incineration plant, essentially consists in controlling the incineration in such a way that a sintering and/or fusing of the slag takes place as early as in the incineration bed of the main incineration zone, and that as yet unsintered or unfused incineration residues are separated off at the end of the incineration operation and fed back to the incineration operation.

Abstract translation: 影响来自焚化装置，特别是废物焚化装置的焚烧残渣性质的方法基本上在于控制焚烧，使得炉渣的烧结和/或熔化早在焚化床中发生 的主要焚烧区，并且在焚烧操作结束时分离出尚未烧结或未熔化的焚化残渣，并将其反馈回焚烧操作。

公开(公告)号：US5445088A

公开(公告)日：1995-08-29

申请号：US75721

申请日：1993-05-21

Applicant: William K. Daugherty ,  Bernard A. Parkin, Jr. ,  Franklin D. Ling

Inventor： William K. Daugherty ,  Bernard A. Parkin, Jr. ,  Franklin D. Ling

IPC: F23G5/00 ,  F23J15/00

CPC classification number: F23J15/006 ,  F23G5/006 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/20 ,  F23G2204/103 ,  F23G2206/00 ,  F23L2900/07005 ,  Y02E20/344

Abstract: This abstract describes a process for the complete oxidation of municipal refuse and certain hazardous materials. The facility to accommodate the process consists of a completely enclosed, rotating, cylindrical kiln wherein solids, liquids, and gaseous compounds are simultaneously oxidized. To supplement the burning process, natural gas will be injected into the kiln chamber through a regulatory apparatus. Within the oxidation chamber, temperatures of 3200 degrees F., plus, will be maintained by injecting a regulated flow of pure oxygen, as an oxidant, to ensure the complete oxidation of all materials. After suitable preparation, solids and liquids will be introduced into the kiln chamber through an enclosed, sealed, apparatus i.e., screw conveyor, to control refuse volumes. During the oxidation process, the refuse materials will be kept in suspension for an adequate dwell time by the tilted orientation and rotating operation of the kiln apparatus. Any liquid residue will form a liquid bed at the low end of the chamber while the gaseous residue will rise to the high end. As a result, the liquid residue will continuously exit the chamber through an enclosed trap apparatus, while the gaseous residue will continuously exit the chamber through an enclosed duct system. After exiting the chamber, the liquid residue will be cooled and restructured into environmentally safe products. After exiting the chamber, the gaseous residue will be compressed, cooled, and fractionated into environmentally safe products.

Abstract translation: 本摘要描述了城市垃圾和某些危险物质的完全氧化过程。 容纳该方法的设备由完全封闭的旋转圆柱形窑组成，其中固体，液体和气态化合物同时被氧化。 为了补充燃烧过程，天然气将通过调节装置注入窑室。 在氧化室内，通过注入作为氧化剂的纯氧的调节流将保持3200°F的温度，以确保所有材料的完全氧化。 在适当的制备之后，固体和液体将通过封闭的密封的设备即螺旋输送机引入窑室，以控制垃圾的体积。 在氧化过程中，通过窑设备的倾斜定向和旋转操作，垃圾将被保持在悬浮状态以达到足够的停留时间。 任何液体残余物将在室的低端形成液床，而气态残余物将升至高端。 结果，液体残留物将通过封闭的捕集装置连续地离开室，而气态残留物将通过封闭的管道系统连续地离开室。 离开室后，液体残余物将被冷却并重组成环保产品。 离开室后，气态残渣将被压缩，冷却，并分馏成环保产品。

公开(公告)号：US5425923A

公开(公告)日：1995-06-20

申请号：US966999

申请日：1992-10-27

Applicant: George W. Swisher, Jr. ,  Jerry R. Collette

Inventor： George W. Swisher, Jr. ,  Jerry R. Collette

IPC: B09C1/06 ,  F23G7/14 ,  B01J8/08

CPC classification number: F23G7/14 ,  B09C1/06 ,  F23G2201/50 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/70 ,  F23G2900/50214

Abstract: A system for remediating soil containing contaminants. The system comprises a rotary volatilizer, a thermal dust conductor, a soil cooler, a separator and an afterburner. The rotary volatilizer includes a rotatable, counterflow volatilizer drum with a drying zone, a heating zone and a burn zone. The burn zone of the volatilizer has an outer shell and a stainless steel inner liner supported by spring brackets within the outer shell. A separator is provided to receive exhaust gases from the volatilizer and the soil cooler and to remove dust from the exhaust gases. Dust from the separator and hot soil from the volatilizer is introduced into the thermal dust conductor. Hot gases from the thermal dust conductor are returned to the volatilizer to preheat combustion air for the volatilizer and to incinerate contaminants in the returned gases. Soil is transferred from the thermal dust conductor to the soil cooler, where water injection cools the remediated soil and adds moisture to the soil. The cool remediated soil is conveyed from the soil cooler to a load out hopper.

Abstract translation: 一种补救含有污染物的土壤的系统。 该系统包括旋转挥发器，热尘导体，土壤冷却器，分离器和加力燃烧器。 旋转挥发器包括具有干燥区，加热区和燃烧区的可旋转的逆流挥发器鼓。 挥发器的燃烧区具有外壳和由外壳内的弹簧支架支撑的不锈钢内衬。 提供分离器以接收来自挥发器和土壤冷却器的废气并除去废气中的灰尘。 来自分离器的灰尘和来自挥发物的热土被引入热尘导体中。 来自热尘导体的热气体返回到挥发器中以预热挥发器的燃烧空气并焚烧返回气体中的污染物。 土壤从热尘导体转移到土壤冷却器，在这里，注水冷却修复后的土壤，并向土壤中添加水分。 冷却补救的土壤从土壤冷却器输送到装载出料斗。

公开(公告)号：US4270470A

公开(公告)日：1981-06-02

申请号：US33573

申请日：1979-04-27

Applicant: William O. Barnett ,  William K. Barnett

Inventor： William O. Barnett ,  William K. Barnett

IPC: B03B9/06 ,  B07B9/00 ,  F23G5/00 ,  F23G5/02 ,  F23G5/32 ,  F23N5/00

CPC classification number: F23G5/02 ,  B03B9/06 ,  B07B9/00 ,  F23G5/006 ,  F23G5/32 ,  F23N5/006 ,  F23G2201/602 ,  F23G2201/603 ,  F23G2201/80 ,  F23G2202/20 ,  F23G2203/30 ,  F23G2205/122 ,  F23G2205/20 ,  F23G2207/102 ,  F23G2207/103 ,  F23G2207/20 ,  F23G2207/30 ,  F23G2209/12 ,  F23G2209/26 ,  F23G2900/50214 ,  Y02W30/521

Abstract: The preferred embodiment of the invention disclosed herein includes apparatus for and steps of separating glass, metal and other generally non-combustible material from refuse to provide a volume of generally combustible refuse, shredding this volume of combustible refuse into relatively small particles, mixing these particles with primary combustion air and conveying the resultant mixture of air and particles into a combustion chamber. The combustion chamber is preheated by auxiliary heating means to a temperature sufficient to cause the mixture to be self-igniting in the combustion chamber. Secondary combustion air is fed to the combustion chamber at spaced-apart points within the chamber for assuring a complete combustion process. This chamber is maintained under a negative pressure by a fan downstream and the combustion gases are thus caused to flow from the combustion chamber to an associated device utilizing the heat energy, for example, a steam boiler, and from the steam boiler, the gases are exhausted through a stack to the atmosphere. Oxygen measuring means is located on the discharge side of the boiler for measuring the amount of excess oxygen discharged to the atmosphere. In response to this measurement, the feed rate of the shredded particles of refuse is adjusted to maintain a substantially constant amount of excess oxygen in the combustion gases whereby the B.T.U. output is controlled.

Abstract translation: 本文公开的本发明的优选实施例包括用于将玻璃，金属和其它通常不可燃材料与垃圾分离以提供一定体积的可燃垃圾的装置和步骤，将该体积的可燃垃圾粉碎成相对较小的颗粒，将这些颗粒 与主燃烧空气并将所得的空气和颗粒混合物输送到燃烧室中。 燃烧室由辅助加热装置预热到足以使混合物在燃烧室中自燃的温度。 二次燃烧空气在室内的间隔点处被供给到燃烧室，以确保完全燃烧过程。 该室由下游的风扇保持在负压下，因此燃烧气体利用热能例如蒸汽锅炉从燃烧室流向相关联的装置，并且从蒸汽锅炉，气体是 通过堆栈耗尽大气。 氧气测量装置位于锅炉的排放侧，用于测量排放到大气中的过量氧气的量。 响应于该测量，调节粉碎的垃圾颗粒的进料速率以保持燃烧气体中基本上恒定的过量氧气量，由此B.T.U. 输出被控制。

公开(公告)号：WO2011142437A1

公开(公告)日：2011-11-17

申请号：PCT/JP2011/060997

申请日：2011-05-12

Applicant: 三菱重工業株式会社 ,  竹内 和広 ,  大丸 卓一郎 ,  木下 正昭 ,  山口 啓樹 ,  甲斐 徳親

Inventor： 竹内　和広 ,  大丸　卓一郎 ,  木下　正昭 ,  山口　啓樹 ,  甲斐　徳親

IPC: B02C15/04 ,  C10L5/44 ,  F23C1/00 ,  F23K3/00

CPC classification number: F23K1/00 ,  B02C15/003 ,  B02C15/004 ,  B02C15/007 ,  C10L5/04 ,  C10L5/366 ,  C10L5/44 ,  F23C2900/01001 ,  F23G5/033 ,  F23G2201/60 ,  F23G2201/602 ,  F23G2201/70 ,  F23K1/04 ,  F23K2201/10 ,  F23K2201/103 ,  F23K2201/30 ,  F23K2201/501 ,  Y02E50/10 ,  Y02E50/30

Abstract: 　バイオマス原料(11)を粉砕する鉛直軸方向上方から供給する原料供給管(12)と、バイオマス原料(11)が載置される粉砕テーブル(14)と、粉砕テーブル(14)の回転と連動して作動し、バイオマス原料(11)を押圧力により粉砕する粉砕ローラ(16)と、上昇流を形成する送風手段と、粉砕したバイオマス粉体(17)を分級する分級機(19)と、を具備する粉砕装置(13)において、粉砕テーブル(14)のテーブルライナ(14b)の表面に、その内周部から外縁側に向けて放射状のテーブル溝(31)が複数形成されると共に、その溝(31)の先端がテーブルライナ中央部近傍までとした粉砕装置。

Abstract translation: 公开了一种粉碎装置（13），其具备：原料供给管（12），其沿上下方向从生物质原料（11）被粉碎的位置沿垂直轴方向供给生物质原料（11） 在其上放置生物质原料（11）的粉碎台（14）; 与粉碎台（14）的旋转一起移动的粉碎辊（16），并通过挤压力粉碎生物质原料（11）; 产生上升气流的吹风装置; 以及对粉碎的生物质粉末（17）进行分类的分级器（19）。 在粉碎台（14）的台板（14b）的表面上形成有多个工作台槽（31），其从其内周部朝向粉台（14）的外边缘侧辐射， 的凹槽（31）的靠近桌衬（14b）的中心部分。