公开(公告)号：US06907994B2

公开(公告)日：2005-06-21

申请号：US10274285

申请日：2002-10-18

Applicant: William S. Bradley ,  Robert L. Carnahan ,  Frank A. Elk ,  Riley D. Robbins

Inventor： William S. Bradley ,  Robert L. Carnahan ,  Frank A. Elk ,  Riley D. Robbins

IPC: B03B9/04 ,  C04B18/08 ,  F26B1/00 ,  F26B3/20 ,  B09B3/00 ,  B07B1/46

CPC classification number: F26B3/205 ,  B03B9/04 ,  C04B18/08 ,  C04B2111/1087 ,  F26B1/00 ,  Y02W30/92 ,  Y10S106/01 ,  C04B20/04

Abstract: There is provided a process for converting wet fly ash into a useful product such as cement replacement or industrial filler. A first amount of wet fly ash is provided. The wet fly ash is fed into a mixing chamber. An amount of aggregate, such as stone, is provided. The aggregate is also fed into the mixing chamber where the wet fly ash is mixed with the aggregate. The mixed wet fly ash and aggregate is fed into a drying chamber where the mixture is heated, thereby drying the fly ash and heating the aggregate. The heated aggregate is separated from the fly ash. The heated aggregate is fed back into the mixing chamber. A second amount of wet fly ash is added to the mixing chamber where is it mixed with the heated aggregate. The heated aggregate assists in drying the second amount of wet fly ash. Once in cycle, the process is continuous. Preferably, after the dried fly ash is segregated from the heated aggregate, it is introduced to a burner where the carbon component is oxidized and the beneficated fly ash exits.

Abstract translation: 提供了将湿粉煤灰转化成有用产品如水泥替代品或工业填料的方法。 提供第一量的湿粉煤灰。 将湿粉煤灰送入混合室。 提供了一些总量，如石头。 聚集体也进料到混合室中，其中湿粉煤灰与聚集体混合。 将混合的湿粉煤灰和骨料进料到干燥室中，混合物被加热，从而干燥飞灰并加热聚集体。 加热的聚集体与飞灰分离。 将加热的聚集体反馈到混合室中。 向混合室中加入第二量的湿粉煤灰，其中与加热的聚集体混合。 加热的聚集体有助于干燥第二量的湿粉煤灰。 一旦循环，过程是连续的。 优选地，在将干燥的飞灰与加热的聚集体分离之后，将其引入燃烧器中，其中碳组分被氧化并且有益的飞灰离开。

公开(公告)号：US20050051500A1

公开(公告)日：2005-03-10

申请号：US10657730

申请日：2003-09-08

Applicant: Charles Price ,  William Barnwell ,  John Groppo

Inventor： Charles Price ,  William Barnwell ,  John Groppo

IPC: B03B9/04 ,  C02F1/38 ,  C02F1/56 ,  C02F1/66 ,  C02F11/12 ,  C10J3/52 ,  C02F1/00

CPC classification number: C10J3/526 ,  B03B9/04 ,  C02F1/001 ,  C02F1/38 ,  C02F1/56 ,  C02F1/66 ,  C02F11/121 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10J2300/1807 ,  C10J2300/1884 ,  C10J2300/1892

Abstract: The present invention provides a method of beneficiating slag, including mixing the slag with water to form a slurry. The slurry is screened through a first screen to remove a first portion of material and then screened through a second screen to remove a second portion of material. In one embodiment, the second portion of material has a carbon content less than about 5% and, more preferably, a carbon content less than about 1%.

Abstract translation: 本发明提供一种选矿渣的方法，包括将炉渣与水混合以形成浆料。 通过第一屏幕筛选浆料以除去第一部分材料，然后通过第二筛网筛选以除去第二部分材料。 在一个实施方案中，第二部分材料具有小于约5％的碳含量，更优选碳含量小于约1％。

公开(公告)号：US06814013B2

公开(公告)日：2004-11-09

申请号：US10401007

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: F23J100

CPC classification number: F23G5/006 ,  B03B9/04 ,  F23G2201/602 ,  F23G2202/106 ,  F23G2209/30 ,  F23J1/00 ,  F23J2900/01001 ,  F23J2900/01005

Abstract: In the process for treating incineration residues from waste incineration plants, the incineration material is incinerated on a furnace grate. The incineration residues produced are quenched in a wet slag remover and conveyed out of the latter. The wet incineration residues which come out of the wet slag remover are firstly divided into two fractions by means of a screening operation, after which the main fraction is washed with water taken from the wet slag remover, and in the process adhering fine pieces are separated off. The washed pieces of the incineration residues are fed for reuse. The washing water together with the ultra fine pieces which have been taken up during the washing operation pass into the wet slag remover. The fine fraction produced during the mechanical separation operation is fed back to the incineration operation.

公开(公告)号：US20030206850A1

公开(公告)日：2003-11-06

申请号：US09906941

申请日：2001-07-18

Inventor： Christoph Schultheiss ,  Christel Adelheim ,  Britta Bergfeldt ,  Ralf Straessner ,  Volker Neuben ,  Helmul Dinnig ,  Bernard Kotte

IPC: C01B031/24

CPC classification number: C22B7/005 ,  B02C19/18 ,  B02C2019/183 ,  B03B9/04 ,  B09B3/00 ,  C22B7/006 ,  C22B7/04 ,  Y02P10/234

Abstract: In a method and apparatus for processing materials comprising ashes from waste incineration plants and mineral residues to condition them in a short time by washing them and by subjecting them to electrodynamic processes and shock waves generated by high voltage spark discharges, the material is made chemically inert and aged so that it can be used immediately after treatment without harming the environment.

Abstract translation: 在用于处理来自废物焚烧厂和矿物残余物的灰分的材料的处理材料的方法和装置中，通过洗涤它们并在短时间内对其进行电动处理和由高压火花放电产生的冲击波进行处理，材料被制成化学惰性 老化，可以在治疗后立即使用，不会对环境造成伤害。

公开(公告)号：US06589654B1

公开(公告)日：2003-07-08

申请号：US08948985

申请日：1997-10-10

Applicant: Gianni B. Arcaini ,  Gary M. Carraux ,  William R. Gibbes ,  Takemoto Yashiro ,  Takanori Hirao ,  Kaoru Ishizuka

Inventor： Gianni B. Arcaini ,  Gary M. Carraux ,  William R. Gibbes ,  Takemoto Yashiro ,  Takanori Hirao ,  Kaoru Ishizuka

IPC: B32B1500

CPC classification number: A62D3/33 ,  A62D2101/08 ,  A62D2101/43 ,  B03B9/04 ,  C04B18/10 ,  E01C3/003 ,  Y02W30/92 ,  Y10T428/25 ,  Y10T428/2982 ,  Y10T428/2996 ,  C04B20/023

Abstract: Construction material from granular material reclaimed from the ash of a municipal waste combustor wherein the ash is subjected to sorting and separating recovered metals, the granular material including particles having a maximum particle diameter of 5 to 40 mm, a U-coefficient of 10 or more, and ignition loss of 10% or less in weight and being subjected to at least one heavy metal immobilization agent, preferably phosphoric acid; and a second heavy metal immobilization agent consisting of ferrous sulfate. The ash is further subjected to drying before subjecting the ash to the at least one heavy metal immobilization agent. The ash is further subjected to mulling the material after subjecting the ash to the at least one heavy metal immobilization agent.

Abstract translation: 从城市垃圾焚烧炉的灰分回收的颗粒材料的构造材料，其中灰分经过分选和分离回收的金属，颗粒材料包括最大粒径为5至40mm的颗粒，U系数为10或更大 ，灼烧损失为10重量％以下，并经受至少一种重金属固定剂，优选磷酸; 和由硫酸亚铁组成的第二重金属固定剂。 在将灰分经受至少一种重金属固定剂之前，将灰分进一步进行干燥。 灰分在使灰分经受至少一种重金属固定剂之后进一步对该材料进行研磨。

公开(公告)号：US06500229B1

公开(公告)日：2002-12-31

申请号：US09673051

申请日：2000-10-06

Applicant: Gilles Roux ,  Farouk Tedjar

Inventor： Gilles Roux ,  Farouk Tedjar

IPC: C22B702

CPC classification number: B03B9/04 ,  B03B7/00 ,  C22B7/008 ,  C22B7/02 ,  C22B19/24 ,  C22B19/26 ,  C25C1/16 ,  C25C7/002 ,  C25C7/02 ,  Y02P10/234 ,  Y10S75/961

Abstract: A method for treating steel works dust in order to recuperate elements capable of being upgraded. The method comprises attrition in water followed by hydraulic grading of the resulting load. The method is characterized in that is further comprises: a washing step to separate the water soluble saline fractions of the insoluble oxides; hot treatment to eliminate metals in the form of free oxides such as zinc and lead; treatment by heating at a temperature ranging between 240 and 800° C.; treatment with sulphuric acid having a concentration between 5 and 8%.

Abstract translation: 一种用于处理钢铁灰尘的方法，以便恢复能够升级的元件。 该方法包括在水中磨损，然后对所得负载进行液压分级。 该方法的特征在于还包括：分离不溶性氧化物的水溶性盐馏分的洗涤步骤; 热处理以消除诸如锌和铅的游离氧化物形式的金属; 在240〜800℃的温度范围内进行加热处理。 用浓度为5至8％的硫酸处理。

公开(公告)号：US06484882B1

公开(公告)日：2002-11-26

申请号：US09718893

申请日：2000-11-22

Applicant: Joachim Boretzky ,  Anton Ebert ,  Leonhard Teschers ,  Winfried Von Rhein ,  Helmut Werdinig

Inventor： Joachim Boretzky ,  Anton Ebert ,  Leonhard Teschers ,  Winfried Von Rhein ,  Helmut Werdinig

IPC: B07B900

CPC classification number: C10B53/00 ,  B03B9/04

Abstract: In order to separate a carbon-containing fraction as completely as possible from a residue, for example a pyrolysis residue, a combustible constituent is first separated from a non-combustible constituent. A carbon-containing light fraction is subsequently separated from a small-fragment fraction of the non-combustible constituent. For this purpose, in a preferred embodiment, a combination of a facility for the separation of wire with a heavy-fragment separator following the latter is provided for a continuous separation operation. The carbon-containing fraction thus obtained is preferably supplied for further utilization to a combustion chamber of a pyrolysis plant.

Abstract translation: 为了将残留物（例如热分解残渣）尽可能完全地分离，可燃成分首先从不可燃成分中分离出来。 随后将含碳轻馏分与不可燃组分的小碎片部分分离。 为此，在优选的实施方案中，提供用于分离丝线的设备与后者之间的重片分离器的组合用于连续分离操作。 由此获得的含碳馏分优选供应用于进一步利用到热解设备的燃烧室。

公开(公告)号：US06422392B1

公开(公告)日：2002-07-23

申请号：US09541962

申请日：2000-04-04

Applicant: Edward Kenneth Levy

Inventor： Edward Kenneth Levy

IPC: B07B400

CPC classification number: B03B4/00 ,  B03B4/06 ,  B03B5/46 ,  B03B9/04

Abstract: A process for removing ammonia from fly ash during processing on an inclined fluidized bed. The process begins by introducing a mixture of particulates having ammonia adsorbed therein into an inclined fluidized bed. Concurrently, a fluidizing gas is pre-heated and is also introduced into the fluidized bed. The mixture is then processed along the fluidized bed with the pre-heated fluidizing gas to achieve bubbling fluidization of the particles. This causes segregation by which a dense fraction settles downward and a light fraction rises upward in the bed. Ammonia in the particles is desorbed by the pre-heated fluidizing gas. The fluidizing gas is then scrubbed after the processing step to remove the desorbed ammonia. The process may also include the use of acoustic enhancement whereby an acoustic field is imposed on the fluidized bed to improve fluidization and segregation of the particles and to increase the efficacy of ammonia removal. In addition, a heat exchanger or electric heating elements immersed in the fluidized bed can be used to heat the ash to the temperatures needed to desorb ammonia from the ash. Furthermore, the energy efficiency of the process can be improved by recovering heat from the hot ash discharged from the fluidized bed and/or from the exhaust stream of hot fluidizing gas, for reuse during preheating steps. The improved process removes ammonia in a simple and efficient manner by preheating the fluidizing gas of the inclined bed to temperatures of 300 to 500° F., and using this preheated gas to drive off any adsorbed ammonia.

Abstract translation: 在倾斜流化床加工过程中从飞灰中除去氨的方法。 该方法开始于将其中吸附了氨的微粒的混合物引入到倾斜流化床中。 同时，流化气体被预热并且也被引入到流化床中。 然后将混合物沿着流化床与预热的流化气体一起处理，以实现颗粒的起泡流化。 这导致偏析，致密部分向下沉降，轻馏分在床上向上升高。 颗粒中的氨被预热的流化气体解吸。 然后在处理步骤之后洗涤流化气体以除去解吸的氨。 该方法还可以包括使用声学增强，由此在流化床上施加声场以改善颗粒的流化和分离并提高除氨的效力。 此外，浸入流化床中的热交换器或电加热元件可用于将灰加热到从灰分解氨中所需的温度。 此外，可以通过从流化床排出的热灰和/或从热流化气体的废气流回收热量来提高该方法的能量效率，以便在预热步骤期间重新使用。 改进的方法通过将倾斜床的流化气体预热至300至500°F的温度，并使用该预热气体驱除任何吸附的氨，从而以简单有效的方式除去氨。

公开(公告)号：US20020079392A1

公开(公告)日：2002-06-27

申请号：US09950936

申请日：2001-09-12

Applicant: Shinroku Seiki Kabushiki Kaisha

Inventor： Takao Tango ,  Yo Ito ,  Hirohiko Shibata ,  Kenji Kawaguchi ,  Yutaka Shida

IPC: B02C019/00

CPC classification number: B03B9/00 ,  B03B9/04 ,  B09B3/00 ,  B09C1/02

Abstract: Object of the invention is to finely granulate the granular substances with pollutants, such as the contaminated soils and incinerated ashes, adhered and to separate the pollutants from the granular substances efficiently and further to enable the unnoxious granular substances, from which pollutants as above have been separated, to be recycled. After carrying out fine granulation of the granular substances by carrying out a coarse disintegrating treatment on the granular substances with pollutants adhered through the first fine granulation machine 21, the granular substances, which have been finely granulated by the first fine granulation machine, are subjected to, by the second fine granulation machine 22, mutual polishing among the granular substances themselves being acted by mutual rubbing forces of the substance themselves and thus the pollutants, such as heavy metals and dioxin class substances adhering strongly to the surfaces of the granular substances are separated and also the granular substances without containing the pollutants are classified from the granular substances which have already been finely granulated by the first and second fine granulation machines by the vibrational screen 30 and the classification means 50.

Abstract translation: 本发明的目的是对污染物，污染灰烬等污染物进行细粒化，从而有效地进一步分离颗粒物质中的污染物，进一步使上述污染物成为无毒的粒状物质 分离，待回收。 通过对通过第一细粒化机21粘附的污染物的颗粒状物质进行粗粉碎处理，对粒状物进行细粒化后，将由第一细粒化机进行细粒化的粒状物质 通过第二细粒化机22，颗粒物质本身之间的相互抛光由物质本身的相互摩擦力作用，因此分散在颗粒物质表面的重金属和二恶类物质等污染物被分离 并且不含有污染物的颗粒状物质由通过第一和第二细粒化机通过振动筛30和分类装置50已被细粒化的颗粒状物质分类。

公开(公告)号：US06402064B1

公开(公告)日：2002-06-11

申请号：US09422782

申请日：1999-10-21

Applicant: Takao Tango ,  Yo Ito ,  Hirohiko Shibata ,  Kenji Kawaguchi ,  Yutaka Shida

Inventor： Takao Tango ,  Yo Ito ,  Hirohiko Shibata ,  Kenji Kawaguchi ,  Yutaka Shida

IPC: B02C1912

CPC classification number: B03B9/00 ,  B03B9/04 ,  B09B3/00 ,  B09C1/02

Abstract: Granular substances with pollutants adhered, such as contaminated soils and incinerated ashes, are finely granulated to separate the pollutants from the granular substances efficiently and to enable the granular substances, from which pollutants have been separated, to be recycled. After fine granulation of the granular substances by a coarse disintegrating treatment through a first fine granulation machine, the granular substances, which have been finely granulated by the first fine granulation machine, are subjected to, by a second fine granulation machine, mutual polishing among the granular substances by mutual rubbing forces of the substances themselves and thus the pollutants, such as heavy metals and dioxin class substances adhering strongly to the surfaces of the granular substances, are separated, and also the granular substances not containing the pollutants are classified from the granular substances which have already been finely granulated by a vibrational screen and a classification device.

Abstract translation: 颗粒物质如污染土壤和焚化灰分被细粒化，可以有效地分离颗粒物质中的污染物，使污染物被分离的颗粒物质被回收利用。 在通过第一细粒化机通过粗粉碎处理对颗粒状物质进行细粒化后，将通过第一细粒化机细粒化的粒状物质通过第二细粒化机进行相互抛光 颗粒物质通过物质本身的相互摩擦力以及因此强烈粘附到颗粒物质表面的重金属和二恶类物质等污染物被分离，并且不含污染物的颗粒物质也从粒状物 已经通过振动筛和分级装置精细造粒的物质。