公开(公告)号：US08361187B2

公开(公告)日：2013-01-29

申请号：US13066639

申请日：2011-04-20

Applicant: Alfred Edlinger

Inventor： Alfred Edlinger

IPC: C22B7/02 ,  C22B7/04

CPC classification number: C22B5/10 ,  C21B13/002 ,  C21C5/5241 ,  C21C5/567 ,  C22B7/04 ,  C22B9/003 ,  F27B1/10 ,  Y02P10/136 ,  Y02P10/216 ,  Y02P10/253

Abstract: A method for reducing oxidic slags and dusts possibly loaded with organics uses an inductively heatable coke bed extending in the axial direction and having a temperature gradient. Reaction gas is sucked off in an axial region of the coke bed between two induction bodies and metal regulus and slag melt are tapped on the lower end. An inductively heatable shaft furnace chargeable with a lumpy coke bed for the reduction of metallic slags is made of an electrically insulating refractory material, has an adjustable temperature gradient includes at least one cooled induction body on the head side, a suction connection in an axial region where the prevailing temperature exceeds the condensation point of the substances to be removed, located below the cooled induction body on the head side, and an opening for tapping metal regulus and slag melt is provided on the lower end of the furnace.

Abstract translation: 减少可能装有有机物的氧化渣和粉尘的方法使用沿轴向延伸并且具有温度梯度的可感应加热的焦炭床。 反应气体在两个诱导体之间的焦炭床的轴向区域中被吸出，并且金属沉降物被抽出，熔渣熔化在下端。 一种用于还原金属渣的块状焦炭床可感应加热的竖炉由电绝缘耐火材料制成，具有可调节的温度梯度，其包括在头部侧上的至少一个冷却的感应体，轴向区域中的吸入连接 其中主要温度超过要去除的物质的冷凝点，其位于头部侧的冷却的感应体下方，并且在炉的下端设置用于攻丝金属腐蚀和熔渣的开口。

公开(公告)号：US20050138964A1

公开(公告)日：2005-06-30

申请号：US10504377

申请日：2003-02-14

Applicant: Alfred Edlinger

Inventor： Alfred Edlinger

IPC: C03B3/02 ,  C03B5/00 ,  C03B5/12 ,  C21B3/04 ,  C21C5/52 ,  C22B7/00 ,  C22B7/02 ,  F27D3/00 ,  C03B5/235

CPC classification number: C03B3/026 ,  C03B5/005 ,  C03B5/12 ,  C21B3/04 ,  C21C5/5217 ,  C22B7/003 ,  C22B7/02 ,  F27D3/0025 ,  Y02P10/216 ,  Y02P40/52 ,  Y02W30/542

Abstract: In a device for melting precrushed material and/or dusts such as, e.g., furnace dusts or steel dusts, marl and lime dust mixtures, shredder light fractions and/or crushed waste substances, in which the material and/or dusts are injected into a combustion chamber along with a carrier gas, the dusts and/or are introduced axially, and the carrier gas is introduced tangentially, into a cyclone 3. The cyclone 3 is connected with a combustion chamber (8) via a substantially axially directed discharge opening (9).

Abstract translation: 在用于熔化预先冲洗的材料和/或粉尘的装置中，例如炉灰或钢粉尘，碎石灰和灰尘混合物，粉碎的轻馏分和/或粉碎的废物，其中将材料和/或粉尘注入 燃烧室和载气，尘埃和/或轴向引入，并且载气被切向地引入旋风分离器3中。 旋风分离器3通过基本上轴向排出的开口（9）与燃烧室（8）连接。

公开(公告)号：US06666996B1

公开(公告)日：2003-12-23

申请号：US09890820

申请日：2001-08-02

Applicant: Alfred Edlinger

Inventor： Alfred Edlinger

IPC: B29B900

CPC classification number: C04B35/653 ,  C04B7/153 ,  C04B33/13 ,  C04B35/62695 ,  Y02P40/143 ,  C04B7/436

Abstract: In a process for producing marl slags and marl slag cements or mixed components for mixed cements from marl having a basicity CaO/SiO2 of

Abstract translation: 在碱性CaO / SiO 2 <2.0的马来酸盐混合水泥的生产过程中，规定在第一工艺步骤中，具有碱性的泥质渣或泥土和粘土的混合物 的<2.0被干燥，预热和煅烧，然后在第二工艺步骤中获得的产品在比在第一工艺步骤中施加的温度更高的温度下在独立的熔炉中熔化，并从熔体中造粒。

公开(公告)号：US06660223B2

公开(公告)日：2003-12-09

申请号：US09959060

申请日：2001-10-16

Applicant: Alfred Edlinger

Inventor： Alfred Edlinger

IPC: C21C100

CPC classification number: C04B5/06 ,  C21B3/08

Abstract: In a device for atomizing liquid melts, in particular oxidic slags or glasses, including a slag tundish and an outlet opening into which a lance is immersed to inject gases or vapor while forming an annular gap, the lance (3) is comprised of two coaxial tubes (4, 5) which are separately displaceable in the axial direction and fixable in their respective axially displaced positions.

Abstract translation: 在用于雾化液体熔体的装置中，特别是氧化炉渣或玻璃，包括炉渣中间包和出口，在形成环形间隙的同时，喷枪穿过其喷射气体或蒸气，喷枪（3）由两个同轴 管（4,5），其可以在轴向方向上分开移动并可固定在其相应的轴向位移位置。

公开(公告)号：US6082640A

公开(公告)日：2000-07-04

申请号：US331886

申请日：1999-06-29

Applicant: Alfred Edlinger

Inventor： Alfred Edlinger

IPC: C21B3/08

CPC classification number: C21B3/08

Abstract: In a process for granulating and comminuting molten material, the slag melt is acted upon by compressed water and discharged together with the vapour formed. The liquid slag is introduced into a granulation chamber in a free flowing jet while directing compressed water jets against the slag jet, whereupon the solidified and granulated slag is conducted through a pneumatic conveyor duct and a distributor along with the vapour formed. The partial streams leaving the distributor, via conically tapering nozzles are transferred into a grinding space exhibiting a lower pressure than the granulation space and from which the comminuted and solidified material is drawn off.

Abstract translation: PCT No.PCT / AT98 / 00243 Sec。 371日期1999年6月29日第 102（e）1999年6月29日PCT PCT 1998年10月14日PCT公布。 公开号WO99 /​​ 22031 日期1999年5月6日在熔融材料造粒和粉碎的方法中，熔渣通过压缩水作用并与形成的蒸汽一起排出。 将液体炉渣以自由流动的射流引入造粒室，同时将压缩水射流引导到炉渣射流上，由此固化和造粒的炉渣与形成的蒸气一起通过气动输送管道和分配器传导。 通过锥形锥形喷嘴离开分配器的部分流被转移到显示比造粒空间低的压力的研磨空间中，并且粉碎和固化的材料被从中排出。

公开(公告)号：US6059854A

公开(公告)日：2000-05-09

申请号：US913727

申请日：1997-09-17

Applicant: Alfred Edlinger ,  Bruno Mistelli

Inventor： Alfred Edlinger ,  Bruno Mistelli

IPC: C03B5/04 ,  C21B3/04 ,  C21C5/36 ,  C22B7/04 ,  C21B3/08

CPC classification number: C21B3/04 ,  C21C5/36 ,  C22B7/04 ,  Y02P10/232 ,  Y02W30/542

Abstract: A method for processing solid waste incineration residues is disclosed in which the residues are introduced a steelworks slag bath in a sufficient amount so that the residues constitute from 15-45% by weight of the combined weight of the solid waste incineration residues and the steelworks slag bath. The residues are melted to effect the evaporation of heavy metals; which are drawn off from the steelworks slag bath to leave a heavy-metal-depleted slag bath. The residual bath is reduced with carbon carriers to form a slag phase and a pig iron phase. The slag phase can be granulated to produce mixed cement components.

Abstract translation: PCT No.PCT / AT97 / 00007 Sec。 371日期1997年9月17日 102（e）1997年9月17日PCT PCT 1997年1月23日PCT公布。 公开号WO97 / 27339 日期1997年7月31日公开了一种处理固体废物焚烧残渣的方法，其中残留物被引入足够量的钢厂渣槽，使得残余物占固体废物焚烧的组合重量的15-45重量％ 残渣和炼钢厂渣槽。 残余物被熔化以实现重金属的蒸发; 从炼钢厂渣槽中取出，留下重金属贫化渣槽。 残余浴用碳载体还原，形成渣相和生铁相。 渣相可以造粒以产生混合的水泥组分。

公开(公告)号：US6036768A

公开(公告)日：2000-03-14

申请号：US117582

申请日：1998-07-29

Applicant: Alfred Edlinger ,  Juraj Gebauer ,  Horst Wolter

Inventor： Alfred Edlinger ,  Juraj Gebauer ,  Horst Wolter

IPC: C04B7/13 ,  C04B24/16 ,  C04B28/02

CPC classification number: C04B24/16 ,  C04B28/02 ,  C04B7/13 ,  Y02W30/92 ,  Y10S106/01

Abstract: The cement composition of this invention includes 10 to 35% by weight of portland cement, 65 to 90% by weight of a synthetic pozzolan, and an activator for reducing the positive surface potential of the synthetic pozzolan. The synthetic pozzolan is obtained by an at least partial reduction from combustion residues having a SiO.sub.2 /CaO ratio of greater than 1:1 and containing Na.sub.2 O and K.sub.2 O as alkali oxides in an amount exceeding 1.5% by weight. The activator includes anionically active or anionic tensides.

Abstract translation: PCT No.PCT / AT97 / 00256 Sec。 371日期1998年7月29日第 102（e）日期1998年7月29日PCT 1997年11月21日PCT PCT。 第WO98 / 23550号公报 日期1998年6月4日本发明的水泥组合物包含10-35重量％的波特兰水泥，65-90重量％的合成火山灰，以及用于降低合成火山灰的正表面电位的活化剂。 合成火山灰是通过SiO 2 / CaO比大于1:1的燃烧残余物的至少部分还原得到的，其含有Na 2 O和K 2 O作为碱金属氧化物，其量超过1.5重量％。 活化剂包括阴离子活性或阴离子表面活性剂。

公开(公告)号：US6010553A

公开(公告)日：2000-01-04

申请号：US913702

申请日：1997-09-16

Applicant: Alfred Edlinger ,  Albert Waschnig

Inventor： Alfred Edlinger ,  Albert Waschnig

IPC: C04B7/147 ,  C04B7/153 ,  C04B7/28 ,  C21B3/04 ,  C21B3/06 ,  C21B11/00 ,  C22B7/04 ,  C21B13/14

CPC classification number: C04B7/153 ,  C04B7/28 ,  C21B11/00 ,  C21B3/04 ,  C21B3/06 ,  C22B7/04 ,  Y02P10/136 ,  Y02P10/212 ,  Y02P40/143 ,  Y02P40/145 ,  Y02W30/542 ,  Y02W30/543 ,  Y10S75/961

Abstract: In a process for producing pig iron, nonferrous heavy metal alloys, ferrochromium carbure or carbon-free ferrochromium and synthetic blast furnace slags, using metal-oxide-containing waste incineration residues or slags, the charging materials of waste burning, e.g., car shredder light fractions and/or metallurgical dusts, are at least partially oxidized and subsequently are reduced while separating nonferrous metals or alloys, whereupon the oxidic slag phase depleted from metals or alloys is mixed with liquid steelworks slag optionally upon further addition of metallurgical dusts, whereupon crude steel is drawn off while lowering the viscosity of the steelworks slag and the remaining slag portion is subjected to further reduction while recovering pig iron and optionally Fe chromium alloys, whereupon the resulting synthetic blast furnace slag is discharged.

Abstract translation: PCT No.PCT / AT97 / 00006 Sec。 371日期：1997年9月16日 102（e）1997年9月16日PCT PCT 1997年1月16日PCT公布。 公开号WO97 / 26381 日期1997年7月24日在生产生铁，有色重金属合金，铬铁碳化物或无碳铬铁和合成高炉炉渣的过程中，使用含有氧化物的废物焚烧残渣或炉渣，废物燃烧的充电材料， 例如，汽车碎纸机轻馏分和/或冶金粉尘至少部分被氧化并随后在分离有色金属或合金的同时被还原，随后从金属或合金中消耗的氧化渣相与液态钢铁渣混合，任选地在进一步添加冶金 因此，在降低钢厂渣的粘度的同时，粗钢被拔出，剩余的炉渣部分在回收生铁和任选的Fe铬合金的同时进一步还原，随后所得的合成高炉矿渣排出。

公开(公告)号：US5671688A

公开(公告)日：1997-09-30

申请号：US568837

申请日：1995-12-07

Applicant: Markus Burgin ,  Bruno Carcer ,  Alfred Edlinger ,  Jean-Marc Martelli

Inventor： Markus Burgin ,  Bruno Carcer ,  Alfred Edlinger ,  Jean-Marc Martelli

IPC: B03B9/04 ,  C04B5/00 ,  F23J3/00

CPC classification number: B03B9/04

Abstract: In the process for treating slag from refuse incineration plants, the crude slag, after passing through the firing grate, is separated into at least two fractions directly and without previous quenching in a water bath. These two fractions are further processed separately, the coarse fraction being fed to a wet deslagger. For optimum separation of the two fractions, the first fraction, having a particle size preferably up to 32 mm, is separated off in a first screening stage and the screen oversize of the first screening stage is fed to the wet deslagging. The screen undersize and if appropriate the material passing through the firing grate are fed to a second screening stage to separate off the fine fraction 0 . . . 2 mm. The screen oversize of the second screening stage, if appropriate after removing metallic and inert materials, is mechanically comminuted. In an optional third screening stage (8), the fine fraction 0 . . . 2 mm is fed together with the screen undersize of the second screening stage to a special treatment.

Abstract translation: 在从垃圾焚烧厂处理炉渣的过程中，粗渣经过烧结炉排后直接分离成至少两个馏分，在水浴中不经过淬火。 这两个级分进一步分开处理，粗级分进料到湿式除渣器。 为了最佳分离两个级分，在第一筛选阶段分离具有优选至多32mm的粒度的第一级分，并将第一筛选阶段的筛网过筛进料至湿式除渣。 筛网尺寸过小，如果合适，将通过烧结炉排的材料进料到第二筛选阶段以分离细馏分0。 。 。 2毫米。 在除去金属和惰性材料之后，如果合适的话，第二筛选阶段的筛网尺寸被机械粉碎。 在可选的第三筛选阶段（8）中，细分为0。 。 。 2毫米与第二筛选阶段的筛网过小一起进行特殊处理。

公开(公告)号：US5405429A

公开(公告)日：1995-04-11

申请号：US60566

申请日：1993-05-12

Applicant: Theo Rey ,  Alfred Edlinger

Inventor： Theo Rey ,  Alfred Edlinger

IPC: B09B3/00 ,  C04B5/02 ,  C04B18/02 ,  C22B7/00 ,  C22B7/04 ,  C21B11/00

CPC classification number: C04B18/023 ,  Y02E50/30 ,  Y02W30/92

Abstract: In the processing of mainly inorganic refuse incineration products polluted by heavy metals and/or heavy metal compounds, and/or analogues of such products, to give environmentally acceptable products by melt-thermal treatment, an iron-containing melt is used whose iron content can be adjusted by addition of iron or an iron compound. The melt is first melted above 1300.degree. C. in a reactor. The melt is then oxidized with vigorous agitation by blowing in oxygen-containing gas until all the metals and metal compounds present in the reactor have been converted to the oxide form, the melt being kept above 1450.degree. C. and preferably at about 1500.degree. C., at least at the end of the oxidation. Subsequently, the melt is reduced, preferably by means of a part fraction of the refuse incineration product and/or iron, preferably in the form of scrap, and/or hydrogen. The reduction can then be continued by means of added aluminum and/or calcium and/or ferrosilicon. If appropriate, metal melt is fractionated in a lower part of the reactor and slag melt is separately collected as a supernatant layer. Heating energy can be saved by heat exchange and recirculation of fluid.

Abstract translation: 在主要由重金属和/或重金属化合物和/或这类产品的类似物污染的无机垃圾焚烧产品的加工中，通过熔融热处理得到环境可接受的产品，使用含铁熔体，其含铁量可以 通过加入铁或铁化合物进行调节。 熔化物首先在1300℃以上在反应器中熔化。 然后通过吹入含氧气体直到所有存在于反应器中的金属和金属化合物都转化为氧化物形式，熔体在剧烈搅拌下被氧化，熔体保持在1450℃以上，优选在约1500℃ 至少在氧化结束时。 随后，优选通过垃圾焚烧产物和/或铁的部分馏分，优选以废料和/或氢气的形式来减少熔体。 然后可以通过添加的铝和/或钙和/或硅铁继续还原。 如果合适，将金属熔体在反应器的下部分馏，并将渣熔分别作为上清液层收集。 通过热交换和流体再循环可以节省加热能量。