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公开(公告)号：US08048380B2
公开(公告)日：2011-11-01
申请号：US12501022
申请日：2009-07-10
CPC分类号： B01J8/384 , B01J8/0025 , B01J8/1827 , B01J8/1845 , B01J8/1863 , B01J8/1872 , C01B13/324 , C01F7/445 , F23C10/12 , F23C10/14 , Y02P20/129
摘要： A plant for producing metal oxide from metal compounds includes a fluidized-bed reactor in which the metal compounds are heated by a combustion of a fuel to produce metal oxide. The fluidized-bed-reactor reactor includes at least one gas supply tube at least partly surrounded by an annular chamber in which a stationary annular fluidized bed is disposed, and a mixing chamber disposed above an orifice region of the gas supply tube. A gas flowing through the gas supply tube entrains solids from the stationary annular fluidized bed when passing through the orifice region.
摘要翻译： 用于从金属化合物生产金属氧化物的设备包括流化床反应器，其中金属化合物被燃料燃烧而被加热以产生金属氧化物。 流化床反应器包括至少一个气体供应管，其至少部分地被设置有固定环形流化床的环形室环绕，以及设置在气体供应管的孔口区域上方的混合室。 流过气体供应管的气体在穿过孔口区域时夹带固体环形流化床的固体。
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公开(公告)号：US08021601B2
公开(公告)日：2011-09-20
申请号：US12628479
申请日：2009-12-01
申请人： Dirk Nuber , Michael Stroeder , Werner Stockhausen , Lothar Formanek , Martin Hirsch , Ali-Naghi Beyzavi
发明人： Dirk Nuber , Michael Stroeder , Werner Stockhausen , Lothar Formanek , Martin Hirsch , Ali-Naghi Beyzavi
IPC分类号： F27B15/02
CPC分类号： B01J8/1818 , B01J8/1836 , B01J8/26 , B01J2208/00548 , B01J2208/00725 , C21B13/0033 , C22B1/10 , C22B5/14 , C22B34/1204 , C22B34/1209 , F27B15/02 , F27B15/10 , Y02P10/136
摘要： A plant for the heat treatment of solids containing titanium includes a fluidized bed reactor. The reactor includes at least one gas supply tube being at least partly surrounded by an annular chamber in which a stationary annular fluidized bed is located, and a mixing chamber being located above the upper orifice region of the gas supply tube. The gas flowing through the gas supply tube entrains solids from the stationary annular fluidized bed into the mixing chamber when passing through the upper orifice region of the gas supply system. The plant further includes a solids separator downstream of the reactor. The solids separator includes a solids conduit leading to the annular fluidized bed of the reactor.
摘要翻译： 用于热处理含钛固体的设备包括流化床反应器。 反应器包括至少一个气体供应管，其至少部分地被环形室围绕，其中定位有固定环形流化床，并且混合室位于气体供应管的上孔区域上方。 流过气体供应管的气体在通过气体供应系统的上部孔口区域时将固体从固定的环形流化床引入混合室。 该设备还包括在反应器下游的固体分离器。 固体分离器包括通向反应器的环形流化床的固体导管。
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13.发明授权公开(公告)号：US07632334B2
公开(公告)日：2009-12-15
申请号：US10540434
申请日：2003-12-12
申请人： Martin Hirsch , Michael Ströder , Peter Weber
发明人： Martin Hirsch , Michael Ströder , Peter Weber
CPC分类号： B01J8/0055 , B01J8/1827 , B01J8/1872 , B01J2208/00274 , B01J2208/00548 , B01J2219/00006 , C21B13/0033 , C22B5/14 , Y02P10/136
摘要： A method for the heat treatment of solids containing iron oxide, in which fine-grained solids are heated to a temperature of about 630° C. in a fluidized-bed reactor (1). To improve the utilization of energy, it is proposed to introduce a first gas or gas mixture from below through a supply tube (3) into a mixing chamber (7) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (10) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture and of the fluidizing gas for the annular fluidized bet (10) are adjusted such that the Particle-Froude-Numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (10) between 0.02 and 2, and in the mixing chamber (7) between 0.3 and 30.
摘要翻译： 一种用于热处理含有氧化铁的固体的方法，其中在流化床反应器（1）中将细粒固体加热至约630℃的温度。 为了提高能量的利用率，提出从下方将第一气体或气体混合物从供给管（3）引入到反应器（1）的混合室（7）中，气体供给管（3）处于 最少部分地被固定的环形流化床（10）包围，所述静止环形流化床通过供应流化气体而被流化。 第一气体或气体混合物以及用于环形流化床（10）的流化气体的气体速度被调节，使得气体供应管（3）中的粒子 - 弗劳德数在1和100之间，在环形 流化床（10）在0.02和2之间，并且在混合室（7）中在0.3和30之间。
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公开(公告)号：US20090150809A1
公开(公告)日：2009-06-11
申请号：US11951294
申请日：2007-12-05
申请人： Martin Hirsch
发明人： Martin Hirsch
IPC分类号： G06F3/048
CPC分类号： G06F16/954 , G06F16/90324
摘要： The present invention relates to a computer aided method and an apparatus for a comfortable and optimum display of activatable information elements in an interaction window and associated information portions in a result window on a graphics display device. The associated information portions result from a search operation. The activatable information elements are, for example, key words and part of a specific theme or area. The information portions are, for example, abstracts of documents such as scientific publications that relate to the respective key words.
摘要翻译： 本发明涉及一种计算机辅助方法和用于在图形显示装置的结果窗口中的交互窗口和关联信息部分中舒适且最佳地显示可激活信息元素的装置。 相关联的信息部分来自搜索操作。 可激活的信息元素例如是关键词和特定主题或区域的一部分。 信息部分是例如涉及各个关键词的诸如科学出版物的文献的摘要。
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公开(公告)号：US20060263292A1
公开(公告)日：2006-11-23
申请号：US10540071
申请日：2003-12-13
CPC分类号： B01J8/384 , B01J8/0025 , B01J8/1827 , B01J8/1845 , B01J8/1863 , B01J8/1872 , C01B13/324 , C01F7/445 , F23C10/12 , F23C10/14 , Y02P20/129
摘要： The present invention relates to a process for producing metal oxide from metal compounds, in particular metal hydroxide or metal carbonate, in which the metal compound is conveyed into a reactor (25) with fluidized bed, heated there to a temperature of 650 15 to 1150° C. by combustion of fuel, and metal oxide is generated, as well as to a corre-sponding plant. To improve the utilization of energy, it is proposed to introduce a first gas or gas mixture from below through a gas supply tube (26) into a mixing chamber (20) of the reactor (25), the gas supply tube (26) being at least partly surrounded by a stationary annular fluidized bed (27) which is fluidized by supplying fluidizing gas, and 20 to adjust the gas velocities of the first gas or gas mixture and of the fluidizing gas for the annular fluidized bed (27) such that the Particle-Froude numbers in the gas supply tube (26) lie between 1 and 100, in the annular fluidized bed (27) between 0.02 and 2, and in the mixing chamber (20) between 0.3 and 30.
摘要翻译： 本发明涉及一种由金属化合物，特别是金属氢氧化物或金属碳酸盐生产金属氧化物的方法，其中金属化合物被输送到具有流化床的反应器（25）中，加热到650-1510℃的温度 通过燃料燃烧产生金属氧化物，以及相应的工厂。 为了提高能量的利用率，提出从下方将第一气体或气体混合物从气体供给管（26）引入反应器（25）的混合室（20），气体供给管（26）为 至少部分地由通过供应流化气体流化的固定环形流化床（27）和20来调节第一气体或气体混合物和用于环形流化床（27）的流化气体的气体速度，使得 在环形流化床（27）为0.02和2之间，以及在混合室（20）中，0.3至30之间，气体供应管（26）中的粒子 - 弗劳德数位于1和100之间。
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公开(公告)号：US5466278A
公开(公告)日：1995-11-14
申请号：US223833
申请日：1994-04-06
申请人： Paul E. Queneau , Martin Hirsch
发明人： Paul E. Queneau , Martin Hirsch
CPC分类号： C21B13/0026 , Y02P10/122 , Y02P10/126 , Y02P10/136 , Y10S75/957
摘要： The invention describes a process for the manufacture of steel with a carbon content of
摘要翻译： 本发明描述了一种通过还原铁矿石和精炼铁水来制造碳含量<0.8wt％的钢的方法。 将铁矿石和燃料引入到还原区中含有铁熔体的反应器的还原区中。 该熔体被液体渣层覆盖，液体渣从该液体渣层中排出。 此外，含氧气体和燃料一起被吹入包含在还原区域中的铁熔体中。 铁熔体延伸到反应器的精炼区中，渣层从精炼区流入还原区，在精炼区中取出液态钢。 将含氧气体供给到精炼区中所含的铁熔体中，并从其中取出液态铁。
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公开(公告)号：US4676824A
公开(公告)日：1987-06-30
申请号：US761017
申请日：1985-07-31
申请人： Georg Daradimos , Martin Hirsch , Wolfram Schnabel
发明人： Georg Daradimos , Martin Hirsch , Wolfram Schnabel
CPC分类号： F23C10/26 , C21B13/08 , F22B31/003 , F22B31/0084 , F23C10/10 , F23G5/30 , F27B19/04 , F27B7/00 , F27D17/004 , F23C2206/101 , F23G2206/203 , F23G2209/14 , Y02E20/12 , Y02P10/136 , Y02P10/212 , Y02P10/265 , Y02P10/283 , Y02P10/34
摘要： Sponge iron is produced by a direct reduction of iron oxide containing materials in a rotary kiln, the material discharged from the rotary kiln is separated into sponge iron and material which contains surplus carbon, the carbon-containing material is burnt in a fluidized bed reactor containing a circulating fluidized bed, and the heat generated by the combustion is recovered and utilized to produce electric power. To ensure a utilization of the surplus energies of the rotary kiln process and to minimize the contents of SO.sub.2, NO.sub.X, and CaS, the dust-containing exhaust gas from the rotary kiln is supplied to the fluidized bed reactor and is afterburnt therein, at least a major part of all oxygen-containing gases supplied to the fluidized bed reactor is supplied as a fluidizing gas to the lower portion of the fluidized bed reactor, the combustion of the combustible constituents is effected with an over-stoichiometric oxygen content, and the solids entrained by the gases discharged from the fluidized bed reactor are recycled to the fluidized bed reactor in such a manner that the weight of solids circulated per hour is at least 5 times the weight of the solids contained in the fluidized bed reactor.
摘要翻译： 通过在回转窑中直接还原含氧化铁的材料制造海绵铁，将从回转窑排出的材料分离成海绵铁和含有多余碳的材料，含碳材料在含有 循环流化床，并且回收利用燃烧产生的热量来产生电力。 为了确保利用回转窑工艺的剩余能量并使SO2，NOX和CaS的含量最小化，来自回转窑的含尘废气被提供给流化床反应器，并在其中被燃烧至少 供应到流化床反应器的所有含氧气体的主要部分作为流化气体供应到流化床反应器的下部，可燃组分的燃烧以超过化学计量的氧含量进行，并且固体 由流化床反应器排出的气体夹带的循环方式使得每小时循环的固体重量至少为流化床反应器中所含固体重量的5倍。
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公开(公告)号：US4540432A
公开(公告)日：1985-09-10
申请号：US577952
申请日：1984-02-08
申请人： Martin Hirsch , Peter Fischer , Harry Serbent
发明人： Martin Hirsch , Peter Fischer , Harry Serbent
CPC分类号： C21B13/085 , C21B13/0013 , Y02P10/136
摘要： The melting operation is carried out in an elongated horizontal reactor, in which sponge iron is charged onto the molten material in an intermediate region of the reactor, carbonaceous fuel and high-oxygen gases are blown into the molten material and slag and sponge iron are tapped at opposite ends of the reactor. To permit an economical melting of sponge iron having a large particle size range with the aid of virtually only solid carbonaceous fuels, the sponge iron is charged into the reactor in an intermediate region of 20 to 40% of the total length of the reactor, fine-grained carbonaceous fuel and high-oxygen gas are blown into the molten material from below in that region, the rates of oxygen and carbon are so controlled that a molten iron containing 1 to 3% carbon is produced, the remaining carbon contained in the molten material is reacted in the melt to produce CO, and the remaining energy required in the process is produced in that the CO and hydrogen are virtually completely burnt above the molten material as a result of a supply of oxygen-containing gases into the free space of the reactor.
摘要翻译： 熔化操作在细长的水平反应器中进行，其中将海绵铁装入反应器中间区域的熔融材料上，将含碳燃料和高氧气体吹入熔融材料中，并将炉渣和海绵铁轻敲 在反应器的相对端。 为了允许经济地熔化具有大粒度范围的海绵铁，仅借助固体碳质燃料，将海绵铁以反应器总长度的20至40％的中间区域装入反应器中 在该区域从下方将熔融碳质燃料和高氧气从熔融材料吹入熔融材料中，氧气和碳的速率被控制，使得产生含有1至3％碳的铁水，所述熔融物中包含的剩余碳 材料在熔体中反应以产生CO，并且在该过程中所需的剩余能量的产生是由于将CO和氢气实际上完全燃烧在熔融材料上方，这是由于含氧气体供应到熔融材料的自由空间 反应堆。
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19.发明授权Process of producing sponge iron by a direct reduction of iron oxide-containing materials 失效通过直接还原含氧化铁材料生产海绵铁的方法
公开(公告)号：US4443250A
公开(公告)日：1984-04-17
申请号：US417958
申请日：1982-09-14
申请人： Kurt Meyer , Lothar Reh , Martin Hirsch , Wolfram Schnabel , Harry Serbent
发明人： Kurt Meyer , Lothar Reh , Martin Hirsch , Wolfram Schnabel , Harry Serbent
CPC分类号： C21B13/08 , C21B13/146
摘要： Fine-grained material which contains iron oxide is prereduced in a fluidized bed and is subsequently completely reduced in a rotary kiln. In order to avoid agglomeration and incrustation in the rotary kiln, the prereduction is carried out to effect a metallization of 50 to 80%.
摘要翻译： 含有氧化铁的细粒材料在流化床中被还原，随后在回转窑中完全还原。 为了避免回转窑中的团聚和结垢，进行预还原以实现50〜80％的金属化。
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公开(公告)号：US4347064A
公开(公告)日：1982-08-31
申请号：US225952
申请日：1981-01-19
申请人： Lothar Reh , Martin Hirsch , Gerhard Baron , Eberhard Blaum , Carl Hafke
发明人： Lothar Reh , Martin Hirsch , Gerhard Baron , Eberhard Blaum , Carl Hafke
CPC分类号： C10J3/721 , C10J3/54 , C10J3/56 , C10J3/78 , C10J2300/093 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0996 , C10J2300/1823 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , Y02E20/16
摘要： A process of gasifying fine-grained solid fuels for the production of a product gas that contains hydrogen, carbon oxides and methane comprises a treatment with steam, oxygen and/or carbon dioxide in two interconnected gasifying stages under a pressure in the range from 2 to 150 bars and at temperatures of 500.degree. to 1500.degree. C. In the first gasifying stage, the fuel is gasified in a circulating fluidized bed by a treatment with gasifying stage. The residual solids which become available in the first gasifying stage are fed to the second gasifying stage and are virtually completely gasified therein, except for residual ash, by a treatment with a gasifying agent which includes oxygen. At least one-half of the product gas from the second gasifying stage is fed to the first gasifying stage and used as fluidizing fluid therein.
摘要翻译： 气化精细固体燃料以生产含有氢，碳氧化物和甲烷的产物气体的方法包括在两个相互连通的气化阶段中的蒸汽，氧气和/或二氧化碳的处理，压力范围为2至 150巴，500〜1500℃的温度。在第一气化阶段，通过气化阶段的处理，在循环流化床中使燃料气化。 在第一气化阶段中可获得的残留固体通过用包括氧气的气化剂处理而被供给到第二气化阶段并且除了残余灰分之外几乎完全气化。 来自第二气化阶段的至少一半的产物气体被供给到第一气化阶段并用作其中的流化流体。
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