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1. 发明授权

US5858058A Process and plant for avoiding metal dusting in the direct reduction of iron-oxide-containing materials 失效
标题翻译：用于避免金属粉尘直接还原含氧化铁材料的工艺和设备
公开(公告)号：US5858058A
公开(公告)日：1999-01-12
申请号：US765331
申请日：1997-01-15
申请人： Gerald Kern , Werner Leopold Kepplinger , Johannes Schenk , Roy Hubert Whipp, Jr.
发明人： Gerald Kern , Werner Leopold Kepplinger , Johannes Schenk , Roy Hubert Whipp, Jr.
IPC分类号： C21B13/00 , F27B15/10 , F27D17/00
CPC分类号： C21B13/0073 , Y02P10/122 , Y02P10/136 , Y02P10/143
摘要： A direct reduction process is disclosed for iron-oxide-containing materials. Synthesis gas is mixed with top gas produced during direct reduction of the iron-oxide-containing materials and is used as reduction gas for directly reducing iron-oxide-containing materials. In order to avoid or reduce metal dusting caused by an increased CO content of the reduction gas with a simple technique and equipment, the CO/CO.sub.2 ratio of the reduction gas is set at a predetermined value from 1 to 3.
摘要翻译： PCT No.PCT / AT95 / 00123 Sec。 371日期1997年1月15日 102（e）日期1997年1月15日PCT提交1995年6月20日PCT公布。出版物WO96 / 00304 PCT 日期1996年1月4日公开了含氧化铁材料的直接还原方法。将合成气与直接还原含铁氧化物的材料中产生的顶部气体混合，并用作直接还原含氧化铁材料的还原气体。为了通过简单的技术和设备避免或减少由还原气体的CO含量增加引起的金属粉尘，将还原气体的CO / CO 2比设定在1至3的预定值。

2. 发明授权

US06569377B2 Plant for the direct reduction of particulate iron-oxide-containing material 有权
公开(公告)号：US06569377B2
公开(公告)日：2003-05-27
申请号：US10045061
申请日：2002-01-15
申请人： Siegfried Zeller , Konstantin Milionis , Johann Reidetschläger , Leopold Werner Kepplinger , Johann Zirngast , Johannes Schenk , Roy Hubert Whipp, Jr.
发明人： Siegfried Zeller , Konstantin Milionis , Johann Reidetschläger , Leopold Werner Kepplinger , Johann Zirngast , Johannes Schenk , Roy Hubert Whipp, Jr.
IPC分类号： C21B1300
CPC分类号： C21B13/0033 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P10/143
摘要： In a process for the direct reduction of particulate iron-oxide-containing material by fluidization, a synthesis gas is introduced as a reducing gas into several fluidized bed zones consecutively arranged in series. The reducing gas is conducted from one fluidized bed zone to another fluidized bed zone in counterflow to a flow of particulate iron-oxide containing material through the fluidized bed zones. In order to reduce operating costs and, in particular, the energy demand, various process parameters are varied according to the temperature of the iron-oxide-containing material in the first fluidized bed zone being adjusted to be below 400° C. (and, preferably, below 350° C.), above 580° C. (and preferably about 650° C.), or to a temperature within the range of from 400° C. to 580° C. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is maintained to be below 400° C., the temperature of the iron-oxide-containing material in the following fluidized bed zone is passed through the temperature range between 400° C. and 580° C. within a period of 10 minutes and, preferably, within 5 minutes. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is adjusted to a temperature above 580° C., the temperature range of between 400° C. and 580° C. in the first fluidized bed zone is passed through within a maximum period of time of 10 minutes and, preferably, 5 minutes. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is adjusted to be within the range of from 400° C. to 580° C., the iron-oxide-containing material remains in the first fluidized bed zone within that temperature range for a maximum of 10 minutes and, preferably, 5 minutes, and the material is then passed on into the following fluidized bed zone immediately after having reached the desired temperature.

3. 发明授权

US06336954B1 Process and plant for the direct reduction of particulate iron-oxide-containing material 有权
标题翻译：用于直接还原颗粒状氧化铁的材料的工艺和设备
公开(公告)号：US06336954B1
公开(公告)日：2002-01-08
申请号：US09505559
申请日：2000-02-17
申请人： Siegfried Zeller , Konstantin Milionis , Johann Reidetschläger , Leopold Werner Kepplinger , Johann Zirngast , Johannes Schenk , Roy Hubert Whipp, Jr.
发明人： Siegfried Zeller , Konstantin Milionis , Johann Reidetschläger , Leopold Werner Kepplinger , Johann Zirngast , Johannes Schenk , Roy Hubert Whipp, Jr.
IPC分类号： C21B1300
CPC分类号： C21B13/0033 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P10/143
摘要： A process for the direct reduction of particulate iron-oxide-containing material by fluidization. A synthesis gas is introduced as a reducing gas into several fluidized bed zones consecutively arranged in series for the reducing gas. The reducing gas is conducted from one fluidized bed zone to another fluidized bed zone in counterflow to the particulate iron-oxide containing material. In order to reduce operating costs and, in particular, the energy demand, the temperature of the iron-oxide-containing material is adjusted in the first fluidized bed zone to be either below 400° C. (and, preferably, below 350° C.), or above 580° C. (and preferably about 650° C.), or to a temperature ranging from 400° C. to 580° C. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is adjusted to be below 400° C., the temperature range in the following fluidized bed zone between 400° C. and 580° C. is passed through within a period of 10 minutes and, preferably, within 5 minutes. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is adjusted to be above 580° C., the temperature range in the first fluidized bed zone between 400° C. and 580° C. is passed through within a period of time of maximally 10 minutes and, preferably, 5 minutes. If the temperature of the iron-oxide-containing material in the first fluidized bed zone is adjusted to be in the range of from 400° C. to 580° C., the iron-oxide-containing material remains within that temperature range for a maximum of 10 minutes and, preferably, 5 minutes, and the material is passed on into the following fluidized bed zone immediately after having reached the desired temperature.
摘要翻译：一种通过流化直接还原含氧化铁颗粒物质的方法。将合成气作为还原气体引入连续排列为还原气体的多个流化床区域。还原气体从一个流化床区域传导到另一个流化床区域，与含铁氧化物颗粒材料相反。为了降低运行成本，特别是能量需求，将含铁氧化物的材料的温度在第一流化床区域调节至低于400℃（优选低于350℃）），或高于580℃（优选约650℃），或达到400℃至580℃的温度。如果第一流化床中含氧化铁的材料的温度将区域调节至低于400℃，在下述流化床区域中在400℃至580℃之间的温度范围在10分钟内优选在5分钟内通过。如果将第一流化床区域中含氧化铁的材料的温度调节至高于580℃，则在400℃至580℃之间的第一流化床区域内的温度范围通过时间最长为10分钟，最好为5分钟。如果将第一流化床区域中含氧化铁的材料的温度调节至400℃至580℃的范围内，则含铁氧化物的材料保持在该温度范围内最多10分钟，优选5分钟，并且在达到所需温度之后立即将材料通入下一流化床区。

4. 发明授权

US5873926A Process for reducing oxide-containing material and plant for carrying out the process 失效
标题翻译：用于还原含氧化物材料和工厂进行该工艺的方法
公开(公告)号：US5873926A
公开(公告)日：1999-02-23
申请号：US809341
申请日：1997-03-12
申请人： Leopold Werner Kepplinger , Siegfried Zeller , Karl-Heinz Zimmerbauer , Roy Hubert Whipp, Jr.
发明人： Leopold Werner Kepplinger , Siegfried Zeller , Karl-Heinz Zimmerbauer , Roy Hubert Whipp, Jr.
IPC分类号： C22B5/12 , C21B13/00 , C21B13/14 , C22B5/14 , C22B1/10
CPC分类号： C21B13/14 , C21B13/0033 , C22B5/14 , Y02P10/122 , Y02P10/136
摘要： In a process for reducing particulate oxide-containing material using the whirl bed method, the oxide-containing material, by means of reducing gas flowing from bottom to top, is maintained in the whirl layer, thus being reduced. In order to avoid or considerably reduce operational interruptions of the reduction process caused by sticking or fouling, the clear tube speed (superficial velocity) of the reducing gas, exclusively above the whirl layer, is continuously lowered along the total free height of a space above the whirl layer while the formation of further whirl formations is avoided.
摘要翻译： PCT No.PCT / AT95 / 00180 Sec。 371日期1997年3月12日 102（e）1997年3月12日PCT PCT 1995年9月14日PCT公布。 WO96 / 10094 PCT公开号日期1996年4月4日在使用旋转方法还原含氧化物的材料的方法中，含氧化物的材料通过从底部向顶部流动的还原气体保持在旋转层中，从而减少。为了避免或大大减少由于粘结或结垢引起的还原过程的操作中断，除了旋转层之上的还原气体的透明管速度（表面速度）沿上述空间的总自由高度连续降低避免了涡旋层的形成。

5. 发明授权

US5833734A Process for the direct reduction of particulate iron-containing material and a plant for carrying out the process 失效
标题翻译：用于直接还原含微粒铁的材料和用于进行该方法的设备的方法
公开(公告)号：US5833734A
公开(公告)日：1998-11-10
申请号：US849838
申请日：1997-07-24
申请人： Gerhard Cip , Gottfried Rossmann , Konstantin Milionis , Roy Hubert Whipp, Jr.
发明人： Gerhard Cip , Gottfried Rossmann , Konstantin Milionis , Roy Hubert Whipp, Jr.
IPC分类号： C21B13/00 , C22B5/14
CPC分类号： C21B13/0033 , Y02P10/122 , Y02P10/126 , Y02P10/128 , Y02P10/136 , Y02P10/143
摘要： With a process for the direct reduction of particulate iron-containing material by fluidization, reformed gas, at least partially freed from CO.sub.2, is supplied to a fluidized-bed reduction zone as a reducing gas and is carried off from the same as a top gas and at least a portion of the top gas together with reformed gas is utilized for direction reduction. To economize on parts of the plant that are impinged on by reducing gas and in order to achieve savings in terms of heating costs, CH.sub.4 and N.sub.2 are, in addition to CO.sub.2, at least partially removed by adsorption, from 50 to 100% of the reformed as and 0 to 100% of the top gas, and the tail gas removed from the reformed gas and/or the top gas by adsorption is utilized as a heating gas.
摘要翻译： PCT No.PCT / AT96 / 00190 Sec。 371日期1997年7月24日 102（e）1997年7月24日PCT PCT 1996年10月8日PCT公布。公开号WO97 / 13879 日期1997年04月17日为了通过流化直接还原颗粒状含铁材料的方法，至少部分从CO 2中除去的重整气体作为还原气体被供给到流化床还原区，并从与顶部气体相同，并且顶部气体的至少一部分与重整气体一起用于方向减少。为了节省通过减少气体冲击的工厂的部分，为了节约加热成本，CH4和N2除CO2之外至少部分通过吸附除去，从50％到100％的重整为顶部气体的0〜100％，通过吸附从重整气体和/或顶部气体除去的尾气被用作加热气体。

6. 发明授权

US5871560A Process and plant for the direct reduction of iron-oxide-containing materials 失效
标题翻译：用于直接还原含氧化铁材料的工艺和设备
公开(公告)号：US5871560A
公开(公告)日：1999-02-16
申请号：US765342
申请日：1997-01-15
申请人： Roland Fluch , Karl Czermak , Gunter Peer , Roy Hubert Whipp, Jr.
发明人： Roland Fluch , Karl Czermak , Gunter Peer , Roy Hubert Whipp, Jr.
IPC分类号： C21B13/00
CPC分类号： C21B13/0073 , Y02P10/122 , Y02P10/128 , Y02P10/136 , Y02P10/143
摘要： A direct reduction process is disclosed for iron oxide-containing materials. Synthesis gas is mixed with top gas produced during direct reduction of the iron oxide-containing materials and is used as reduction gas for directly reducing and heating the iron oxide-containing materials up to reduction temperature. In order to set the H.sub.2 S content at a predetermined value by a relatively simple technique and with a relatively simple equipment, at least part of the sulphur contained in the iron oxide-containing materials as H.sub.2 S produced during heating or direct reduction is added to the reduction gas together with the top gas.
摘要翻译： PCT No.PCT / AT95 / 00121 Sec。 371日期1997年1月15日 102（e）日期1997年1月15日PCT提交1995年6月20日PCT公布。公开号WO96 / 00302 日期1996年1月4日公开了含氧化铁材料的直接还原工艺。将合成气与直接还原含氧化铁材料时产生的顶部气体混合，并用作直接还原和加热含氧化铁材料直到还原温度的还原气体。为了通过相对简单的技术将H2S含量设定在预定值，并且使用相对简单的设备，在加热或直接还原期间产生的含氧化铁的材料中所含的硫的至少一部分被加入还原气体与顶部气体一起。

7. 发明授权

US5676734A Method of treating fine ore 失效
标题翻译：处理细矿的方法
公开(公告)号：US5676734A
公开(公告)日：1997-10-14
申请号：US408485
申请日：1995-03-22
申请人： Ernst Oberndorfer , Gero Tessmer , Rudolf Weidinger , Roy Hubert Whipp, Jr.
发明人： Ernst Oberndorfer , Gero Tessmer , Rudolf Weidinger , Roy Hubert Whipp, Jr.
IPC分类号： F26B17/10 , B03B4/02 , C21B13/00 , C21B13/10 , C22B1/00 , C22B1/10 , F26B3/08 , F26B25/00 , F27B15/00
CPC分类号： B03B4/02 , C21B13/00 , C22B1/00 , C22B1/10 , F26B25/007 , F26B3/08 , Y02P10/143 , Y10S75/961
摘要： In a process for treating fine ore, the fine ore is dried by aid of a hot drying gas flowing around the ore particles of the fine ore, the drying gas, after having flown around the ore particles, is purified while releasing entrained dust ore particles and the dust ore particles are collected and admixed to the dried fine ore. In order to avoid process disturbances in the further processing of fine ore due to excessive portions of dust ore particles present within the fine ore, drying is effected in the whirl-bed, i.e., fluidized-bed method under simultaneous wind-screening of the fine ore, wherein the drying gas is passed through the fine ore under formation of a whirl bed and the speed of the drying gas is fixed at a rate at which entraining of dust ore particles having dimensions below a predetermined dimension is effected, and that the dust ore particles entrained by the drying gas are separated, collected and admixed to the dried fine ore in dosed amounts.
摘要翻译：在处理细矿石的过程中，细矿石通过在细矿石矿石颗粒周围流动的热干燥气体而干燥，干燥气体在矿石颗粒周围流动之后被净化，同时释放夹带的灰尘颗粒并将粉尘矿石颗粒收集并混合到干燥的细矿石上。为了避免由于细矿石中存在的粉尘矿石颗粒过多而进一步处理细矿石的过程紊乱，在旋转床中进行干燥，即流化床法同时风筛精细矿石，其中干燥气体在涡旋床形成下通过细矿石，并且干燥气体的速度以固定在尺寸低于预定尺寸的粉尘矿石颗粒的速度被固定，并且灰尘由干燥气体夹带的矿石颗粒被分离，收集并以剂量混合到干燥的细矿石中。

8. 发明授权

US6143053A Process for producing sponge iron by direct reduction of iron-oxide-containing material 失效
标题翻译：通过直接还原含铁氧化物材料生产海绵铁的方法
公开(公告)号：US6143053A
公开(公告)日：2000-11-07
申请号：US101292
申请日：1998-09-30
申请人： Johann Reidetschlager , Siegfried Zeller , Felix Wallner , Roy Hubert Whipp, Jr.
发明人： Johann Reidetschlager , Siegfried Zeller , Felix Wallner , Roy Hubert Whipp, Jr.
IPC分类号： C21B13/00 , C21B13/14
CPC分类号： C21B13/0073 , C21B13/0033 , C21B13/146 , Y02P10/122 , Y02P10/136 , Y02P10/143
摘要： In a process for producing sponge iron by direct reduction of iron-oxide-containing material, synthesis gas is mixed with top gas forming in the direct reduction of the iron-oxide-containing material and is utilized as a CO- and H.sub.2 -containing reducing gas for direct reduction and for heating the iron-oxide-containing material to a reduction temperature. To be able to save energy in an economically efficient manner when producing steel, especially in the refining process, direct reduction is carried out as follows: (1) in addition to the reducing gas, a carbon-containing gas, such as natural gas, or a gas having higher hydrocarbons is utilized for reduction; (2) the iron-oxide-containing material for a predetermined period of time exceeding the period necessary for complete reduction is exposed to the reducing gas and to the additionally supplied carbon-containing gas, and (3) a CO/CO.sub.2 ratio ranging between 2 and 5, preferably a ratio in excess of 2.5, is adjusted in the reducing gas.
摘要翻译： PCT No.PCT / AT97 / 00236 Sec。 371日期：1998年9月30日 102（e）1998年9月30日PCT PCT 1997年11月5日PCT公布。公开号WO98 / 20171 日期1998年5月14日在通过直接还原含氧化铁材料生产海绵铁的方法中，合成气与直接还原含氧化铁材料混合形成顶部气体，并用作CO-和含H2的还原气体用于直接还原，并将含铁氧化物的材料加热至还原温度。为了在生产钢时能够以经济有效的方式节约能源，特别是在精炼过程中，直接还原如下：（1）除了还原气体之外，还可以使用天然气等含碳气体，或具有较高烃的气体用于还原; （2）超过完全还原所需时间的预定时间段的含铁氧化物的材料暴露于还原气体和附加供给的含碳气体中，（3）CO / CO 2比范围在在还原气体中调节2和5，优选超过2.5的比例。

9. 发明授权

US6048381A Method and arrangement for cooling hot bulk material 失效
标题翻译：冷却散装材料的方法和布置
公开(公告)号：US6048381A
公开(公告)日：2000-04-11
申请号：US875303
申请日：1997-10-15
申请人： Leopold Werner Kepplinger , Gerhard Cip , Anton Himmel , Karl-Heinz Zimmerbauer , Roland Sachsenhofer , Roy Hubert Whipp, Jr.
发明人： Leopold Werner Kepplinger , Gerhard Cip , Anton Himmel , Karl-Heinz Zimmerbauer , Roland Sachsenhofer , Roy Hubert Whipp, Jr.
IPC分类号： C22B1/26 , C21B13/00
CPC分类号： C21B13/0086
摘要： In order to attain as low a final temperature as possible after as short a period of time as possible in a method of cooling hot briquetted sponge iron (3) under optimum utilization of the cooling medium, the hot briquetted sponge iron (3), in a first cooling step (11), is passed exclusively by a gaseous cooling medium while being gently cooled and subsequently, in a second cooling step (14), is sprayed with a liquid cooling medium, thus being intensively cooled to the final temperature desired.
摘要翻译： PCT No.PCT / AT96 / 00008 Sec。 371日期：1997年10月15日 102（e）日期1997年10月15日PCT 1996年1月22日PCT PCT。公开号WO96 / 23081 日期1996年8月1日为了在最佳利用冷却介质的情况下，在热压球铁（3）的冷却方法中尽可能短的一段时间后尽可能低的最终温度，热压块海绵铁（3）在第一冷却步骤（11）中，仅通过气态冷却介质通过轻轻冷却，随后在第二冷却步骤（14）中喷射液体冷却介质，从而被强制冷却至所需的最终温度。

10. 发明授权

US5879618A Apparatus for treating fine ore 失效
标题翻译：用于处理细矿石的设备
公开(公告)号：US5879618A
公开(公告)日：1999-03-09
申请号：US948884
申请日：1997-10-10
申请人： Ernst Oberndorfer , Gero Tessmer , Rudolf Weidinger , Roy Hubert Whipp, Jr.
发明人： Ernst Oberndorfer , Gero Tessmer , Rudolf Weidinger , Roy Hubert Whipp, Jr.
IPC分类号： F26B17/10 , B03B4/02 , C21B13/00 , C21B13/10 , C22B1/00 , C22B1/10 , F26B3/08 , F26B25/00 , F27B15/00
CPC分类号： B03B4/02 , C21B13/00 , C22B1/00 , C22B1/10 , F26B25/007 , F26B3/08 , Y02P10/143 , Y10S75/961
摘要： An apparatus for treating fine ore in which fine ore is dried by aid of a hot drying gas flowing around the ore particles. After having flown around the ore particles, the drying gas is purified while releasing entrained dust ore particles. The dust ore particles are collected and admixed to the dried fine ore. In order to avoid process disturbances in the further processing of fine ore due to excessive portions of dust ore particles present without the fine ore, drying is effected in the whirl-bed method under simultaneous wind-screening of the fine ore. The drying gas is passed through the fine ore under formation of a whirl bed and the speed of the drying gas is fixed at a rate at which entraining of dust ore particles having dimensions below a predetermined dimension is effected. The dust ore particles entrained in the drying gas are separated, collected and admixed to the dried fine ore in dosed amounts. The apparatus includes a fine ore whirl-bed drying means including a drying-gas feeding means. A drying-gas purification means receives the hot drying gas from the whirl-bed drying means. A separating means separates from the hot drying gas dust ore particles entrained by the drying gas. A first collecting vessel receives the dust ore particles separated from the hot drying gas. A mixing means mixes the dried fine ore and the dust ore particles separated from the drying gas to a predetermined quantitative ratio.
摘要翻译：一种用于处理细矿石的装置，其中通过在矿石颗粒周围流动的热干燥气体干燥细矿石。在矿石颗粒周围流动之后，干燥气体被净化，同时释放夹带的灰尘颗粒。粉尘矿石颗粒被收集并混合到干燥的细矿石上。为了避免细粒矿进一步处理过程中的干扰，由于过多的灰尘矿颗粒不存在细矿石，因此在旋转床方式下，在细矿石的同时风筛下进行干燥。干燥气体通过旋转床形成的细矿石，并且干燥气体的速度以固定在尺寸低于预定尺寸的粉尘矿石颗粒的速度被固定。夹带在干燥气体中的灰尘颗粒被分离，收集并以经过量的量混合到干燥的细矿石中。该设备包括一个包括干燥气体供给装置的细矿石旋转干燥装置。干燥气体净化装置从旋转干燥装置接收热干燥气体。分离装置与干燥气体夹带的热干燥气体灰尘颗粒分离。第一收集容器接收与热干燥气体分离的灰尘颗粒。混合装置将干燥的细矿石和从干燥气体分离的粉尘矿颗粒混合至预定的定量比例。

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