会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Method and device for distributing a lumpy bulk material
    • 用于分配块状散装材料的方法和装置
    • US07513729B2
    • 2009-04-07
    • US11393970
    • 2006-03-30
    • Leopold Werner KepplingerJohann WurmFranz Berner
    • Leopold Werner KepplingerJohann WurmFranz Berner
    • B65G11/00
    • C21B5/008C21B13/002F27B1/20F27D2003/0007
    • The invention relates to an apparatus and a process for distributing a lumpy bulk material, in particular iron ore which has been at least partially prereduced, onto an extensive surface, in particular onto a fixed bed, this surface extending within a reactor or vessel used in physical or chemical process technology, in particular in a reactor used in a metallurgical plant to produce pig iron or primary steel products, and the lumpy bulk material being charged via at least one charging apparatus, which has at least two, in particular rotationally symmetrical, chutes, which are preferably arranged at the same distance from the vertical longitudinal axis of the reactor. In this arrangement, at least a proportion of the bulk material, in particular after it has been introduced into the chute, before it comes into contact with the extensive surface, is distributed in the radial and/or tangential direction—as seen from above—at a scattering device which is assigned to at least one of the chutes and is preferably in the chute.
    • 本发明涉及一种用于将块状块状材料,特别是至少部分预还原的铁矿石分散到广泛的表面上,特别是在固定床上的装置和方法,该表面在用于 特别是在用于冶金设备中用于生产生铁或初级钢产品的反应器中的块状体材料,以及经由至少一个充电装置充填的块状体材料,其至少具有两个,特别是旋转对称的, 斜槽优选地布置在与反应器的垂直纵向轴线相同的距离处。 在这种布置中,散装材料的至少一部分,特别是在与大面积接触之后已被引入滑槽中的部分材料分布在径向和/或切向方向上, 在分配给至少一个滑槽并且优选地在滑槽中的散射装置中。
    • 5. 发明授权
    • Plant and process for the production of pig iron and/or sponge iron
    • 用于生产生铁和/或海绵铁的生产和加工
    • US5989308A
    • 1999-11-23
    • US817263
    • 1997-04-17
    • Leopold-Werner KepplingerKonstantin MilionisDieter SiukaHorst Wiesinger
    • Leopold-Werner KepplingerKonstantin MilionisDieter SiukaHorst Wiesinger
    • C21B11/00C21B13/00C21B13/14C22B5/12
    • C21B13/0033C21B13/002C21B13/14Y02P10/122Y02P10/128Y02P10/136Y02P10/265Y02P10/283
    • A plant for the production of pig iron and/or sponge iron includes a direct-reduction shaft furnace for lumpy iron ore, a melter gasifier, a feed duct for a reducing gas connecting the melter gasifier with the shaft furnace, a conveying duct for the reduction product formed in the shaft furnace connecting the shaft furnace with the melter gasifier, a top-gas discharge duct departing from the shaft furnace, feed ducts for oxygen-containing gases and carbon carriers running into the melter gasifier and a tap for pig iron and slag provided at the melting vessel. In order to be able to process not only lumpy ore, but also fine ore within a wide variation range with regard to quantity in a manner optimized in terms of energy and product, the plant includes at least one fluidized bed reactor for receiving fine ore, a reducing-gas feed duct leading to the fluidized bed reactor, an offgas discharge duct departing from the fluidized bed reactor and a discharge means provided for the reduction product formed in the fluidized bed reactor, wherein the top-gas discharge duct of the shaft furnace and the offgas discharge duct of the fluidized bed reactor run into a purifier and subsequently into a heat exchanger from which the reducing-gas feed duct of the fluidized bed reactor departs.
    • PCT No.PCT / AT95 / 00199 Sec。 371日期1997年04月17日 102(e)日期1997年4月17日PCT提交1995年10月12日PCT公布。 出版物WO96 / 12045 日期1996年04月25日生产生铁和/或海绵铁的工厂包括用于块状铁矿石的直接还原竖炉,熔炉气化器,用于将熔化炉气化器与竖炉连接的还原气体的进料管, 在竖炉中形成的用于还原产品的输送管道,其将竖炉与熔化器气化器连接起来,从立式炉排出的顶部气体排出管道,用于含氧气体的进料管和进入熔化炉气化器的碳载体, 在熔化容器处提供生铁和矿渣的水龙头。 为了能够在能量和产品方面优化的方式处理不仅块状矿石,而且能够处理在数量方面的广泛变化范围内的细矿石,该装置包括至少一个用于接收细矿石的流化床反应器, 通向流化床反应器的还原气进料管道,离开流化床反应器的废气排放管道和为流化床反应器中形成的还原产物提供的排放装置,其中竖炉的顶部排气管道 并且流化床反应器的废气排放管道进入净化器,随后进入热交换器,流化床反应器的还原气体进料管从该换热器排出。
    • 6. 发明授权
    • Process for producing an iron melt
    • 铁熔体的制造方法
    • US5514203A
    • 1996-05-07
    • US419146
    • 1995-04-10
    • Herbert GrunbacherLeopold-Werner KepplingerFranz ReuferGunter Schrey
    • Herbert GrunbacherLeopold-Werner KepplingerFranz ReuferGunter Schrey
    • C04B5/06C21B3/02C21B13/00C21B13/02C21B13/14C21B15/02C22B1/24C22B7/02C21B11/00
    • C21B13/14C22B7/02Y02P10/216Y10S75/961
    • In a process for producing an iron melt, iron ore is reduced to sponge iron in a direct reduction zone. The sponge iron is melted in a meltdown gasifying zone while supplying carbon-containing material under gasification of the carbon-containing material to reducing gas and under formation of a slag. The reducing gas is injected into the direct reduction zone, is reacted there and is drawn off as a top gas. The reducing gas and/or the top gas is subjected to gas scrubbing and the sludges separated during scrubbing are admixed with binder and coal dust and subsequently are agglomerated. In order to be able to supply back to the direct reduction process in large amounts sludges incurring in the direct reduction of iron ore without disturbing the process course of the direct reduction in any way, the sludges separated during scrubbing are dehydrated to a residual moisture content prior to being further treated, coal dust and, as a binder, quick lime are then admixed to the sludges, the sludges subsequently are granulated and the granulate thus formed is supplied to the meltdown gasifying zone while increasing the basicity of the slag to a maximum of 1.25.
    • 在生产铁熔体的方法中,在直接还原区中将铁矿石还原成海绵铁。 海绵铁在熔化气化区熔化,同时在含碳材料气化的同时向还原气体供给含碳材料并形成炉渣。 将还原气体注入到直接还原区中,在其上反应并作为顶部气体排出。 将还原气体和/或顶部气体进行气体洗涤,并且在洗涤期间分离的污泥与粘合剂和煤尘混合并随后凝聚。 为了能够在直接还原铁矿石的同时大量​​回收直接还原工艺,而不会干扰直接还原的过程,洗涤过程中分离的污泥脱水至残留水分含量 在进一步处理之前,将煤灰和作为粘合剂的生石灰混合到淤泥中,随后将污泥造粒,并将由此形成的颗粒供应到熔化气化区,同时将炉渣的碱度提高到最大 的1.25。
    • 9. 发明授权
    • Process and plant for the direct reduction of particulate iron-oxide-containing material
    • 用于直接还原颗粒状氧化铁的材料的工艺和设备
    • US06336954B1
    • 2002-01-08
    • US09505559
    • 2000-02-17
    • Siegfried ZellerKonstantin MilionisJohann ReidetschlägerLeopold Werner KepplingerJohann ZirngastJohannes SchenkRoy Hubert Whipp, Jr.
    • Siegfried ZellerKonstantin MilionisJohann ReidetschlägerLeopold Werner KepplingerJohann ZirngastJohannes SchenkRoy Hubert Whipp, Jr.
    • C21B1300
    • C21B13/0033Y02P10/122Y02P10/128Y02P10/136Y02P10/143
    • 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.
    • 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。