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    • 3. 发明授权
    • Burner arrangement for the combustion of fine-grained to dusty solid fuel
    • 燃烧器配置精细颗粒燃烧固体燃料
    • US5127346A
    • 1992-07-07
    • US776632
    • 1991-10-15
    • Leopold-Werner KepplingerWilhelm SchifferRolf Hauk
    • Leopold-Werner KepplingerWilhelm SchifferRolf Hauk
    • C10J3/48C21B5/00F23D1/00
    • C21B5/001C10J3/506F23D1/00C10J2200/152C10J2300/1223F23D2214/00Y02P10/122
    • A burner for the combustion of fine-grained to dusty solid fuels incorporates a central internal tube for supplying the solid fuels and an annular gap surrounding the internal tube and delimited by a cooled external tube, for supplying oxygen or oxygen-containing gas. The annular gap ends externally by an exhaust port directed obliquely relative to the longitudinal axis of the burner and peripherally surrounding the end of the central internal tube, or by a plurality of exhaust ports annularly disposed about the longitudinal axis of the burner. In order to ensure the complete combustion of the fine-grained to dusty fuels at a long service life of the burner, the inclination of the exhaust port(s) relative to the longitudinal axis of the burner is below 20.degree.. The exhaust port(s) is/are arranged transverse to the longitudinal axis of the burner and in the radial direction relative to the same at a distance of between 5 and 30 mm from the inner wall of the internal tube. The inclination of the exhaust port(s) relative to the longitudinal axis of the burner and the radial distance of the exhaust port(s) relative to the inner wall of the central internal tube are coordinated in a manner that the intersection of the extensions of the exhaust port and of the inner wall of the internal tube outside of the burner lies 20 to 80 mm in front of the burner mouth.
    • 用于燃烧细颗粒到多尘的固体燃料的燃烧器包括用于供应固体燃料的中心内管和围绕内管的环形间隙并由冷却的外管限定,用于供应氧气或含氧气体。 环形间隙通过相对于燃烧器的纵向轴线倾斜地指向并围绕中心内管的端部或围绕燃烧器的纵向轴线环形设置的多个排气口的外部终止。 为了确保在燃烧器使用寿命长的细颗粒燃料中完全燃烧,排气口相对于燃烧器纵轴的倾角低于20度。 排气口横向于燃烧器的纵向轴线并且相对于排气口在与内管的内壁5至30mm的距离处相对于其径向设置。 排气口相对于燃烧器的纵向轴线的倾斜度和排气口相对于中心内管的内壁的径向距离是以这样一种方式协调的, 燃烧器外面的内部排气口和内壁的内壁在燃烧口前面20至80mm。
    • 4. 发明授权
    • Method of producing molten pig iron or steel pre-products from
particulate ferrous material
    • 从颗粒状黑色金属材料生产熔融生铁或钢制前产品的方法
    • US4708736A
    • 1987-11-24
    • US838669
    • 1986-03-12
    • Rolf HaukWerner Kepplinger
    • Rolf HaukWerner Kepplinger
    • C21B11/02C21B13/00C21B11/00
    • C21B13/002
    • In a method of producing molten pig iron or steel pre-products from particulate ferrous material, as well as of producing reduction gas in a melt-down gasifier by adding coal and by blowing in oxygen-containing gas by means of nozzle pipes penetrating the wall of the melt-down gasifier, a fixed bed formed of coke particles, through which the oxygen-containing gas flows and a superposed fluidized bed of coke particles are formed, and the ferrous material is charged onto the fluidized bed. Below the fixed bed through which oxygen-containing gas flows, a fixed bed of coke particles not passed through by gas is provided, and the fluidized bed above the fixed bed passed through by oxygen-containing gas is passed through by a gas free from oxygen or having a low oxygen content.
    • 在从含铁材料颗粒生产熔融生铁或钢预制品的方法中,以及通过加入煤和通过穿透壁的喷嘴管吹入含氧气体在熔化气化器中生产还原气体的方法 的熔融气化器,由焦炭颗粒形成的固定床,含氧气体通过该固定床和重叠的焦炭颗粒流化床,并将铁质材料装入流化床中。 在含有气体的固定床下面,设置不被气体通过的固定床的焦炭颗粒,并且通过含氧气体通过的固定床上方的流化床通过不含氧气体的气体 或具有低氧含量。
    • 7. 发明授权
    • Method for producing molten pig iron or steel pre-products in a
melt-down gasifier
    • 在熔融气化炉中生产生铁或钢制前产品的方法
    • US4588437A
    • 1986-05-13
    • US563359
    • 1983-12-20
    • Werner KepplingerRolf Hauk
    • Werner KepplingerRolf Hauk
    • C21B11/02C21B13/00C21B13/02C21B11/08
    • C21B13/002Y02P10/136
    • There is disclosed a method and a melt-down gasifier for producing molten pig iron or steel pre-products and reduction gas. A first fluidized-bed zone is formed by coke particles, with a heavy motion of the particles, above a first blow-in plane by the addition of coal and by blowing in oxygen-containing gas. Iron sponge particles and/or pre-reduced iron ore particles with a substantial portion of particle sizes of more than 3 mm are added to the first fluidized-bed zone from above. A melt-down gasifier for carrying out the method is formed by a refractorily lined vessel having openings for the addition of coal and ferrous material, openings for the emergence of the reduction gases produced, and openings for tapping the metal melt and the slag. Pipes or nozzles enter into the meltdown gasifier above the slag level at at least two different heights.
    • 公开了一种用于生产熔融生铁或钢预制品和还原气体的方法和熔化气化器。 第一流化床区由焦炭颗粒形成,颗粒的重运动通过加入煤和吹入含氧气体在第一吹入平面之上。 将大部分粒径大于3mm的铁海绵颗粒和/或预还原的铁矿石颗粒从上方加入到第一流化床区。 用于实施该方法的熔化气化器由具有用于添加煤和铁质材料的开口的耐火衬里容器形成,用于产生的还原气体的出口的开口,以及用于挖掘金属熔体和炉渣的开口。 管道或喷嘴在至少两个不同高度的炉渣水平面上进入熔化炉中。
    • 9. 发明授权
    • Process for the production of pig iron using cyclone
    • 使用旋风式生产生铁的工艺
    • US4851039A
    • 1989-07-25
    • US188715
    • 1988-04-29
    • Gero PapstRolf Hauk
    • Gero PapstRolf Hauk
    • C21B11/08C21B11/00C21B13/14
    • C21B11/00C21B13/14Y02P10/122Y02P10/128
    • A process for the production of pig iron from fine ore is described, in which initially the fine ore undergoes prereduction to a degree of metallization of preferably 65 to 75%. The sponge iron obtained is then melted down and under goes a final reduction. This process takes place in a melting cyclone 2, to which the sponge iron is supplied by means of a central opening 1 and into which are tangetially blown via a lateral opening 3 a carbon carrier, an oxygen-containing gas and optionally fluxes. As a result of the angular momentum produced, the sponge iron particles are deflected to the side and melted and finally reduced by the combustion gases of the carbon carrier. The molten iron collects in an iron bath 8. The gas produced in the melting cyclone is cooled from approximately 1500.degree. C. to approximately 800.degree. C. in a waste heat system 10, as well as by admixing cooling gas supplied via a line 11 and is then used for the prereduction of the iron ore.
    • 描述了从细矿石生产生铁的方法,其中最初将细矿石预先还原至优选65至75%的金属化程度。 然后将获得的海绵铁熔化,并进行最终还原。 该过程在熔融旋流器2中进行,海绵铁通过中心开口1供应到其中,通过侧向开口3,碳载体,含氧气体和任选的助熔剂对其进行正向吹送。 作为产生角动量的结果,海绵铁颗粒被偏转到侧面并且被碳载体的燃烧气体熔化并最终减少。 铁水在铁浴槽8中收集。在废热系统10中,将熔融旋流器中产生的气体从大约1500℃冷却至约800℃,以及通过混合通过管线11供应的冷却气体 然后用于铁矿石的预还原。