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    • 2. 发明授权
    • Method for simultaneous combined production of electrical energy and
crude iron
    • 同时联合生产电能和粗铁的方法
    • US3985544A
    • 1976-10-12
    • US493614
    • 1974-07-31
    • Per Harald CollinFolke Karl Evald Johansson
    • Per Harald CollinFolke Karl Evald Johansson
    • C21B11/00C21B11/10C21B13/00C21B13/12C21B13/14C21C5/52
    • C21B13/14C21B11/00C21B11/10C21B13/0013C21B13/002C21B13/12C21B13/143Y02P10/136Y02P10/143Y10S75/958
    • The invention relates to a method of combined production of electrical energy and crude iron, comprising reducing iron oxides while keeping the temperature below the melting point of the crude iron during a pre-reduction and above said melting point during a final reduction. The pre-reduction is made by introducing carbonaceous material and the material containing iron oxides into a fluid bed containing solid carbonaceous material, producing reducing gases in the fluid bed by partial combustion of the carbonaceous material with air/or oxygen gas, pre-reducing the iron oxides by said reducing gases until the material has achieved a metallization degree of 30-80 %, most of the heat requirement of the pre-reduction being covered by said combustion. The pre-reduced material is finally reduced and molten by being brought into contact with carbon, and the heat requirement of this final reduction and melting process is covered by electric heating. A substantial part of the exhaust gases from the reduction operations is passed to a thermal power station to generate electrical power therein.
    • 本发明涉及一种组合生产电能和粗铁的方法,包括在预还原过程中将氧化铁还原成低于原铁的熔点,并在最终还原期间高于所述熔点。 通过将碳质材料和含有氧化铁的材料引入含有固体碳质材料的流化床中来进行预还原,通过碳质材料与空气或/或氧气的部分燃烧在流化床中产生还原气体,预还原 通过所述还原气体的氧化铁,直到材料达到30-80%的金属化度,预还原的大部分热量需求被所述燃烧覆盖。 预还原材料最终通过与碳接触而被还原和熔化,并且该最终还原和熔融过程的热需求被电加热覆盖。 来自还原操作的废气的很大一部分被传递到火力发电站以在其中产生电力。
    • 4. 发明授权
    • Method and apparatus for the melt reduction of iron oxides
    • 氧化铁熔融还原的方法和装置
    • US4079185A
    • 1978-03-14
    • US672341
    • 1976-03-31
    • Per Harald Collin
    • Per Harald Collin
    • C21B11/00C21B13/12C21C5/52C22C33/04F27B3/08F27D3/18F27D11/08H05B7/18F27D3/00
    • F27D11/08C21B13/12F27D3/18
    • For the melt reduction of iron oxides, arcs are formed between at least three arcing electrodes in an iron melt, the electrodes being symmetrically positioned about a common vertical axis. The arcs are powered by direct current with the electrodes being cathodic and the melt anodic, and the electrodes are interspaced so closely together that the arcs, due to the direct current powering, converge and form a common focal spot at the electrodes' axis, on the melt, the spot remaining stationary and with any slag on the melt blown away so that the spot is formed by bare metal. Iron oxide material and carbonaceous material, in fine form, is fed downwardly to this spot with the reaction between the oxides and carbon occurring practically immediately.
    • 对于铁氧化物的熔融还原,在铁熔体中的至少三个电弧电极之间形成弧,电极围绕公共垂直轴对称定位。 电弧由直流电流供电,电极为阴极,熔体阳极,并且电极交替紧密地在一起,使得电弧由于直流供电而会聚并在电极的轴线上形成共同的焦斑 熔体,保持静止的位置和熔体上的任何炉渣吹走,使得斑点由裸露的金属形成。 氧化铁材料和微细形式的碳质材料向下送入该点,氧化物和碳之间的反应几乎立即发生。
    • 5. 发明授权
    • Furnace for melting solid ferrous pieces
    • 用于熔炼固体亚铁的炉子
    • US4033562A
    • 1977-07-05
    • US479078
    • 1974-06-13
    • Per Harald Collin
    • Per Harald Collin
    • F27B1/08C21B11/08C21C5/56F27B1/10F27B3/08C21C7/00
    • C21C5/562C21B11/08Y02P10/216Y10S266/90Y10S266/901
    • A furnace for melting solid ferrous pieces such as pig iron and steel scrap, features a combination of electric induction heating and flame heating of the pieces which are charged into the furnace hearth via a charging stack up through which the products of combustion flow from the furnace counter-current to the descending charged pieces moving downwardly through the stack. The flame heating is via burners supplied with hydrocarbon fluid fuel with oxygen proportioned for incomplete combustion, the products of combustion and unburned fuel ascending through the stack and preheating the descending charged pieces. Air is supplied to the stack to complete the combustion of the previously unburned fuel in and around the descending pieces, this being done at a level where the descending pieces have not yet reached temperatures sufficient to cause excessive oxidation of the pieces. Other details providing for effective utilization of these principles, are included in the disclosure.
    • 用于熔炼固体铁片如生铁和废钢的炉子,其特征在于,通过加料产物将炉子产生的燃料从炉子中流出的装料堆放起来,将电感应加热和火焰加热组合成炉底 与下降的带电件逆流通过堆叠向下移动。 火焰加热通过燃烧器供应碳氢化合物流体燃料,氧气成比例用于不完全燃烧,燃烧产物和未燃烧燃料通过堆叠上升并预热下降的带电件。 空气被提供给堆叠,以完成先前未燃烧的燃料在下降件中和周围的燃烧,这在下降部件尚未达到足以引起件的过度氧化的温度下进行。 本公开包括提供有效利用这些原理的其他细节。
    • 7. 发明授权
    • Furnace and method for reducing metal oxides to molten metal
    • 炉和将金属氧化物还原成熔融金属的方法
    • US3947621A
    • 1976-03-30
    • US558177
    • 1975-03-13
    • Per Harald CollinYngve Sundberg
    • Per Harald CollinYngve Sundberg
    • C21B11/00C21B13/00C21B13/10C22B5/10C22B23/02F27B3/08
    • C21B13/002C21B13/105C22B23/02C22B5/10
    • To reduce metal oxides to molten metal, an electrically non-conductive, annular hearth is used, the hearth being radially corrugated to form radial ridges and valleys. A circumferentially continuous coke bed forming a closed electric circuit, is formed on this bed and heated to incandescence by electric current passed through the bed in its circumferential direction, the current being either induced or applied directly. The oxides in particulated form are fed to this bed for reduction to molten metal, the metal collecting in the valleys of the hearth and thereby being prevented from forming a circumferentially continuous melt of higher electrical conductivity than the coke. Particulated coke and oxides can be fed continuously to the bed, the molten metal being then continuously tapped from the valleys of the hearth to thereby prevent the formation of a circumferentially continuous melt.
    • 为了将金属氧化物还原成熔融金属,使用非导电的环形炉床,炉床沿径向瓦楞形成径向脊和谷。 形成闭合电路的周向连续焦炭床形成在该床上,并通过沿其圆周方向通过床的电流加热至白炽,电流被直接引入或施加。 颗粒形式的氧化物被供给到该床以还原成熔融金属,金属收集在炉床的谷中,从而被防止形成比焦炭更高的电导率的周向连续的熔体。 颗粒状焦炭和氧化物可以连续地进料到床上,然后熔融金属从炉床的谷部连续地攻丝,从而防止形成周向连续的熔体。
    • 9. 发明授权
    • Apparatus for and process of converting carbonaceous materials
containing sulphur to an essentially sulphur-free combustible gas
    • 用于将含硫的碳质材料转化为基本上不含硫的可燃气体的装置和方法
    • US4026679A
    • 1977-05-31
    • US664514
    • 1976-03-08
    • Per Harald Collin
    • Per Harald Collin
    • C10J3/54C10J3/20C10K1/20
    • C10J3/54C10J2300/0996C10J2300/1807
    • A process for the conversion of carbonaceous materials containing sulphur to an essentially sulphur-free combustible gas by gasification, comprising partially gasifying the carbonaceous material in a first circulating fluid bed by supplying to said zone adjusted streams of the carbonaceous material, finely-divided CaO-containing material and steam, separating solid materials from streams of gases and solid materials leaving said reaction zone, subjecting an adjusted fraction stream of said solid materials to separation of ashes and sulphur purification and then returning this stream to the reaction zone, transferring the rest of the solid materials to a second circulating fluid bed, wherein the solid materials by partial combustion with an adjusted stream of gases containing molecular oxygen is heated to an overtemperature which is adjusted by controlling the content of oxygen of the gas in such a way that the materials after separation from the reaction gases and recirculation to the first fluid bed satisfies the heat requirement for the gasification therein. The invention also covers an apparatus for carrying out said process.
    • 一种通过气化将含硫的碳质材料转化成基本上不含硫的可燃气体的方法,包括通过向所述区域供应调节的碳质材料的流,将第一循环流化床中的含碳材料部分气化,将细碎的CaO- 将固体物质与离开所述反应区的气体和固体物质分离出来,使所述固体物质的调整的馏分物流分离灰分和硫的纯化,然后将该物流返回到反应区,将其余的 将固体材料输送到第二循环流化床,其中通过用调节的含有分子氧气流的部分燃烧将固体材料加热到过热,该温度通过控制气体的氧含量来调节,使得材料 在与反应气体分离后再循环 第一流化床满足其中气化的热需求。 本发明还包括用于执行所述过程的装置。