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    • 4. 发明授权
    • Vacuum refining furnace
    • 真空精炼炉
    • US6162387A
    • 2000-12-19
    • US219
    • 1998-09-18
    • Kensuke ShimomuraTadashi ImotoMayumi OkimoriGaku OgawaTomoaki Tanaka
    • Kensuke ShimomuraTadashi ImotoMayumi OkimoriGaku OgawaTomoaki Tanaka
    • C21C5/28C21C7/10C22B9/04
    • C21C7/10C21C5/28C22B9/04Y10S266/903
    • A refining furnace used for vacuum refining has a sealing cover mounted on the refining furnace so as to cover the furnace throat of the refining furnace and to be in close contact with a sealing flange (10) formed on the refining furnace. The adhesion of metal and slag to the sealing flange is prevented without using any flange cover. A sealing flange (10) is formed on the outer surface of the refining furnace (1) at a position on a conical part (8) extending between the furnace throat (9) and a straight body part or on the straight body part. A slag-stopping dummy flange (11) is formed on the outer surface of the refining furnace (1) at a position between a furnace throat (9) and the sealing flange (10). The slag-stopping dummy flange (11) has an outer circumference lying on the inner side of the inner circumference of a sealing cover (4) and on the outer side of the inner circumference of a lower end part of a dust collecting hood for atmospheric refining.
    • PCT No.PCT / JP98 / 00821 Sec。 371日期:1998年9月18日 102(e)1998年9月18日PCT 1998年2月27日提交PCT用于真空精炼的精炼炉具有安装在精炼炉上的密封盖,以覆盖精炼炉的炉喉,并与 形成在精炼炉上的密封凸缘(10)。 在不使用任何法兰盖的情况下,可以防止金属和炉渣对密封法兰的粘附。 密封凸缘(10)在精炼炉(1)的外表面上形成在在炉喉(9)和直体部分之间或直体部分上延伸的锥形部分(8)上的位置处。 在炉膛(9)和密封凸缘(10)之间的位置,在精炼炉(1)的外表面上形成止渣假模法兰(11)。 防渣假凸缘(11)具有位于密封盖(4)的内周的内侧的外周和大气的集尘罩的下端部的内周的外侧 精制。
    • 6. 发明授权
    • Blast furnace with narrowed top section and method of using
    • US6030430A
    • 2000-02-29
    • US122086
    • 1998-07-24
    • H. Bruce ClaflinJohn Jasbinsek
    • H. Bruce ClaflinJohn Jasbinsek
    • F23G5/00C10G1/00C10J3/00C10J3/02C10J3/16C10J3/20C21B5/00C21B7/00C21B7/16C21C5/28C21C5/30C21C5/36C21C5/40C22B7/02C21B5/06
    • C21B5/008C21B5/00C21B5/001C21B7/00Y02E20/12Y02P10/212Y02P10/34Y10S75/958
    • Described herein is an Improved Converter System designed to help reduce air, land and water pollution by completely converting materials that presently cause pollution into clean burning fuels and a host of other products beneficial to mankind. The primary conversion unit in the system is a zone controlled multipurpose slagging-ash oxygen jet blast converter. All incoming materials are passed through this process computer aided talented offspring of its two ancient prototypes the blast furnace and slagging-ash gas producers and the zone controlled blast furnaces described in U.S. Pat. Nos. 4,381,938, 4,495,054, 3,928,023 and 3,814,404. It employs two sets of tuyeres located in the bosh to input endothermic reacting gases, vapors and dusts through tuyere sets T1 and T2. A 100% oxygen jet blast is also input through tuyere set T2. Three sets of tuyeres in the stack are used to output finished products and by-products, T3, T4 and T5, zone control the stack temperature profile and remove recycling in the stack materials.Incoming solid raw materials are charged in at the top and molten slag and metal are removed from near the bottom as in conventional blast furnace practice. As the burden descends it is completely converted by the precisely controlled as to temperature volume, and composition up moving gas stream. It is originated by combusting in the bosh a more central than conventional portion of the carbonaceous grate with the oxygen jet blast entering through tuyere set T2. It furnishes the heat required to completely convert the downmoving burden to a gas, vapor, molten slag, molten metal or dust. The portion of the gas withdrawn through tuyere set T3 just above the mantel in two modes of operation is an ideal boiler fuel or reducing gas as withdrawn. When it is combusted it produces only water, carbon dioxide and nitrogen, no harmful gases or chemical residues. All other by-products withdrawn or raw materials consumed in other units in the improved converter system producing finished products needed by mankind. Burning in the bosh a more central than conventional portion of the carbonaceous grate with the oxygen jet blast entering through tuyere set T2. It furnishes the heat required to completely convert the down moving burden to a gas, vapor, molten slag, molten metal or dust. The portion of the gas withdrawn through tuyere set T3 located in the stack just above the bosh is an ideal boiler fuel or reducing gas as withdrawn. When it is combusted it produces only water, carbon dioxide and nitrogen, no harmful gases or chemical residues.
    • 9. 发明授权
    • Method for direct use of chromite ore in the production of stainless
steel
    • 方法直接使用铬铁矿生产不锈钢
    • US5702502A
    • 1997-12-30
    • US573316
    • 1995-12-14
    • David M. KundratAllan M. SmillieRichard C. Sussman
    • David M. KundratAllan M. SmillieRichard C. Sussman
    • C21C7/00C21C5/00C21C5/28C21C7/04C21C7/06C21C7/068C21C7/10C21B15/00C22B4/04C22B9/00
    • C21C5/005
    • A three-stage process for obtaining metallic Cr units insitu during the production of stainless steel. Raw chromite ore or a concentrate produced from chromite ore is mixed with a carbonaceous reductant and slagging agents are added to an iron bath (24) for smelting and refining in a refining reactor (10). During the first stage, partially metallized chromite is smelted by carbon in the reactor that is top-and bottom-blown with oxygen and oxygen-containing gases respectively to produce a chromium alloy bath having a carbon content well below saturation. In the second stage, the alloy bath is decarburized by being bottom stirred with the oxygen-containing gas to the final bath carbon specification. In the third stage, the alloy bath is reduced by a metalloid reductant such as silicon or aluminum and again bottom stirred but with a non-oxidizing gas to achieve a high chromium yield. The reactor includes a top lance (18) extending through a throat (14) with a lower portion (20) of the lance extending to a point just above the bath and means (22) such as a tuyere or porous plug mounted at or near a bottom (16) and extending through a refractory lining (12) for stirring the iron bath containing dissolved carbon. Lance (18) includes a central passage (34) for injecting a compact, focused jet oxygen gas (30) that can penetrate through a slag layer (26) for decarburization of the iron bath and an outer passage (32) for discharging an oxygen gas (28) above the bath for post-combustion of CO to CO.sub.2. Passage (32) includes a plurality of evenly spaced annular diverging nozzles (33). The lance also includes a pair of concentric conduits (36) and (38) for conducting a coolant.
    • 在不锈钢生产过程中获得金属铬单元的三阶段工艺。 将原铬铁矿或由铬铁矿生产的浓缩物与碳质还原剂混合,并将成渣剂加入到铁浴(24)中,以在精炼反应器(10)中熔炼和精炼。 在第一阶段,部分金属化的铬铁矿分别用氧气和含氧气体进行顶吹和底吹的反应器中的碳熔炼,以产生碳含量远低于饱和度的铬合金浴。 在第二阶段,通过与含氧气体底部搅拌至最终浴碳规格,使合金浴脱碳。 在第三阶段中,合金浴由诸如硅或铝的类金属还原剂还原,并再次用底部搅拌而用非氧化性气体还原,以获得高的铬产率。 反应器包括延伸穿过喉部(14)的顶部喷枪(18),其中喷枪的下部(20)延伸到浴的正上方,以及装置(22),例如安装在或靠近 底部(16)并延伸穿过耐火衬里(12),用于搅拌含有溶解碳的铁浴。 喷枪(18)包括一个中心通道(34),用于喷射一个致密聚焦的喷射氧气(30),该气体可以穿透用于铁浴脱碳的炉渣层(26),以及用于排出氧气的外部通道 在浴上方的气体(28),用于CO至CO的后燃烧。 通道(32)包括多个均匀间隔开的环形发散喷嘴(33)。 喷枪还包括用于传导冷却剂的一对同心导管(36)和(38)。
    • 10. 发明授权
    • Method and apparatus for producing steel rods with a desired tensile
strength and model for simulating same
    • 用于生产具有所需拉伸强度的钢棒的方法和装置以及用于模拟它的模型
    • US5462613A
    • 1995-10-31
    • US254969
    • 1994-06-07
    • Robert J. GlodowskiAllyen E. Wilson, III
    • Robert J. GlodowskiAllyen E. Wilson, III
    • C21C5/28C21D9/573
    • C21C5/285C21D9/5732
    • A method and apparatus are provided for producing rods having a desired tensile strength from a rod manufacturing process set to an optimal operating condition. Initially, the rod manufacturing process is set in an optimal condition to produce rods at a maximum rate, while optimizing the mechanical properties therein. Raw materials are melted and a "heat of steel" representing one lot is poured into a ladle which is sampled to determine its chemical composition. The percentage content of each element is utilized within an empirical model modeling the rod manufacturing process to predict the tensile strength of rods. The empirical model is again utilized to determine the amount by which a control element must be varied to adjust the predicted tensile strength to the desired tensile strength. The control element represents an element, such as, carbon which significantly impacts the tensile strength of the rod. The predicted level of the control element necessary to achieve the target tensile strength is referred to as the "floating aim level" thereof. If the floating aim level exceeds a maximum accepted level for the control element the empirical model is again used to determine the necessary level of a second control element. Next, the heat of steel is trimmed to provide a lot having the target tensile strength.
    • 提供了一种方法和装置,用于从棒制造过程设置到最佳操作条件来生产具有期望拉伸强度的棒。 最初,杆制造过程被设定在最佳条件下,以最大速率生产杆,同时优化其中的机械性能。 将原材料熔化,将代表一批的“钢热”倒入钢包中,该钢包被取样以确定其化学成分。 在一个经验模型中利用每个元素的百分比来建模棒制造过程来预测棒的拉伸强度。 经验模型再次用于确定控制元件必须变化的量,以将预测的拉伸强度调整到所需拉伸强度。 控制元件表示一种元素,例如显着影响杆的拉伸强度的碳。 实现目标拉伸强度所需的控制元件的预测值被称为“浮动目标水平”。 如果浮动目标水平超过控制元件的最大可接受水平,则经验模型再次用于确定第二控制元件的必要水平。 接下来,对钢的热量进行修整以提供具有目标拉伸强度的很多。