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    • 5. 发明授权
    • Soundproofed conduit to discharge fumes
    • 隔音导管排放烟雾
    • US06059070A
    • 2000-05-09
    • US19744
    • 1998-02-06
    • Marco Peter CudicioGiorgio Beuzer
    • Marco Peter CudicioGiorgio Beuzer
    • C21C5/36C21C5/52F27D17/00F27D21/00E04F17/04
    • F27D17/001C21C5/5217F27D21/00C21C2005/366F23J2900/13003F27D2021/0064Y02P10/216Y10S454/906
    • Soundproofed conduit to discharge fumes, advantageously associated with assemblies to discharge fumes for melting systems in steel production plants, the conduit being located between the ventilation system (14) and an outlet chimney (13), at least the first segment (19a) of the discharge conduit defining a section with a value (A) through which the fumes transit, the conduit (12) defining a path, from the relative ventilation system (14) to the discharge chimney (13), comprising at least two counter-opposed and controlled changes in direction (15a, 15b) defining at least respective consecutive segments (19a, 19b, 19c) arranged one at an angle to another, the changes in direction being functionally configured so as to cause phase and counter-phase effects of the sound waves generated by the fluid in transit, the phase and counter-phase effects having the purpose of at least deadening partly the sound waves caused by the passage of the fluid.
    • 用于排出烟雾的隔音导管,其有利地与组件相关联,以排出用于钢铁生产设备中的熔化系统的烟雾,所述管道位于通风系统(14)和出口烟囱(13)之间,至少第一段(19a) 排出管道,其限定具有值(A)的部分,烟道从所述相对通风系统(14)到所述排放烟道(13)从所述通道(12)限定出路径,所述通道包括至少两个反向对置和 限定至少相应的连续段(19a,19b,19c)的方向(15a,15b)的改变,所述至少相应的连续段(19a,19b,19c)以一角度相互排列成一个方向,所述方向上的变化被功能地配置为引起声音的相位和相位效应 由运输中的流体产生的波浪,相位和相位效应至少使得由流体通过引起的声波至少部分消音。
    • 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.
    • 8. 发明授权
    • Process and unit for continuous metal refinement
    • 连续金属细化的工艺和单元
    • US5558695A
    • 1996-09-24
    • US513783
    • 1995-08-29
    • Valentin P. TsymbalSergei P. MochalovKim M. ShakirovRafik S. AizatulovBoris A. KustovNikolai I. MikheevAnatoly I. Toropov
    • Valentin P. TsymbalSergei P. MochalovKim M. ShakirovRafik S. AizatulovBoris A. KustovNikolai I. MikheevAnatoly I. Toropov
    • C21C7/00C21C5/36C21C5/56C21C7/04C21C7/072C22B9/00C21C5/30
    • C22B9/00C21C5/567B01J2219/1942C21C2005/366Y10S75/962
    • A process of continuous metal refinement comprising feeding molten metal to a reaction chamber, introducing gaseous and solid oxidants, adding bulk materials, fully converting the metal and slag into a foamy emulsion, creating, in the reaction chamber, an increased pulsating pressure and a considerable deviation of a system from thermodynamic equilibrium by way of creating a self-organizing system of chemical reaction with gas evolution and taking off the emulsion into a refining sump at the critical speed of egress of two-phase liquid, separating the metal and slag in said refining sump and withdrawing the gas through a high layer of emulsion at a definite rate. A unit for continuously refining metal, comprising a spherical reaction chamber (1) with a channel (5) for supplying molten metal and a channel (4) for feeding bulk materials, with a device for feeding a gaseous oxygen made in the form of oppositely arranged lances, a cylindrical connection channel (2), a refining sump (3) with tap holes (20, 15) for withdrawing metal and slag, respectively, the slag tap hole is divided into two vertical channels (16, 17) for separating slag and gas, respectively, a channel (13) for the delivery of slag-forming materials, and lances (11, 12) for feeding oxygen.
    • PCT No.PCT / RU93 / 00325 Sec。 371日期1995年8月29日 102(e)日期1995年8月29日PCT 1993年12月30日PCT PCT。 公开号WO95 / 18238 日期1995年7月6日一种连续金属细化的方法,包括将熔融金属加入到反应室中,引入气态和固体氧化剂,加入大量材料,将金属和矿渣完全转化成泡沫状乳液,在反应室中产生增加的 脉动压力和系统与热力学平衡的显着偏差,通过建立与气体放出的化学反应的自组织系统,并以两相液体出口的临界速度将乳液分离成精炼池,将 金属和矿渣,并以一定的速率将气体通过高层乳液取出。 一种用于连续精炼金属的单元,包括具有用于供应熔融金属的通道(5)的球形反应室(1)和用于供给散装材料的通道(4),用于供给相反形式的气态氧气的装置 排出的喷枪,圆柱形连接通道(2),具有用于分离金属和炉渣的排放孔(20,15)的精炼池(3),分渣孔分为两个垂直通道(16,17),用于分离 渣和气体,用于输送成渣材料的通道(13)和用于供给氧气的喷枪(11,12)。