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    • 32. 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 The portion of the gas withdrawn through tuyere set T3 just above the mantel in two modes of operation is an ideal boiler fuel or reducing gas as withdrawn.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 All other by-products withdrawn or raw materials consumed in other units in the improved converter system producing finished products needed by mankind.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.
    • 34. 发明授权
    • Charge preheater
    • 充电预热器
    • US5645791A
    • 1997-07-08
    • US507270
    • 1995-08-21
    • Gerhard FuchsJoachim EhleKlaus von Ploetz
    • Gerhard FuchsJoachim EhleKlaus von Ploetz
    • C21B7/18C21C5/56F27D3/00F27D13/00C21B7/00
    • C21B7/18F27D13/002F27D3/0028C21C5/565Y02P10/216
    • In a charging material preheater for a metallurgical smelting plant having a shaft (5) which has closure members (7, 8) which are pivotable by a control member (6) and which include fingers (9, 10) which are arranged parallel and at a spacing relative to each other, the fingers (9, 10) of a closure member (7, 8) are mounted with a central portion in a first rotary mounting (12, 13) and in a second rotary mounting (21, 22) of the frame structure (2) with an outer portion which is passed outwardly through an opening (14, 15) in the shaft wall, by way of an elbow lever mechanism (16, 17), and lever arms (18, 19) of at least two elbow lever mechanisms are connected together by a connecting member (23) which is pivotably engaged by a control member (6) which is supported in a third rotary mounting (26, 27) of the frame structure (2).
    • PCT No.PCT / EP94 / 02405 Sec。 371日期1995年8月21日 102(e)日期1995年8月21日PCT 1994年7月21日PCT公布。 出版物WO95 / 04910 日期1995年2月16日在具有轴(5)的冶金冶炼厂的充电材料预热器中,该轴(5)具有可由控制构件(6)枢转并且包括手指(9,10)的闭合构件(7,8) 相对于彼此平行且间隔设置,封闭构件(7,8)的指状物(9,10)安装有第一旋转安装件(12,13)中的中心部分,并且在第二旋转安装 (21),其外侧部分通过肘杆机构(16,17)通过轴壁中的开口(14,15)向外通过,并且杠杆臂( 至少两个肘杆机构通过连接构件(23)连接在一起,所述连接构件(23)由支撑在框架结构的第三旋转安装件(26,27)中的控制构件(6)可枢转地接合 2)。
    • 35. 发明授权
    • Melt shop layout
    • 熔化车间布局
    • US5628958A
    • 1997-05-13
    • US465396
    • 1995-06-05
    • William R. Frank
    • William R. Frank
    • C21B13/00C21B13/12C21C5/52C21C5/56F27B3/08C21B7/00
    • C21B13/004C21C5/567Y02P10/212Y10S266/901
    • A melt shop for melting scrap steel comprises a pair of primary melting furnaces and a pair of refining facility stations. The layout for the primary melting furnaces, refining facility, associated support, and peripheral equipment and caster is a single-aisle layout with general longitudinal alignment of the major constituent elements. Scrap delivery to the primary melt furnaces may comprise trackways running perpendicular to the longitudinal layout, the discharge end of each trackway being proximate to a primary melt furnace. A single trackway is preferably provided for a pair of overhead cranes running longitudinally from the caster to the primary melt furnaces.
    • 用于熔炼废钢的熔化车间包括一对主熔化炉和一对精炼设备站。 主熔化炉,精炼设备,相关支持和周边设备和脚轮的布局是单通道布局,主要构成要素具有总体纵向对齐。 向初级熔化炉的废料输送可以包括垂直于纵向布局运行的轨道,每个轨道的排放端靠近主熔融炉。 优选地提供用于从脚轮纵向延伸到主熔化炉的一对顶起重机的单个轨道。