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Improvements in or relating to the process of smelting of metal and a furnace therefor

机译:金属或金属熔炼工艺的改进或相关

摘要

662,634. Melting and refining metals. WEIL, W. M. June 27, 1947. [July 12, 1946] No. 17014/47. Class, 82(i). [Also in Groups XI and XII] Metals such as aluminium are melted and refined in a reverberatory furnace (see Group XII), which in one form, Figs. 2 and 3, comprises a main heating chamber, which normally contains a pool of molten metal B, and an auxiliary open chamber having a hearth 18 arranged at substantially the same level as the main hearth 1 and divided by a partition 40 into two compartments adapted to contain pools of metal C and A and communicating with the main chamber through passages 20 and 21 respectively. The passage 21 is provided with a vertically-movable door 22 which is normally so positioned as to prevent flow of slag from the surface of the pool A into the main chamber. Molten metal may be withdrawn from the pool C through vertical passages 23, 24 and caused to flow upwardly through a central passage 26 by means of an electromagnetic induction pump, (see Group XI), which also effects heating of the metal in the passages. The passage 26 communicates with a pipe 37 through which a stream of metal may be directed into the pool A over a lip 38 formed on the partition 40. In operation, solid metal to be melted is charged into the pool A adjacent the partition and is engulfed by or mixed with molten metal fed through the pipe 37, fluxing or refining agents being added to the resulting pasty mass. Charging is then discontinued for a period sufficient to allow liquefaction of the mass, the impurities rising to the surface being skimmed off and the refined material flowing into the heating chamber where it may be tapped off. Molten solid metal may then be charged and the process repeated. In a second form, Fig. 7 suitable for a continuous process, metal is withdrawn from a pool D in the auxiliary chamber by an electrically-driven pump 76 and supplied to a manifold 82 having lateral branches 83 and 84, controlled by gate valves 85 and 86, from which the metal may be discharged tangentially into a hopper 72, 73 and into the pool E respectively. Solid metal to be melted together with fluxing and refining agents is fed continuously into the hopper and becomes mixed with the molten metal due to the whirling motion induced by the discharge from the branch 83, the resulting pasty mass passing through opening 75 into the pool E where it is liquefied by the stream of metal from the branch 84. At this stage the metal is puddled and the slag skimmed off, the refined metal passing into the main chamber through the passage 22. Further refining agents may be introduced through the branch 84. Specifications 542,347 and 632,947, [Group Xi], are referred to.
机译:662,634。熔化和提炼金属。威尔,W。M.,1947年6月27日。[1946年7月12日]第17014/47号。第82(i)类。 [第XI和XII族中也]在反射炉(参见第XII族)中熔融和精炼铝之类的金属,其形式为图1和2。如图2和图3所示,该炉包括主加热室,该加热室通常包含熔融金属B的池,以及辅助开放室,该辅助开放室具有炉床18,该炉床布置在与主炉床1基本相同的高度处,并且由分隔壁40分成适合于两个的隔室。容纳金属池C和A,并分别通过通道20和21与主腔连通。通道21设置有可竖直移动的门22,该门通常被定位成防止炉渣从池A的表面流入主腔室。熔融金属可通过垂直通道23、24从池C中抽出,并借助于电磁感应泵(参见第XI组)使其向上流过中央通道26,这也影响了通道中金属的加热。通道26与管37连通,金属流可通过该管37在隔板40上形成的唇缘38上被引导到池A中。在操作中,待熔化的固体金属被注入到隔板附近的池A中,并且被熔化。被通过管道37输送的熔融金属吞没或与之混合,将助熔剂或精炼剂添加到所得糊状物料中。然后,中断充电的时间应足以使物料液化,上升至表面的杂质会被撇去,精炼后的物料会流入加热室,然后从中排出。然后可以装入熔融的固体金属并重复该过程。在第二种形式中,适用于连续过程的图7中,金属通过电动泵76从辅助腔室的池D中抽出,并输送到歧管82,歧管82具有侧向分支83和84,由闸阀85控制和86,金属可以分别切向地排入料斗72、73和池E中。将与助熔剂和精炼剂一起熔化的固体金属连续地进料到料斗中,并由于分支83的排出引起的回旋运动而与熔融金属混合,所得糊状物料通过开口75进入池E在这里,它被来自分支机构84的金属流液化。在这一阶段,将金属搅成泥状,将矿渣撇去,精炼金属通过通道22进入主室。可以通过分支机构84引入其他精炼剂。参照规格542,347和632,947,[第Xi组]。

著录项

  • 公开/公告号GB662634A

    专利类型

  • 公开/公告日1951-12-12

    原文格式PDF

  • 申请/专利权人 WALTER M. WELL;

    申请/专利号GB19470017014

  • 发明设计人

    申请日1947-06-27

  • 分类号C22B9/00;

  • 国家 GB

  • 入库时间 2022-08-24 01:03:01

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