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    • 21. 发明申请
    • METAL MELTING APPARATUS AND METHOD FOR MELTING METAL
    • 金属熔炼设备和金属冶炼方法
    • US20130161881A1
    • 2013-06-27
    • US13337933
    • 2011-12-27
    • Shao-Hua Lu
    • Shao-Hua Lu
    • C22B9/00F27D3/08F27D27/00F27D13/00
    • F27D13/002C22B7/003F27B19/02F27D27/00
    • A metal melting apparatus has a heating furnace, a melting furnace mounted on the heating furnace, a high-cycle regenerative system (FIRS), a raw material feeding device and a melted material feeding device mounted on the melting furnace. The HRS heats and recycles high temperature air in the heating furnace and guides the high temperature air to the preheating screw to preheat metal materials in the preheating screw. Thus, a time for melting the metal materials from solid to liquid is greatly shortened. Furthermore, a series of processes for preheating the metal materials in the raw material feeding device, melting the metal materials in the melting furnace and injecting the molten materials to the molds is fluent, time-saving and safe, and can progress continuously.
    • 金属熔化装置具有加热炉,安装在加热炉上的熔炉,高周期再生系统(FIRS),原料供给装置和安装在熔炉上的熔融材料供给装置。 HRS加热并回收加热炉中的高温空气,并将高温空气引导到预热螺杆,以预热预热螺杆中的金属材料。 因此,将金属材料从固体熔化成液体的时间大大缩短。 此外,一系列用于预热原料进给装置中的金属材料的方法,熔化熔融炉中的金属材料并将熔融材料注入到模具中是流畅的,节省时间和安全的,并且可以连续进行。
    • 27. 发明申请
    • Recovery of steel from contaminated scrap
    • 从受污染的废料回收钢
    • US20070180955A1
    • 2007-08-09
    • US10590409
    • 2005-05-26
    • Noel Warner
    • Noel Warner
    • C21C7/00C22B9/00
    • C22B9/04C21C5/562C21C7/10C22B7/003C22B9/05C22B15/0056Y02P10/132Y02P10/216Y02P10/22Y02P10/228Y02P10/232
    • This invention provides a method for overcoming the adverse effects of disintegration of molten steel streams due to sub-surface growth of carbon monoxide bubbles when exposed to reduced pressures and thus permits refining of liquid scrap much the same way as if it were a quiescent liquid melt. Steel scrap contaminated with copper, tin, zinc and organics, such as PVC coating, is preheated and melted continuously using melt circulation and then continuously refined in-line to yield high quality liquid steel and separate non-ferrous metal byproducts by straightforward physical desorption under reduced pressure using an inert strip gas within a desorber and then subsequent iron vapour condensation by direct contacting with liquid steel followed by selective condensation of copper initially and then recovery of tin. Formation of dioxins from scrap containing chlorine is precluded by inline scrubbing of pyrolysis gas formed during scrap preheating. The initial melting of preheated scrap employs melt circulation and gas combustion rather than fossil fuel generated electricity and is thus inherently energy efficient.
    • 本发明提供了一种克服当暴露于减压时由于一氧化碳气泡的亚表面生长而导致的钢水流分解的不利影响的方法,并且因此允许液体废料的精炼与其静态液体熔体相同 。 用铜,锡,锌和有机物(如PVC涂层)污染的废钢被熔融循环连续预热和熔融,然后在线连续精炼,得到高品质的液态钢,并通过直接的物理解吸分离有色金属副产物 在解吸器内使用惰性带状气体减压,然后通过与液态钢直接接触随后的铁蒸汽冷凝,然后首先选择性地冷凝铜,然后回收锡。 通过在废料预热期间形成的热解气体的在线洗涤排除了含有氯的废料形成二恶英。 预热废料的初始熔化使用熔体循环和气体燃烧而不是化石燃料发电,因此本来就是能量效率。
    • 29. 发明授权
    • Battery recycling
    • 电池回收
    • US07169206B2
    • 2007-01-30
    • US11108321
    • 2005-04-18
    • Daniel CheretSven Santen
    • Daniel CheretSven Santen
    • C22B23/06
    • C22B23/06C22B7/003C22B23/023Y02P10/224
    • Process for the recovery of Co or Ni, comprising the steps of: preparing a metallurgical charge comprising Fe, slag formers, and a useful load containing either one or both of Co and Ni; feeding the charge to a shaft furnace; and smelting the charge so as to form a Co or Ni-bearing alloy, an Fe-bearing slag and a gaseous phase, characterised in that the useful load comprises at least 30 wt. % electrochemical batteries or their scrap, and in that the redox potential in the furnace is chosen so as to slag at least 20 wt. % of the Fe, and at most 20 wt. % of the Co or 20 wt. % of the Ni present in the charge.
    • 用于回收Co或Ni的方法,包括以下步骤:制备包含Fe,成矿剂和含有Co和Ni中的一种或两种的有用载体的冶金装料; 将电荷送入竖炉; 并且熔炼所述电荷以形成Co或Ni承载合金,含Fe矿渣和气相,其特征在于所述有用载荷包含至少30wt。 %的电化学电池或其废料,并且选择炉中的氧化还原电位以使炉渣至少20wt。 Fe%,最多20wt。 Co的百分比或20重量% Ni中存在的%的电荷。