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    • 6. 发明授权
    • Neodymium recovery process
    • 钕回收工艺
    • US5362459A
    • 1994-11-08
    • US61461
    • 1993-05-17
    • Bernard Greenberg
    • Bernard Greenberg
    • C01F17/00
    • C01F17/0062
    • The present invention is a method of recovering neodymium (Nd) from waste by-products of rare earth magnet manufacture. Two main waste by-products, NdFeB swarf and NdFeB slag, are treated by two respective chemical schemes as described above. However, the only major consumption of chemical compound in both schemes is hydrofluoric acid (HF). The present invention scheme for NdFeB swarf recovery is characterized by using acetic acid (HC.sub.2 H.sub.3 O.sub.2) having a pK value of approximately 4.7. The present invention scheme for NdFeB slag recovery is characterized by using sulfamic acid electrolyte bath having a pH value of approximately 2.7. The moist neodymium trifluoride (NdF.sub.3) produced by both schemes can be dried by using the same microwave radiation technique to produce dry neodymium trifluoride (NdF.sub.3) which contains less than 3% moisture.
    • 本发明是从稀土磁体制造废弃副产物中回收钕(Nd)的方法。 两种主要的废弃副产品,钕铁硼切屑和钕铁硼矿渣,按照上述两种相应的化学方案进行处理。 然而,两种方案中化学化合物的主要消费量是氢氟酸(HF)。 NdFeB切屑回收的本发明方案的特征在于使用pK值为约4.7的乙酸(HC2H3O2)。 NdFeB渣回收的本发明方案的特征在于使用pH值为约2.7的氨基磺酸电解液浴。 通过使用相同的微波辐射技术,可以通过两种方案产生的湿的三氟化钕(NdF 3)干燥以产生含有小于3%水分的干式三氟化钕(NdF 3)。
    • 9. 发明授权
    • Scavenger and process for purification of metal fluorides
    • 净化金属氟化物的清除剂和方法
    • US3282641A
    • 1966-11-01
    • US31495363
    • 1963-10-09
    • HARSHAW CHEM CORP
    • MARKO SFILIGOJSWINEHART CARL F
    • C01D3/20C01F5/28C01F11/22C01F17/00C01G1/06C30B11/00G02B1/02
    • G02B1/02C01D3/20C01F5/28C01F11/22C01F17/0062C01G1/06C30B11/00C30B29/12
    • A colour-free crystal of alkaline earth or rare earth fluorides is obtained by melting and solidifying the fluorides in the presence of the vapour of CoF3 and/or MnF3. Fluorides of Mg, Ca, Sr, Ba, and all the rare earths La-Lu are specified, and mixtures, e.g. BaF2 with 10-30% CaF2. They may be synthetic (obtained by reacting acetate, carbonate, or nitrate with HF) or natural, e.g. fluorspar, and may be solid bodies grown previously from a melt but having an optical defect, or may be comminuted. The CoF3 or MnF3 in amounts of 0.25-2% b.w. of the charge is placed in a vented cup above the fluoride charge in a crucible, and vaporizes as the charge melts. The crucible is then lowered into a cooler zone across a sharp temperature gradient to effect crystal growth. The melt may also include 1-4% b.w. lead fluoride with or without PbO or Pb3O4 and Pb metal, or 0.05-0.2% V metal; alternatively the additive metal may be placed in a vented cup.ALSO:A colour-free crystal of alkaline earth or rare earth fluorides is obtained by melting and solidifying the fluorides in the presence of the vapour of CoF3 and/or MnF3. Fluorides of Mg, Ca, Sr, Ba, and all the rare earth La-Lu are specified, and mixtures, e.g. BaF2 with 10-30% CaF2. They may be synthetic (obtained by reacting acetate, carbonate, or nitrate with HF) or natural, e.g. fluorspar, and may be solid bodies grown previously from a melt but having an optical defect, or may be comminuted. The CoF3 or MnF2 in amounts of 0.25-2% b.w. of the charge is placed in a vented cup above the fluoride charge in a crucible, and vaporises as the charge melts. The crucible is then lowered into a cooler zone across a sharp temperature gradient to effect crystal growth. The melt may also include 1-4% b.w. lead fluoride with or without PbO or Pb3O4 and Pb metal, or 0.05-0.2% V metal; alternatively the additive metal may be placed in a vented cup.