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    • 3. 发明授权
    • Recovery of molybdenum from molybdenum bearing sulfide materials by bioleaching in the presence of iron
    • 在铁存在下通过生物浸出从含钼硫化物材料中回收钼
    • US08268037B2
    • 2012-09-18
    • US12375955
    • 2007-07-19
    • Wolfgang KummerWilfried GutknechtJames Gregory OlsonThomas R. Clark
    • Wolfgang KummerWilfried GutknechtJames Gregory OlsonThomas R. Clark
    • C22B3/18C22B3/06
    • C22B3/18C22B3/08C22B34/34Y02P10/234
    • The invention relates to a method of recovering molybdenum from a molybdenum bearing sulfide material. The material is contacted with a leaching solution in the presence of iron compounds and mesophilic or thermophilic iron oxidizing microorganisms and subsequently, a leaching process is performed by controlling the molar ratio of dissolved ferric iron to dissolved molybdenum. Preferably, a high amount and molar excess of dissolved iron is used. The presence of high concentrations of ferric iron in bioleach solutions allows iron-oxidizing microorganisms to grow and oxidize iron and bioleach molybdenite at dissolved Mo concentrations as high as 4.4 g/L. Organic metabolites were not required for protecting cells from Mo toxicity. Maximum dissolution rates depend on reactor configuration, with agglomerated material simulating heap leaching of almost 1% Mo/day, but up to 10.2% Mo/day in suspension/stirred reactor configurations, with rate highly dependent on temperature within the range of 25° C. to 40° C. The ultimate extent of Mo removal from the molybdenum bearing sulfide material is 89%. Finally, molybdenum is recovered from a leach residue of the leaching process.
    • 本发明涉及从含钼硫化物材料中回收钼的方法。 在铁化合物和嗜温或嗜热铁氧化微生物的存在下,将材料与浸出溶液接触,随后,通过控制溶解的三价铁与溶解的钼的摩尔比来进行浸出过程。 优选地,使用高量和摩尔过量的溶解铁。 在生物浸出溶液中存在高浓度的三价铁可使铁氧化微生物在溶解的Mo浓度高达4.4g / L时生长并氧化铁和生物漂白辉钼矿。 不需要有机代谢物来保护细胞免受Mo毒性。 最大溶解速率取决于反应器构型,其中模拟堆浸浸出量为1%Mo /天的聚集材料,但在悬浮/搅拌反应器构型中高达10.2%Mo /天,速率高度依赖于25℃范围内的温度 至40℃。从含钼硫化物材料除去Mo的最终程度为89%。 最后,从浸出过程的浸出残渣中回收钼。
    • 4. 发明申请
    • RECOVERY OF MOLYBDENUM FROM MOLYBDENUM BEARING SULFIDE MATERIALS BY BIOLEACHING IN THE PRESENCE OF IRON
    • 通过在铁存在下通过生物柴油回收莫来石轴承硫化物材料
    • US20090320648A1
    • 2009-12-31
    • US12375955
    • 2007-07-19
    • Wolfgang KummerWilfried GutknechtJames Gregory OlsonThomas R. Clark
    • Wolfgang KummerWilfried GutknechtJames Gregory OlsonThomas R. Clark
    • C22B34/34E21B43/28
    • C22B3/18C22B3/08C22B34/34Y02P10/234
    • The invention relates to a method of recovering molybdenum from a molybdenum bearing sulfide material. The material is contacted with a leaching solution in the presence of iron compounds and mesophilic or thermophilic iron oxidizing microorganisms and subsequently, a leaching process is performed by controlling the molar ratio of dissolved ferric iron to dissolved molybdenum. Preferably, a high amount and molar excess of dissolved iron is used. The presence of high concentrations of ferric iron in bioleach solutions allows iron-oxidizing microorganisms to grow and oxidize iron and bioleach molybdenite at dissolved Mo concentrations as high as 4.4 g/L. Organic metabolites were not required for protecting cells from Mo toxicity. Maximum dissolution rates depend on reactor configuration, with agglomerated material simulating heap leaching of almost 1% Mo/day, but up to 10.2% Mo/day in suspension/stirred reactor configurations, with rate highly dependent on temperature within the range of 25° C. to 40° C. The ultimate extent of Mo removal from the molybdenum bearing sulfide material is 89%. Finally, molybdenum is recovered from a leach residue of the leaching process.
    • 本发明涉及从含钼硫化物材料中回收钼的方法。 在铁化合物和嗜温或嗜热铁氧化微生物的存在下,将材料与浸出溶液接触,随后,通过控制溶解的三价铁与溶解的钼的摩尔比来进行浸出过程。 优选地,使用高量和摩尔过量的溶解铁。 在生物浸出溶液中存在高浓度的三价铁可使铁氧化微生物在溶解的Mo浓度高达4.4g / L时生长并氧化铁和生物漂白辉钼矿。 不需要有机代谢物来保护细胞免受Mo毒性。 最大溶解速率取决于反应器构型,其中模拟堆浸浸出量为1%Mo /天的聚集材料,但在悬浮/搅拌反应器构型中高达10.2%Mo /天,速率高度依赖于25℃范围内的温度 至40℃。从含钼硫化物材料除去Mo的最终程度为89%。 最后,从浸出过程的浸出残渣中回收钼。
    • 8. 发明授权
    • Process for producing pure ammonium metallates
    • 生产纯铵金属盐的方法
    • US5891407A
    • 1999-04-06
    • US973351
    • 1997-12-05
    • Wilfried GutknechtWolfgang Mathy
    • Wilfried GutknechtWolfgang Mathy
    • C01G31/00C01G37/00C01G39/00C01G41/00C01G47/00
    • C01G39/003C01G31/003C01G37/003C01G41/003C01G47/003
    • The present invention relates to a process for the production of pure ammonium metallates of the metals W, Mo, V, Cr and Re, wherein alkaline metal salt solutions are adjusted to a pH value in the range from 5 to 9 by reaction with CO.sub.2, these metal salt solutions are passed through an anion exchanger in carbonate form, wherein, in addition to the alkali metal carbonate solution, the metallate form of the ion exchanger is formed, the ion exchanger is then washed until free of alkali and is then eluted by means of aqueous ammonia to form ammonium metallate solutions and the anion exchanger in the OH form, wherein the anion exchanger is converted into the carbonate form by means of CO.sub.2 treatment and is recycled.
    • PCT No.PCT / EP96 / 02318 Sec。 371 1997年12月4日第 102(e)日期1997年12月4日PCT提交1996年5月30日PCT公布。 WO96 / 41767 PCT出版物 日期:1996年12月27日本发明涉及生产金属W,Mo,V,Cr和Re的纯金属铵盐的方法,其中将碱金属盐溶液调节至5至9的pH值 通过与CO 2反应,这些金属盐溶液通过碳酸盐形式的阴离子交换剂,其中,除了碱金属碳酸盐溶液之外,形成离子交换剂的金属化物形式,然后将离子交换剂洗涤直至不含碱 然后通过氨水洗脱以形成金属铵溶液和OH形式的阴离子交换剂,其中阴离子交换剂通过CO 2处理转化为碳酸盐形式并被再循环。