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    • 2. 发明授权
    • Process for separately recovering zinc and lead values from zinc and
lead containing sulphidic ore
    • 从锌和含铅硫化矿石中分别回收锌和铅的过程
    • US4545963A
    • 1985-10-08
    • US536013
    • 1983-09-26
    • Donald R. WeirIan M. MastersBarry N. DoyleMichael E. Chalkley
    • Donald R. WeirIan M. MastersBarry N. DoyleMichael E. Chalkley
    • C22B13/00B03D1/02B03D1/06C22B19/00C22B19/20C01G3/00C01G9/00C01G21/00
    • C22B19/22B03D1/02B03D1/06C22B13/04Y02P10/234
    • A process for separately recovering zinc and lead values from zinc and lead containing sulphidic ore which also contains iron comprises subjecting ground ore to a first flotation step to float an initial lead concentrate containing zinc and produce zinc and iron containing tailings. The zinc and iron containing tailings are subjected to a second flotation step to float an initial zinc concentrate containing iron and also produce tailings. The initial zinc concentrate is subjected to a third flotation step to float a further zinc concentrate containing iron and also produce zinc and iron containing tailings. The zinc and iron containing tailings from the third flotation step and at least a lead and zinc containing portion of the initial lead concentrate are leached in a first leach step under oxidizing conditions at a temperature in the range of from about 130.degree. to about 170.degree. C. in aqueous sulphuric acid solution with a stoichiometric excess of sulphuric acid relative to the zinc content of from about 50 to about 150% so as to give a terminal acidity of from about 50 to about 80 g/L to produce a lead-containing residue and a first leach solution containing zinc and iron. The lead containing residue is separated from the first leach solution and the first leach solution is treated with the further zinc concentrate or calcine produced therefrom by roasting to dissolve zinc therefrom and precipitate a substantial amount of dissolved iron, thereby producing an iron containing residue and a second leach solution containing zinc. The iron containing residue is separated from the second leach solution, and the second leach solution is treated to recover zinc.
    • 还含有铁和含锌硫化矿石的锌和铅值分别回收还含有铁的方法包括对地矿进行第一浮选步骤以漂浮含有锌的初始含铅浓缩物并产生含锌和铁的尾矿。 对含锌和铁的尾矿进行第二浮选步骤以漂浮含有铁的初始锌精矿并且还产生尾矿。 初始锌精矿经受第三浮选步骤以漂浮含有铁的另外的锌精矿,并且还产生含锌和铁的尾矿。 在氧化条件下,在约130℃至约170℃的温度范围内,将第一浮选步骤中含锌和铁的尾矿以及至少含铅和锌的部分初始浓缩铅浸出, 在相对于锌含量为约50至约150%的化学计量过量硫酸的硫酸水溶液中,以产生约50至约80g / L的终端酸度以产生含铅的 残渣和含锌和铁的第一浸出溶液。 含铅残渣与第一浸出溶液分离,第一浸出溶液用另外的浓缩锌或煅烧物通过焙烧处理,从而溶解锌,并沉淀出大量的溶解铁,从而产生含铁残渣和 含锌的第二浸出溶液。 将含铁残渣与第二浸出溶液分离,并处理第二浸出溶液以回收锌。
    • 4. 发明授权
    • Recovery of metal values from zinc plant residues
    • 从锌植物残渣回收金属价值
    • US5348713A
    • 1994-09-20
    • US929927
    • 1992-08-14
    • Derek E. KerfootMichael J. CollinsMichael E. Chalkley
    • Derek E. KerfootMichael J. CollinsMichael E. Chalkley
    • C22B7/00C22B15/00C22B19/30C22B3/08
    • C22B13/045C22B11/042C22B15/0067C22B19/22C22B19/30C22B7/007Y02P10/214Y02P10/234Y02P10/236
    • A process is disclosed for recovering zinc, lead, copper and precious metals from zinc plant residue, said process comprising leaching the residue with return zinc spent electrolyte, neutralizing residual acid and reducing ferric iron in the solution by addition of zinc sulphide concentrate in the presence of a limited quantity of oxygen, flotation of the resulting slurry to separate unreacted zinc sulphide, treatment of flotation tailings with sulphur dioxide and elemental sulphur to further leach iron, zinc and impurity elements and precipitate copper, flotation of the resulting slurry to separate a copper sulphide concentrate, thickening, filtering and washing of the flotation tailings followed by addition of lime and sodium sulphide to activate lead sulphate and flotation of a lead concentrate from the residue. Iron and impurity elements are precipitated from the copper flotation tailings thickener overflow solution by addition of zinc hydroxide sludge, lime and oxygen to produce a high strength, iron free zinc sulphate solution.
    • 公开了一种用于从锌植物残渣中回收锌,铅,铜和贵金属的方法,所述方法包括用返回的锌废电解液浸出残余物,通过在存在下加入硫化锌浓缩物中和残留酸和还原三价铁,还原三价铁 的有限量的氧气,所得浆料的浮选以分离未反应的硫化锌,用二氧化硫和元素硫处理浮选尾矿以进一步浸出铁,锌和杂质元素并沉淀铜,将所得浆液浮选分离铜 硫化物浓缩物,增稠,过滤和洗涤浮选尾矿,然后加入石灰和硫化钠以活化硫酸铅并从残余物中浮选铅精矿。 通过加入氢氧化锌污泥,石灰和氧气,从铜浮选尾矿增稠剂溢流溶液中沉淀出铁和杂质元素,产生高强度的无铁硫酸锌溶液。