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    • 3. 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。
    • 5. 发明授权
    • Recovery of zinc from zinc containing sulphidic materials
    • 从含锌硫化物材料中回收锌
    • US4443253A
    • 1984-04-17
    • US417829
    • 1982-09-14
    • Donald R. WeirIan M. Masters
    • Donald R. WeirIan M. Masters
    • C22B19/00C01B17/027C01G5/00C01G21/00C22B20060101C22B3/00C22B3/04C22B19/20
    • C22B19/26C22B19/22Y02P10/234
    • A process for recovering zinc from zinc-containing sulphidic material also containing iron and from zinc oxide containing material. Zinc-containing sulphidic material is leached 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 an initial stoichiometric excess of sulphuric acid relative to the zinc content of the sulphidic material to form a leach slurry containing dissolved zinc and iron. The leach step is continued until a substantial amount of zinc has been dissolved from the sulphidic material. Zinc oxide containing material is then added to the leach slurry to raise the pH of the slurry to a value in the range of from about 4.5 to about 5.5 to precipitate dissolved iron and form an iron-containing residue and a relatively iron-free leach solution. The residue is separated from the leach solution, and the leach solution is treated to recover zinc.
    • 还含有铁和含氧化锌的材料的含锌硫化物材料中回收锌的方法。 含锌硫化物材料在氧化条件下在约130至约170℃的温度范围内,在硫酸水溶液中浸出,其中初始化学计量过量的硫酸相对于硫化物材料的锌含量至 形成含有溶解的锌和铁的浸出浆料。 浸出步骤持续进行,直到大量锌从硫化物质中溶解出来。 然后将含氧化锌的材料加入浸出浆料中以将浆料的pH升高至约4.5至约5.5的范围,以沉淀溶解的铁并形成含铁残渣和相对无铁的浸出溶液 。 将残余物与浸出溶液分离,并将浸出溶液处理以回收锌。
    • 9. 发明授权
    • Recovery of zinc from zinc-containing sulphidic material
    • 从含锌硫化物质中回收锌
    • US4832925A
    • 1989-05-23
    • US514733
    • 1983-07-18
    • Donald R. WeirIan M. MastersBarry N. Doyle
    • Donald R. WeirIan M. MastersBarry N. Doyle
    • C22B19/00C22B11/02C22B13/02C22B19/20
    • C22B11/021C22B13/02C22B19/22Y02P10/214Y02P10/234
    • A process for the recovery of zinc from zinc-containing sulphidic material which also contains iron and from zinc oxide containing material, at least one of the materials containing lead and/or silver values. The process includes leaching zinc-containing sulphidic material and zinc oxide containing material under pressurized 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 the materials of from about 40 to about 100% to produce a residue containing a major proportion of lead and/or silver values and a leach solution containing a major proportion of the zinc and iron. The residue is separated from the leach solution and treated to recover lead and/or silver values. The pH of the solution is then raised to neutralize the acid in an iron removal step to cause precipitation of at least some of the dissolved iron from the leach solution as an iron compound. The precipitated iron compound is separated from the remaining leach solution, and the remaining leach solution is treated to recover zinc.
    • 还含有铁和含氧化锌的材料的含锌硫化物材料回收锌的方法,含有铅和/或银的材料中的至少一种材料。 该方法包括在加氢氧化条件下,在约130℃至约170℃的温度范围内,在含硫化学计量过量的硫酸溶液中,将含锌硫化物材料和含氧化锌的物质相对于 材料的锌含量为约40至约100%,以产生含有主要比例的铅和/或银值的残渣和含有主要比例的锌和铁的浸出溶液。 将残余物与浸出溶液分离并处理以回收铅和/或银值。 然后在铁去除步骤中升高溶液的pH以中和酸,以使作为铁化合物的浸出溶液中的至少一些溶解的铁沉淀。 将沉淀的铁化合物与剩余的浸出溶液分离,并处理剩余的浸出溶液以回收锌。
    • 10. 发明授权
    • Recovery of zinc from zinc containing sulphidic material
    • 从含锌硫化物材料中回收锌
    • US4505744A
    • 1985-03-19
    • US508699
    • 1983-06-28
    • Donald R. WeirIan M. MastersGerald L. Bolton
    • Donald R. WeirIan M. MastersGerald L. Bolton
    • C22B11/00C22B13/00C22B19/00C22B19/20C25C1/16C01B17/02C01G5/00C01G21/00
    • C25C1/16C22B19/22C22B19/26Y02P10/234
    • A process for recovering zinc from zinc-containing sulphidic material which also contains iron and lead includes leaching the material under oxidizing conditions at a temperature in the range of from about 130.degree. to about 155.degree. C. in aqueous sulphuric acid solution with a stoichiometric excess of sulphuric acid relative to the zinc content of the material of from about 50 to about 100% to produce an undissolved residue containing a major proportion of the lead and a leach solution containing a major proportion of the zinc and iron. The sulphur and lead containing residue is separated from the zinc and iron containing leach solution. Elemental sulphur is physically separated from the remaining lead-containing residue, and the remaining lead-containing residue is recovered. The zinc and iron containing leach solution is treated to recover zinc by feeding the solution to another process in which zinc-containing material is treated to recover zinc and which includes an iron-precipitation step.
    • 从含有铁和铅的含锌硫化物中回收锌的方法包括在氧化条件下将物料在约130至约155℃的温度范围内,在硫酸水溶液中浸出,其化学计量过量 的硫酸相对于材料的锌含量为约50至约100%,以产生含有主要比例的铅的未溶解残余物和含有主要比例的锌和铁的浸出溶液。 含硫和含铅残渣与含锌和铁的浸出溶液分离。 将元素硫与剩余的含铅残渣物理分离,并回收剩余的含铅残渣。 处理含锌和铁的浸出溶液以通过将溶液进料到另一种处理含锌材料以回收锌并且包括铁沉淀步骤的方法来回收锌。