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    • 1. 发明授权
    • Recovery of non-ferrous metals by thermal treatment of solutions
containing non-ferrous and iron sulphates
    • 通过热处理含有铁和硫酸铁的溶液回收有色金属
    • US4415540A
    • 1983-11-15
    • US346837
    • 1982-02-08
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • C01G9/06C22B1/10C22B3/08C22B3/22C22B15/00
    • C22B3/22C22B1/10C22B15/0017C22B15/0071C22B15/0082C22B15/0086C22B19/22C22B3/08Y02P10/234Y02P10/236Y10S423/02Y10S423/16
    • The specification discloses a method for recovering non-ferrous metals such as zinc or copper iron from their concentrates, ores or any other metal containing materials into a solution containing these non-ferrous metals as sulphates and a minimal amount of dissolved iron. The resultant solution is suited without or with minimum pre-purification treatment for conventional electrowinning processes to recover such non-ferrous metals with less difficulties than the previous methods involving complex iron-removal processing. There is disclosed a method for recovering at least one non-ferrous metal soluble in sulphuric acid from a strong sulphuric acid solution containing said metal and iron as sulphates, said method comprising the following consecutive steps:subjecting said solution in a sub-divided form to thermal decomposition in a fluidized bed reactor at a temperature of from 600.degree. to 750.degree. C. with 20-150% excess air for an average retention time of 1-12 hours to obtain calcine containing ferric oxide and the sulphate of said non-ferrous metal;leaching said non-ferrous metal sulphate out from said calcine with water or dilute sulphuric acid solutions;separating said leach solution containing said non-ferrous metal sulphate from the residue; andrecovering said non-ferrous metal from said leach solution, via electrolysis or any other method.
    • 本说明书公开了一种从其浓缩物,矿石或任何其它含金属材料中回收有色金属如锌或铜铁的方法,该方法含有这些有色金属作为硫酸盐和最少量的溶解铁。 所得到的溶液适合于没有或具有最少的预纯化处理用于常规电解沉积方法以回收这种有色金属,而不是先前涉及复杂除铁处理的方法的困难。 公开了一种从硫酸盐中含有所述金属和铁的强硫酸溶液中回收至少一种可溶于硫酸的有色金属的方法,所述方法包括以下连续步骤:将分解形式的所述溶液 在流化床反应器中在600至750℃的温度下用20-150%过量的空气进行热分解,平均保留时间为1-12小时,得到含有氧化铁和所述有色金属硫酸盐的煅烧物 金属; 用水或稀硫酸溶液从所述煅烧物中浸出有色金属硫酸盐; 从残留物中分离含有所述有色金属硫酸盐的所述浸出溶液; 并通过电解或任何其他方法从所述浸出溶液中回收所述有色金属。
    • 2. 发明授权
    • Recovery of copper from copper sulfide ores containing copper and iron
    • 从含铜和铁的硫化铜矿中回收铜
    • US4003740A
    • 1977-01-18
    • US646807
    • 1976-01-06
    • Dale K. HugginsLowell R. AndersonFred J. Gefri
    • Dale K. HugginsLowell R. AndersonFred J. Gefri
    • C22B15/00C22B15/08
    • C22B15/0071C22B15/0006C22B15/0017C22B15/0082Y02P10/236
    • The invention provides a cyclic process for recovering copper from sulfide ores containing copper and iron which comprises reacting the sulfide ore with sulfur dioxide gas at a temperature of at least about 500.degree. C. to form elemental sulfur, removing the elemental sulfur, reacting the residual solids with concentrated sulfuric acid at a temperature of about 180.degree. to 500.degree. C. to form copper sulfate and sulfur dioxide gas, recycling the sulfur dioxide gas for reaction with additional ore, roasting the remaining solids at a temperature of about 400.degree. C. to 900.degree. C., leaching the roasted solids with an aqueous solution to solubilize the copper sulfate and recovering copper from the solubilized copper sulfate. In another embodiment of the invention, the roasting step is eliminated by removing magnetite from the solids remaining after removal of the elemental sulfur.
    • 本发明提供一种循环方法,用于从含有铜和铁的硫化矿中回收铜,该方法包括在至少约500℃的温度下使硫化矿与二氧化硫气体反应,形成元素硫,除去元素硫, 用浓硫酸在约180℃至500℃±20℃的温度下固体固体,形成硫酸铜和二氧化硫气体,再循环二氧化硫气体与另外的矿石反应,在约400℃的温度下焙烧剩余的固体 ℃至900℃,用水溶液浸提焙烧固体,溶解硫酸铜并从溶解的硫酸铜中回收铜。 在本发明的另一个实施方案中,通过从除去元素硫后残留的固体除去磁铁矿来消除焙烧步骤。
    • 6. 发明授权
    • Recovery of non-ferrous metals by thermal treatments of solutions
containing non-ferrous and iron sulphates
    • 通过热处理含有铁和硫酸铁的溶液回收有色金属
    • US4317803A
    • 1982-03-02
    • US189249
    • 1980-09-22
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • C22B1/10C22B3/00C22B3/08C22B3/22C22B15/00C01G9/06
    • C22B15/0086C22B1/10C22B15/0017C22B15/0071C22B15/0082C22B19/22C22B3/08C22B3/22Y02P10/216Y02P10/234Y02P10/236Y10S423/02Y10S423/16
    • The specification discloses a method for recovering non-ferrous metals such as zinc or copper from their concentrates, ores or any other metal containing materials into a solution containing these non-ferrous metals as sulphates and a minimal amount of dissolved iron. The resultant solution is suited without or with minimum pre-purification treatment for conventional electrowinning processes to recover such non-ferrous metals with less difficulties than the previous methods involving complex iron-removal processing. There is disclosed a method for recovering at least one non-ferrous metal soluble in sulphuric acid from a strong sulphuric acid solution containing said metal and iron as sulphates, said method comprising the following consecutive steps:subjecting said solution in a sub-divided form to thermal decomposition in a fluidized bed reactor at a temperature of from 600.degree. to 750.degree. C. with 20-150% excess air for an average retention time of 1-12 hours to obtain calcine containing ferric oxide and the sulphate of said non-ferrous metal;leaching said non-ferrous metal sulphate out from said calcine with water or dilute sulphuric acid solutions;separating said leach solution containing said non-ferrous metal sulphate from the residue; andrecovering said non-ferrous metal from said leach solution, via electrolysis or any other method.
    • 本说明书公开了一种从其浓缩物,矿石或任何其它含金属材料中回收含有金属如锌或铜的有色金属成为含有这些有色金属作为硫酸盐和少量溶解铁的溶液的方法。 所得到的溶液适合于没有或具有最少的预纯化处理用于常规电解沉积方法以回收这种有色金属,而不是先前涉及复杂除铁处理的方法的困难。 公开了一种从硫酸盐中含有所述金属和铁的强硫酸溶液中回收至少一种可溶于硫酸的有色金属的方法,所述方法包括以下连续步骤:将分解形式的所述溶液 在流化床反应器中在600至750℃的温度下用20-150%过量的空气进行热分解,平均保留时间为1-12小时,得到含有氧化铁和所述有色金属硫酸盐的煅烧物 金属; 用水或稀硫酸溶液从所述煅烧物中浸出有色金属硫酸盐; 从残留物中分离含有所述有色金属硫酸盐的所述浸出溶液; 并通过电解或任何其他方法从所述浸出溶液中回收所述有色金属。
    • 7. 发明授权
    • Recovery of non-ferrous metals by thermal treatment of solutions
containing non-ferrous and iron sulphates
    • 通过热处理含有铁和硫酸铁的溶液回收有色金属
    • US4224122A
    • 1980-09-23
    • US940937
    • 1978-09-11
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • Igor A. E. WilkomirskyRoy S. BoormanRobert S. Salter
    • C22B19/00C22B1/00C22B1/02C22B1/10C22B3/00C22B3/04C22B3/08C22B3/20C22B3/22C22B15/00C22B19/20C25C1/16C01G9/06
    • C22B15/0071C22B1/10C22B15/0017C22B15/0082C22B15/0086C22B19/22C22B3/08C22B3/22Y02P10/216Y02P10/234Y02P10/236Y10S423/02Y10S423/16
    • The specification discloses a method for recovering non-ferrous metals such as zinc or copper from their concentrates, ores or any other metal containing materials into a solution containing these non-ferrous metals as sulphates and a minimal amount of dissolved iron. The resultant solution is suited without or with minimum pre-purification treatment for conventional electrowinning processes to recover such non-ferrous metals with less difficulties than the previous methods involving complex iron-removal processing. There is disclosed a method for recovering at least one non-ferrous metal soluble in sulphuric acid from a strong sulphuric acid solution containing said metal and iron as sulphates, said method comprising the following consecutive steps:subjecting said solution in a sub-divided form to thermal decomposition in a fluidized bed reactor at a temperature of from 600.degree. to 750.degree. C. with 20-150% excess air for an average retention time of 1-12 hours to obtain calcine containing ferric oxide and the sulphate of said non-ferrous metal;leaching said non-ferrous metal sulphate out from said calcine with water or dilute sulphuric acid solutions;separating said leach solution containing said non-ferrous metal sulphate from the residue; andrecovering said non-ferrous metal from said leach solution, via electrolysis or any other method.
    • 本说明书公开了一种从其浓缩物,矿石或任何其它含金属材料中回收含有金属如锌或铜的有色金属成为含有这些有色金属作为硫酸盐和少量溶解铁的溶液的方法。 所得到的溶液适合于没有或具有最少的预纯化处理用于常规电解沉积方法以回收这种有色金属,而不是先前涉及复杂除铁处理的方法的困难。 公开了一种从硫酸盐中含有所述金属和铁的强硫酸溶液中回收至少一种可溶于硫酸的有色金属的方法,所述方法包括以下连续步骤:将分解形式的所述溶液 在流化床反应器中在600至750℃的温度下用20-150%过量的空气进行热分解,平均保留时间为1-12小时,得到含有氧化铁和所述有色金属硫酸盐的煅烧物 金属; 用水或稀硫酸溶液从所述煅烧物中浸出有色金属硫酸盐; 从残留物中分离含有所述有色金属硫酸盐的所述浸出溶液; 并通过电解或任何其他方法从所述浸出溶液中回收所述有色金属。