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    • 6. 发明授权
    • Recovery of gold from refractory auriferous iron-containing sulphidic ore
    • 从难熔含铁含铁硫化矿中回收金
    • US4571264A
    • 1986-02-18
    • US707923
    • 1985-03-04
    • Donald R. WeirRoman M. Genik-Sas-Berezowsky
    • Donald R. WeirRoman M. Genik-Sas-Berezowsky
    • C22B11/00C22B20060101C22B1/10C22B3/00C22B3/04C22B3/08C22B3/20C22B11/08C22B11/04
    • C22B3/08C22B11/04Y02P10/234
    • A process for recovering gold from refractory auriferous iron-containing sulphidic ore which comprises feeding ground ore as an aqueous slurry to an acidic pretreatment step. The ground ore in the acidic pretreatment step is treated with aqueous sulphuric acid solution to decompose carbonate and acid consuming gangue compounds, and subjecting the treated slurry to a first liquid-solids separation step to produce a sulphate solution and separated solids. Water is added to the separated solids in a first repulping step to form a slurry having a pulp density in the range of from about 25 to about 60% by weight solids. The first repulped slurry is oxidized in a pressure oxidation step at a temperature in the range of from about 135.degree. to about 250.degree. C. under a pressurized oxidizing atmosphere while maintaining a free acid concentration of from about 5 to 40 g/L sulphuric acid to cause dissolution of iron, formation of sulphuric acid and oxidation of substantially all oxidizable sulphide compounds to sulphate form with less than about 20% of oxidized sulphur being present as elemental sulphur during the oxidation step. Water is added to the oxidized slurry in a seocnd repulping step to produce a repulped oxidized slurry with a pulp density in the range of from about 5 to 15% by weight, and subjecting the repulped oxidized slurry to a second liquid-solids separation step to produce an acid and iron containing solution and oxidized separated solids. The acid and iron containing solution is recycled to at least one of the first and second repulping steps.
    • 一种从难熔含铁含铁硫化矿石中回收金的方法,包括将研磨矿石作为含水浆料进料至酸性预处理步骤。 酸性预处理步骤中的研磨矿石用硫酸水溶液处理以分解碳酸盐和酸消耗的脉石化合物,并将经处理的浆料进行第一液固固体分离步骤以产生硫酸盐溶液并分离固体。 在第一再制浆步骤中将水加入到分离的固体中,以形成浆料,浆料的固体重量为约25至约60重量%。 在压力氧化步骤中,在加压氧化气氛下,在约135℃至约250℃的温度范围内,将第一个再浆化浆料氧化,同时保持约5至40g / L硫酸的游离酸浓度 导致铁的溶解,硫酸的形成和基本上所有可氧化的硫化物化合物氧化成硫酸盐形式,在氧化步骤期间以小于约20%的氧化的硫作为元素硫存在。 在再造浆步骤中将水加入到氧化浆料中,以产生纸浆密度在约5至15重量%范围内的再浆化的氧化浆料,并将再淤化的氧化浆料进行第二液 - 固分离步骤 产生含酸和铁的溶液和氧化的分离固体。 将含酸和铁的溶液再循环至第一和第二再制浆步骤中的至少一个。
    • 8. 发明授权
    • Separation of cobalt and nickel by oxidative precipitation with
peroxymonosulfuric acid
    • 用过氧单硫酸氧化沉淀分离钴和镍
    • US4394357A
    • 1983-07-19
    • US321575
    • 1981-11-16
    • Diana M. MounseyDavid B. Mobbs
    • Diana M. MounseyDavid B. Mobbs
    • B01D20060101C01G20060101C01G51/00C01G51/04C01G53/00C01G53/10C07F15/04C22B20060101C22C19/00C25C1/20
    • C22B23/0484
    • The invention relates to the preferential precipitation of cobalt from aqueous acidic sulphate solutions of nickel and cobalt.The separation is carried out by introducing at least a stoichiometric amount of Caro's Acid containing no more than a small amount of hydrogen peroxide into the nickel/cobalt solution progressively over a period of at least an hour, while maintaining the solution of a pH from 3.1 or 3.5 up to 4.7 by addition of an alkali metal hydroxide carbonate or bicarbonate, or at 4.3 to 4.7 with the corresponding ammonium compound, and, thereafter separating the precipitate from the aqueous cobalt depleted solution.In preferred features, the Caro's Acid solution used contains hydrogen peroxide in a mole ratio to peroxomonosulphuric acid of not more than 1:10; the Caro's Acid solution is introduced continuously or in increments of less than 1% of the total over a period of at least an hour; the Caro's Acid is produced by reaction between 93-98% sulphuric acid and 65-72% aqueous hydrogen peroxide in a mole ratio of 2.7:1 to 3.5:1; the Caro's Acid solution is diluted before use; and particular amounts of Caro's Acid are used depending upon the nature of the nickel/cobalt solution, the mode of treatment, and the nature of the neutralizing agent. Further separation can be effected by subsequent water and particularly not acid washing of the precipitate.
    • 本发明涉及钴从镍和钴的酸性硫酸盐水溶液中优先沉淀。 通过在至少1小时的时间内将至少含有不超过少量过氧化氢的化学计量量的Caro酸向镍/钴溶液中逐渐引入,同时保持pH为3.1的溶液来进行分离 或通过加入碱金属氢氧化物碳酸盐或碳酸氢盐,或在4.3至4.7℃下加入相应的铵化合物,然后从含钴贫化溶液中分离出沉淀物,3.5至4.7。 在优选的特征中,所用Caro's酸溶液含有与过氧二硫酸的摩尔比不大于1:10的过氧化氢; Caro酸溶液在至少一小时内持续或以小于总量的1%的增量引入; 卡罗酸是通过93-98%硫酸和65-72%过氧化氢水溶液之间的摩尔比为2.7:1至3.5:1的反应产生的; 使用前将Caro's Acid溶液稀释; 并且根据镍/钴溶液的性质,处理方式和中和剂的性质,使用特定量的Caro酸。 进一步的分离可以通过随后的水进行,特别是不是酸洗该沉淀物。
    • 9. 发明授权
    • Metal recovery process from aluminum dross
    • 铝浮渣的金属回收工艺
    • US4386956A
    • 1983-06-07
    • US212408
    • 1980-12-03
    • David J. RothLawrence R. CullerRalph D. Heifner
    • David J. RothLawrence R. CullerRalph D. Heifner
    • C22B7/00C22B20060101C22B7/04C22B15/00C22B21/00
    • C22B7/04C22B21/0069C22B21/0092Y02P10/218
    • An improved method for recovery of metal, particularly aluminum, from metal bearing dross utilizes a trough for collection of the dross. A wedge member compresses the dross in the trough. In this manner, metal is decanted from the compressed dross and flows through slots in the bottom or passages in the walls of the trough for collection in a pan, or becomes concentrated at the edges or walls of the volume of dross. The trough and wedge members also serve to cool the dross material thereby diminishing metal loss due to thermite reaction. The compressed dross coalesces and solidifies, is broken and is mechanically separated. The larger dross components from the separation process are substantially metallic and may be recycled through the furnace. The remaining components are charged in a vortex melting furnace for the lowest possible melt loss. This also effects segregation of the remaining metal from the dross by melting the metal and allowing the dross to rise to the top of the bath. The improved method of the present invention provides for recovery of about 95% of aluminum metal from a dross which contains about 70% aluminum as compared with a recovery rate of about 50% aluminum metal utilizing a generally known prior art technique.
    • 从金属轴承浮渣回收金属,特别是铝的改进方法利用了用于收集浮渣的槽。 楔形件压缩槽中的浮渣。 以这种方式,金属从压缩浮渣中倾出并流过槽底部的狭槽或槽的通道,用于收集在锅中,或者在渣槽的边缘或壁处集中。 槽和楔形构件还用于冷却浮渣材料,从而减少由于铝热反应引起的金属损失。 压缩的浮渣聚结并固化,破碎并机械分离。 来自分离过程的较大的浮渣组分基本上是金属的,并且可以通过炉再循环。 将其余组分装入涡流熔融炉中以获得尽可能低的熔体损失。 这也通过熔化金属并使浮渣上升到浴的顶部来实现残留的金属与浮渣的分离。 本发明的改进方法提供了使用通常已知的现有技术的技术,与含有约70%铝的浮渣相比,回收约95%的铝金属。
    • 10. 发明授权
    • Recovery of cobalt values
    • 回收钴价值
    • US4261737A
    • 1981-04-14
    • US89837
    • 1979-10-31
    • James A. BradburyRichard T. Um
    • James A. BradburyRichard T. Um
    • C22B15/00B01D15/00C22B20060101C22B1/00C22B3/00C22B3/24C22B7/00C22B23/00C22B47/00C22B23/04
    • C22B3/24Y02P10/234
    • The present process involves an improvement in the hydrometallurgical recovery of metal values from metal bearing sources such as ores and the like. The desired metal values are recovered by subjecting a metal bearing source to a reductive roast in a reducing atmosphere after having treated said source with at least one additive. Following the reductive roast the reduced metal bearing source is cooled and extracted by a leaching operation. The separation of various metal values in the metal bearing source may be effected by adding a solid adsorbent to the leach solution whereby selective metal ions are adsorbed thereon. The improvement in the present process comprises pretreating the solid adsorbent prior to use thereof with an acid thereby increasing the loading capacity of the metal ions in the adsorbents as well as kinetics of metal adsorption.
    • 本发明的方法涉及从诸如矿石等金属轴承来源改进金属值的湿法冶金回收。 在用至少一种添加剂处理所述源之后,通过使金属轴承源在还原性气氛中经受还原性焙烧来回收所需的金属值。 还原烘烤后,还原金属轴承源被冷却并通过浸出操作提取。 金属轴承源中各种金属值的分离可以通过向浸出溶液中加入固体吸附剂来实现,其中选择性金属离子被吸附在其上。 本方法的改进包括在使用之前用酸预处理固体吸附剂,从而增加吸附剂中金属离子的负载能力以及金属吸附的动力学。