共查询到16条相似文献,搜索用时 593 毫秒
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针对缅甸某高硫高砷金矿中毒砂和黄铁矿包裹金浸出率低的问题,采用碱浸预处理工艺处理该矿石。确定了磨矿时间、固液比等工艺条件,重点考察预处理过程中的pH、催化剂ZNT用量、时间、氧化剂用量等因素对金浸出率的影响。结果表明,用NaOH调节pH=13,磨矿细度?38 μm含量占90%,再添加10 kg/t催化剂ZNT,40 kg/t氧化剂H2O2,在固液比1:6的条件下预处理12 h,能有效去除包裹金的硫和砷。预处理后的矿样在浸金药剂(1#金虎提金剂) 20 kg/t、矿浆pH=13的条件下浸出24 h,金浸出率提高了近30个百分点。 相似文献
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氰化尾渣还原焙烧酸浸提铁及氰化浸金新工艺 总被引:1,自引:0,他引:1
以氰化尾渣为原料,采用还原焙烧酸浸工艺对其进行处理。当还原温度为850℃、加入煤粉质量为氰化尾渣质量的13%、还原时间为100 min时,对氰化尾渣进行还原,氰化尾渣中Fe2O3转化为Fe3O4或FeO。还原后采用硫酸浸出,当硫酸浓度为50%、硫酸用量系数为1.2、反应温度为105℃、反应时间为3 h时,铁的浸出率达到93.66%。还原焙烧渣在600℃氧化焙烧2 h经过脱碳后氰化浸金,当氰化钠用量为4 kg/t、反应时间为28 h、液固比为2:1时,金的浸出率达到92.4%。经过还原焙烧、硫酸浸出、氧化焙烧及氰化浸金,氰化尾渣渣量减少了38.8%。 相似文献
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难浸砷金精矿的碱性常温常压预氧化 总被引:7,自引:0,他引:7
本文提供了1种难浸金精矿的湿法预氧化新工艺,它包括细磨、强化碱浸预氧化、氰化和炭吸附。在螺旋搅拌式塔式磨浸机中,先将目的难浸金精矿细磨至98%<37μm,然后在40%的矿浆质量浓度、11℃的环境温度和0.1MPa的环境压力下强化碱浸24h,NaOH的消耗量为88kg/t矿,仅为相同氧化率条件下将砷硫氧化成砷酸盐和硫酸盐所需理论碱耗量的30%。预氧化完成后经36h的氰化浸出和炭吸附,金的浸出率从预氧化前的24.6%提高到95.4%,金的吸附率99.2%,NaCN的消耗4kg/t矿。整个提金工艺的成本约300元/t矿。 相似文献
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研究了微波焙烧预处理对微细浸染型难处理金矿浸出的影响。正交试验表明,各因素对浸出率影响程度大小依次为:微波焙烧温度、焙烧时间、浸出时间、浸出剂TY-3用量和氢氧化钠用量。在微波焙烧温度550℃,焙烧时间40 min,浸出剂TY-3用量14 kg/t,氢氧化钠用量8 kg/t,浸出10 h的优化条件下,浸出率达94.8%。XRD分析结果表明,经微波加热焙烧后,原矿中黄铁矿转化为赤铁矿。与马弗炉焙烧对比,微波焙烧可能具有选择性加热作用,更有利于矿石中包裹金的暴露。 相似文献
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对某难处理金精矿进行了热压预氧化-氰化浸金实验,探讨热压预氧化温度、时间、氧化分压和矿浆浓度对金浸出率和氰化钠耗量的影响。结果表明,在粒度-44μm占90.74%、温度220℃、矿浆浓度25%、氧分压0.8 MPa和转速750 r/min条件下预氧化2.5 h,砷主要以稳定的结晶状砷酸铁或者臭葱石形式被固定在氧化渣中;预氧化渣在矿浆浓度33%、pH=10~11、初始氰化钠浓度0.3%和活性炭浓度25 g/L条件下氰化浸出24 h,与金精矿直接氰化相比,浸出率由11.21%提高至95.75%,氰化钠耗量从46.99 kg/t降低至1.36 kg/t。 相似文献
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孟宇群 《中国有色金属学会会刊》2005,15(5):1178-1184
A new hydrometallurgical process for a carbonaceous refractory gold concentrate at ambient temperature and pressure was presented, including grinding-leaching, intensified alkaline leaching(IAL), thiosulfate leaching and cementation by zinc powder. The experimental results show that the grinding-leaching and intensified alkaline leaching process result in the selective oxidation of arsenopyrite and pyrite. The oxidation ratio of As is 96.6%, and 46.7 % for S. The total consumption of NaOH in alkaline leaching is only 28 % of that theoretically calculated under the conditions of full oxidization for the same amount of arsenopyrite and pyrite transforming into arsenates and sulfates, and 83.6% of gold is synchro-dissoluted by thiosulfate self-generated during pretreatment. Since the carbonaceous matter in concentrate possesses a strong capability of preg robbing, the cyanidation process is not suitable for the extraction of gold after pretreatment. However, the gold leaching rate by thiosulfate leaching for 24 h is increased to 91.7% from 0 - 3.2% by ultra-fine grinding without the pretreatment. The recovery of gold by zinc cementation gets to 99.6%. Due to the thiosulfate self-generated during alkaline leaching, the reagent addition in thiosulfate leaching afterwards is lower than the normal one. 相似文献
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难处理金矿加压氧化预处理技术及发展 总被引:3,自引:0,他引:3
难处理金矿由于毒砂和黄铁矿等硫化物的包裹,直接氰化金的回收率很低,为了提高金的浸出率,必须先打破毒砂黄铁矿等的包裹.加压氧化是在高温高压下,在加压釜中由氧气作氧化剂氧化硫化物,破除硫化物对金的包裹,使金能直接与氰化物接触,提高金的浸出率.该工艺具有反应快、金的回收率高、环保等优点,近年来已成为难处理金矿的一种重要预处理工艺. 相似文献
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Marja Riekkola-Vanhanen Ph.Lic. Seppo Heimala D.Sc. Carita A. Sivelä M.Sc. Felipe Viguera M.Sc. Irma Varjola M.Sc. Seppo I. Niemelä Ph.D. Olli H. Tuovinen Ph.D. 《JOM Journal of the Minerals, Metals and Materials Society》1993,45(12):51-53
The oxidation of an auriferous pyrite ore sample was evaluated in biological leaching experiments for subsequent gold recovery via cyanidation. In batch cultures, organisms derived from the mine site oxidized pyrite and ferrous iron at pH values as low as pH 0.6. The recovery of gold was variable in shake flask experiments. In stirred tank bioreactor leaching, gold recovery was proportional to the extent of iron dissolution by bioleaching. The leaching of arsenic from the sample was also directly proportional to iron dissolution. 相似文献