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Pivi H‐M Kinnunen Jaakko A Puhakka 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2004,79(8):830-834
The effects of chloride ions on chalcopyrite leaching by biologically‐produced ferric sulfate solution and on the iron‐oxidizing culture were determined. Chloride ions significantly increased chalcopyrite leaching by ferric sulfate at 67 °C and 87 °C, but slowed down the leaching at 50 °C. At 90 °C, chloride at 5 g dm?3 (0.25 g Cl? g?1 concentrate) increased the copper yield from 60 to 100% in approximately 2 weeks. Further increase in Cl? concentration did not affect the leaching. Addition of chloride increased both leaching yields and iron precipitation, which shows that the passivation was not due to iron precipitation. A decreased Ag‐potential of 60 mV against an Ag/AgCl reference electrode in the presence of Cl? indicates the accumulation of partially oxidized forms of dissolved sulfur compounds such as thiosulfate and polythionate instead of elemental sulfur and, thus, a decrease in sulfur passivation. A chloride concentration of 5 g dm?3 did not affect the iron oxidation rate of the iron‐oxidizing culture dominated by Leptospirillum ferriphilum. Copyright © 2004 Society of Chemical Industry 相似文献
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尾砂中含有大量的金属,是一种潜在的可利用资源。旨在研发一种从铜尾砂中回收铜的生物浸出方法。利用正交设计,通过摇瓶试验,研究培养温度、发酵时间、接种量及培养基成分对黑曲霉菌丝球形态的影响,进而研究不同菌丝球形态的黑曲霉发酵液对尾砂中铜的浸出。研究表明,铜的浸出率随着黑曲霉菌丝球直径的减小而升高。在温度30℃,接种量0.8%(OD600=0.1),马铃薯-蔗糖含量30%,发酵时间65 h的优化发酵条件下,获得大量表面光滑、直径为0.96 mm的菌丝球;利用该条件下的发酵液,在30℃,180 r·min-1条件下浸出3 d,铜的浸出率达83.25%。 相似文献
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研究了在Fe2(SO4)3-H2SO4-NaCl体系中直接电解浸出黄铜矿精矿工艺条件及机理。实验表明,在阳极初始溶液含Fe^3+1mol/L,H2SO4 4mol/L,NaCl1.5mol/L,阴阳极电流密度分别为350和650A/m^2,温度368K的条件下浸出6h,可以获得铜浸出率为95%,精矿中的硫90%以上以单质硫回收。温度是影响铜浸出率最显著的因素,阳极上发生的主要反应是Fe^3+氧化;硫酸铁直接氧化黄铜矿得到单质硫;酸分解黄铜矿产生H2S,H2S溶解后再被Fe^3+氧化为硫。 相似文献
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The experiments of agitation leaching were carried out in aqueous ammonia/ammonium carbonate solution, to recover copper from the flotation tailings of waste copper oxide residue. The main copper minerals contained in the flotation tailings are chrysocolla, malachite, and cuprite, with the copper grade of 1.12%. Effects of lixiviant concentration, solid‐to‐liquid ratio, stirring speed, and reaction temperature on copper leaching ratios at various time were investigated. It is found that the leaching ratio almost cannot be affected by time after 90 min of leaching. The optimised processing conditions have been determined, under which the leaching ratio of 70.6% is obtained. Kinetics analysis indicates that the copper leaching ratio is controlled by diffusion through the product layer in the initial 60 min of leaching, and corresponding measures to strengthen the copper extraction is proposed, with the activation energy of 32.3 kJ/mol. © 2012 Canadian Society for Chemical Engineering 相似文献
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采用酸浸法提取硫铁矿尾矿中有价元素铜。研究了硫酸质量分数、浸出时间、矿石粒度、矿石投加量、浸出温度和转速对铜浸出的影响。在单因素实验的基础上,采用正交实验法对浸出工艺条件进行优化。采用扫描电镜(SEM)和能谱仪(EDS)对酸浸前后尾矿表面的微观形貌进行了分析,初步探讨了酸浸反应后期抑制Cu浸出的影响机制。结果表明,酸浸铜的最佳工艺条件为:硫酸质量分数30%、浸出时间6 h、矿石粒度150 ?m、矿石用量5 g、浸出温度108℃、转速440 r/min,在此条件下,铜的浸出率为50.68%。扫描电镜和能谱分析表明,浸出残渣表面被微米级的二氧化硅颗粒紧密包裹,钝化了后期的浸出反应。 相似文献
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对碳酸铜矿中铜、钴浸出过程的反应及行为进行了分析。在大量实验的基础上,结合理论分析,探讨了浸出条件对矿样中钴选择性浸出的影响,进而确定了钴选择性浸出的实验室最佳条件为:浸出时间3 h,浸出温度70℃以上,pH为5,液固体积比为5∶1,浸出液中添加质量浓度为27.11 g/L的硫酸铜溶液1.5 mL。实验结果表明,该条件下钴的浸出率可达到78.37%,铜的浸出率仅为0.04%,实现了钴与铜的有效分离,可以优先浸出钴,实现钴资源的充分利用。 相似文献
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Ammoniacal leaching and sulfuric acid leaching were explored separately to recover copper from smelter slag. The overall 75% copper recovery was achieved from the smelter slag under optimum condition using ammoniacal leaching. The low copper recovery in this process is directly related to the complex slag mineralogy and dissolution kinetics. To overcome such problems, sulfuric acid leaching was applied separately. This method provided an overall 89% copper recovery under atmospheric condition. The use of sulfuric acid as the leaching agent was found to be more advantageous than ammonia due to the complex interlocking nature of copper bearing particles and different reaction kinetics of the slag. 相似文献
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为了分析外界因素对制备聚合硫酸铁的影响,开展了不同条件下的酸浸还原实验和聚合合成实验,优化了实验条件,进而分析不同pH、不同絮凝剂用量以及不同沉降时间作用下,聚合硫酸铁对污染水的处理效果。结果表明:酸浸实验中尾矿全铁浸出实验的最佳温度为100 ℃,最佳搅拌时间为2 h,最佳搅拌速度为300 r/min;还原试验中硫酸亚铁还原率的最佳还原温度为60 ℃,最佳还原时间为1.5 h,还原铁粉的过量系数为1.10%。聚合合成实验中最佳聚合温度为35 ℃,最佳聚合时间为0.4 h;此条件下,n(双氧水)∶n(Fe2+)∶n(磷酸钠)为0.08∶1∶0.07时,聚合效果最优。在pH为7中性环境中,聚合硫酸铁的质量浓度为2.0 g/mL,沉降时间为0.3 h时,污水的余浊值最小,对于污水的处理效果最好。 相似文献
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基于机械活化原理对铜尾矿性能进行了试验研究,结果表明粉磨10 min的铜尾矿掺入水泥后,水泥标准稠度需水量随着掺加量的增加而减小,继续延长粉磨时间水泥标准稠度需水量随着掺量增加而增加,而粉磨时间对掺有铜尾矿的水泥凝结时间几乎没有影响。在12%~16%范围内,延长粉磨时间对铜尾矿28 d活性指数较为有利,其余掺量并不明显,并且掺入铜尾矿的水泥流动性损失加剧。 相似文献
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为了充分利用低品位铜矿,大树硫铁矿采用微生物浸出的工艺在小规模的工业生产中获得了铜的浸出率达85%的指标,为有效地利用低品位铜矿和大规模工业生产创造了条件。 相似文献
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通过改进的两次盐酸浸取法将毒重石尾矿钡渣中的钡转化为氯化钡实现二次回收,考察了包括液固比、盐酸浓度、浸取时间、浸取温度等因素对除杂提钡效果的影响。实验结果表明,第一步盐酸洗渣能将铁、钙、锶等杂质酸化为相应的氯盐,并将其大部分转入液相,所得含钡滤渣进行第二步盐酸浸取,得氯化钡溶液。实验优化工
艺条件:第一步盐酸洗渣,液固质量比为1∶2,盐酸浓度为1 mol/L;第二步盐酸浸取,液固质量比为7∶1,盐酸浓度为
2 mol/L,浸取时间为2 h,浸取温度为70 ℃,钡的回收率可达95%;第三步氯化钡粗品精制,用草酸进一步沉淀钙、锶,调节滤液pH为3,滤液蒸发浓缩结晶,晶体经无水乙醇洗涤后烘干,所得氯化钡产品纯度可达99.9%。 相似文献