选冶联合处理铜阳极泥高酸高氯废水资源化利用生产实践
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云南铜业股份有限公司西南铜业分公司, 云南 昆明 650102

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李玉东(1987—),男,河南永城人,工程师,主要从事稀贵、稀散金属技术研究及生产管理工作。

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TF811;X758

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Production practice of resourceful utilization of high-acid high-chlorine wastewater from joint mineral processing and metallurgical treatment of copper anode slime
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YCC Southwest Copper Branch, Kunming 650102 , China

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    摘要:

    高酸高氯废水作为选冶联合处理铜阳极泥流程主要外排废水之一,因其高酸度、高氯含量、多杂质等特点,导致其资源化利用率低、处理成本高。通过对阳极泥湿法脱硒原理及生产实践进行分析,探索高酸高氯废水返回湿法脱硒资源化利用的可行性。结果表明,在脱硒料浆浓度1.70~1.80 kg/L,高氯高酸废水用量763 L/槽,工业盐用量50 kg/槽,硫酸用量100 L/釜条件下,可实现脱硒渣含硒2.82%、尾矿含金50 g/t、尾矿含银0.25%、精矿银品位54.04%、高酸废水含铜7.34 g/L、选矿废水含铜0.57 g/L的技术指标,生产指标相对稳定,硒还原后液外排量及硫酸消耗量均得到了降低。

    Abstract:

    The high-acid and high-chlorine wastewater is a major discharged wastewater from the joint mineral processing and metallurgical treatment of copper anode slime and the high acidity, high chlorine content, more impurities and other features result in the low resource recycling and high treatment cost. Through the analysis on the principle and the production practice of wet selenium removal from anode slime, the feasibility of returning the high-acid and high-chlorine wastewater to the wet selenium removal process for resource utilization is explored. The results show that when the concentration of the selenium removal slurry is 1.70-1.80 kg/L the high-chlorine and high-acid wastewater amount is 763 L per tank, the industrial salt consumption is 50 kg per tank and the sulfuric acid consumption is 100 L per kettle, the technical indicators can be achieved that the selenium removed residue contains 2.82% of selenium, the tailing ores contain 50 g/t of gold, the tailing ores contain 0.25% of silver, the concentrate grade is 54.04%, the high acid wastewater contains 7.34 g/L of copper, and the wastewater from mineral processing contains 0.57 g/L of copper. The production indicators are relatively stable and both the discharge of the liquid after selenium reduction and the sulfuric acid consumption are lowered.

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李玉东, 董竞成, 袁瑞. 选冶联合处理铜阳极泥高酸高氯废水资源化利用生产实践[J]. 中国有色冶金, 2022,51(3): 117-120.

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  • 收稿日期:2021-10-12
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  • 在线发布日期: 2025-12-24
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