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有色金属(冶炼部分):2011,(10):13-16
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硫化铅精矿氯化浸出新工艺研究
(沈阳有色金属研究院)
Study on Chlorination Leaching New Technology for Lead Sulphide Concentrate
(Shenyang Research Institute of Nonferrous Metals)
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投稿时间:2011-02-25               
中文摘要: 研究了硫化铅精矿在盐酸—氧气体系中的氯化浸出过程。重点考察了各种参数对硫化铅精矿中铅和银浸出效果和硫在浸出渣中富集率的影响。结果表明,硫化铅精矿在氯化镁溶液中的浸出效果优于氯化钠溶液,在催化剂铜离子浓度为1.45 g/L、盐酸用量为理论量1.5倍、氧气流量40 mL/min、氯化镁浓度5.5 mol/L、浸出温度90 ℃、浸出时间7 h、液固比6∶1的条件下,铅和银的浸出率分别达到99.11%和90.57%,硫富集率为90.12%。
Abstract:Chlorination leaching process of lead sulphide concentrate in hydrochloric acid-oxygen system was studied. A variety of parameters on the effect of lead and silver leaching rate and enriching rate of sulfur in leaching residue were investigated. The results indicate that the leaching effect of lead sulphide concentrate in magnesium chloride solution is superior to that in sodium chloride solution. Lead and silver leaching rate achieved 99.11%, 90.57% respectively, and enriching rate of sulphur is 90.12% under the optimum parameters that catalyst copper ion concentration is 1.45 g/L, hydrochloric acid dosage is 1.5 times to theoretical quantity, oxygen flow is 40 mL/min, magnesium chloride concentration is 5.5 mol/L, leaching temperature is 90 ℃, leaching time is 7 hours, ratio of liquid to solid is 6∶1.
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引用文本:
李淑梅,张福生,丛自范.硫化铅精矿氯化浸出新工艺研究[J].有色金属(冶炼部分),2011(10):13-16.
LI Shu-mei,ZHANG Fu-sheng,CONG Zi-fan.Study on Chlorination Leaching New Technology for Lead Sulphide Concentrate[J].Nonferrous Metals (Extractive Metallurgy),2011(10):13-16.

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