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含Ni^(2+),Fe^(3+),Mg^(2+)的硫酸盐溶液萃取分离Cu^(2+) 被引量:3

Extraction Cu^(2+) via sulfates solution containing Fe^(3+),Mg^(2+) and Ni^(2+)
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摘要 采用Lix984作萃取剂,煤油作稀释剂混合而成溶液萃取的有机相,从含Ni^(2+),Fe^(3+),Mg^(2+)离子的硫酸盐溶液中萃取分离Cu^(2+).实验结果表明,在一定范围内,铜萃取率随萃取剂浓度的升高、相比的增加、萃取时间的延长、初始水相pH值的增加、萃取温度的升高以及搅拌时间的延长而增加.本实验的优化条件为萃取剂体积分数达60%,相比为O∶A=2∶1,萃取时间为16 min,萃取初始水相pH值为2.5,萃取温度在25~45℃之间,搅拌速度为240 r/min.在最佳条件下,铜萃取率高达95.55%.Fe^(3+)萃取率为8.82%,Ni^(2+)的萃取率为5.47%,Mg^(2+)的萃取率为2.36%.从而达到Cu^(2+)与其它金属离子有效分离的效果. Taken Lix984 as an organic phase extraction agent, kerosene as a diluent for the solvent extraction, extraction of Cu2+ was conducted via sulfates solution containing Fe3 + , Mg2 + and Ni2 + . The experimental results showed that in a certain range, copper extraction ratio increases with extractant concentration, the extraction time, the initial pH value, extraction temperature and stirring time. The optimum of conditions are: the extractant concentration is up to 60% , the phase ratio of organic phase to aqueous one is 2 : 1, the extraction time is 16 min and the initial aqueous phase pH value is 2. 5. Under the optimum conditions, the extraction ratio of Cu2+ reaches 95. 55% , that of Fe3+ is only 8. 82% , that of Ni2+ is 5. 47% , and that of Mg2+ is 2. 36% . It is believed that the extraction process can realize separation of Cu2 + from the other ions.
出处 《材料与冶金学报》 北大核心 2017年第3期186-190,共5页 Journal of Materials and Metallurgy
基金 国家重大科技专项973项目(2014CB643405)
关键词 萃取分离 铜镍铁镁离子混合液 Lix984 extraction separation mixed solution o f Cu2+ , Fe3+ , Ni2+ and Mg2+ Lix984
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  • 1吴文健,蒋汉瀛,杨松青.LIX 984萃取分离铜、镍的试验研究[J].矿冶工程,1995,15(4):43-47. 被引量:11
  • 2黄光临,翁桅,王达武,等.一种从硝酸铜废水中回收铜的方法:中国,101906644A. 3 [P]. 2010-12-08.
  • 3Wang Dianzou. The study and progress on mineral bio-proeessingf C]//The Conference of Application on Copper-Nickel Hydrometallurgy . Xiamen : China ,2001.
  • 4Paatero E,Sjoblom J. Phase behavior in metal extractionsystems[ J]. Hydrometallurgy, 1990,25 ;231 -256.
  • 5Wang Pingrui, Lang Huling, Liu Du, et al. Recent pro-gress in copper solvent extraction [ J ]. Study of NonferrousChemical Enginerring, 1991 ( 2 ) :18-21.
  • 6Hossein A M,Claude B, Daniel H,et al. Simulation of aSX-EW pilot plant [ J]. Hydrometallurgy,2000,56 : 13-31.
  • 7Alguacil F J. Reeovery of copper from ammoniacal/ammo-nium carbonate medium by LIX973N[ J]. Hydrometallurgy,1999,52:55-61.
  • 8Fornari P, Abbruzzese C. Copper and nickel selective re-covery by electrowinning from electronic and galvanic in-dustrial solutions[ J ]. Hydrometallurgy ,1999,52 :209-222.
  • 9Chinmay P, Sarma B. Separation of mickel and copper from ammoniacal solutions through coextraction and selec- tive stripping using LIX84 as the extractant [ J ]. Hydro- metallurgy, 2000,54 : 195-204.
  • 10Rashkov S T, Dobrev T S, Noncheva Z, et al. Lead cobaltanodes for electrowinning of zinc from sulphate electrolytes[J ]. Hydrometallurgy,1999 ,52 : 223-230.

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