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Separation of copper,zinc,cobalt and nickel ions by supported liquid membrane technique using LIX 84I,TOPS-99 and Cyanex 272

机译:使用LIX 84I,TOPS-99和Cyanex 272的支持液膜技术分离铜,锌,钴和镍离子

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Separation of copper,zinc,cobalt and nickel ions from synthetic leach liquor using supported liquid membrane was studied.LIX 84I,TOPS-99 and Cyanex 272 were used as the mobile carrier for the supported liquid membrane.From the synthetic leach liquor containing 8.97mole/m3 copper,40.83 mole/m3 zinc,27.49 mole/m3 cobalt,420.51 mole/m3 nickel and 75.677 mole/m3 ammonium sulphate,copper was first separated using LIX 841 followed by zinc using TOPS-99 and cobalt using Cyanex 272.The solution was made copper free using 10% LIX 84I in the membrane phase and 900 mole/m3 H2SO4 in the strip solution at pH 4.5.After copper was separated,the leach liquor was made zinc free at pH 3.65 using 0.15 M TOPS-99 in the membrane phase and 900 mole/m3 H2SO4 in the strip solution followed by separation of cobalt using Cyanex 272.It was observed that co-permeations of zinc,cobalt and nickel with copper using LIX 841 were 0.076,0.085 and 0.10 mole/m3,respectively.Co-permeations of cobalt and nickel with zinc using TOPS-99 were 0.187 and 0.323 mole/m3 and co-permeation of nickel with cobalt using Cyanex 272 was 3.407 mole/m3,respectively.Separation factors for metal ions with different extractants were calculated and reported.
机译:研究了负载型液膜从合成浸出液中分离铜,锌,钴和镍离子的方法。LIX84I,TOPS-99和Cyanex 272被用作负载型液膜的移动载体。从含8.97mole的合成浸出液中/ m3铜,40.83摩尔/ m3锌,27.49摩尔/ m3钴,420.51摩尔/ m3镍和75.677摩尔/ m3硫酸铵,首先使用LIX 841分离铜,然后使用TOPS-99分离锌和使​​用Cyanex 272分离钴。在膜相中使用10%LIX 84I和在pH值为4.5的汽提溶液中使用900mol / m3的H2SO4使溶液中的铜分离。膜相和汽提溶液中900摩尔/立方米的H2SO4,然后使用Cyanex 272分离钴。使用LIX 841观察到锌,钴和镍与铜的共渗透率为0.076、0.085和0.10摩尔/立方米,钴和镍与锌u的共渗透用TOPS-99分别测得0.187和0.323摩尔/立方米,使用Cyanex 272的镍与钴的共渗透分别为3.407摩尔/立方米。计算并报告了不同萃取剂对金属离子的分离系数。

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