Solvent extraction of metals from a Brazilian nickel lateritic liquor with D2EHPA and Cyanex 272

被引:3
作者
Guimaraes, Alexandre Silva [1 ]
da Silva, Marcelle de Fatima [1 ]
de Souza Resende, Georgio Patricio [1 ]
dos Santos, Iranildes Daniel [2 ]
Mansur, Marcelo Borges [1 ]
机构
[1] Univ Fed Rio de Janeiro UFRJ, Programa Engn Met & Mat, Ctr Tecnol, Cidade Univ,Av Horacio Macedo 2030, BR-21941598 Rio De Janeiro, RJ, Brazil
[2] Inst Tecnol Vale ITV, Av Juscelino Kubitschek 31, Ouro Preto, MG, Brazil
关键词
D2EHPA; Cyanex; 272; Cobalt; Nickel; Solvent extraction; SULFATE-SOLUTIONS; LEACH SOLUTION; COBALT; RECOVERY; MAGNESIUM; CALCIUM; MANGANESE; REMOVAL; PRECIPITATION; PURIFICATION;
D O I
10.1007/s43153-022-00252-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The solvent extraction of Fe (residual), Mn, and Co from a real sulfuric Ni lateritic liquor (initial pH = 3) containing Ca and Mg was evaluated using D2EHPA and Cyanex 272 as extractants (A/O ratio = 1, T = 50 degrees C, one contact stage). Fe was practically extracted by both extractants at pH > 3. While Mn was selectively separated from Co and Ni with D2EHPA (5% v/v) at pH 3 (beta(Mn/Co) = 167), it was co-extracted with Co with Cyanex 272, which in turns is much more effective than D2EHPA in separating Co and Ni (beta(Co/Ni) = 697 with 15% v/v of Cyanex 272 at pH 4.5). In addition, D2EHPA presented high affinity to Ca at low pH conditions, while Cyanex 272 extracted Ca and Mg at similar extents but at a higher pH level. Therefore, two SX circuits at staged operations, the first with D2EHPA and the second with Cyanex 272, can produce Co and Ni rich-streams. It was verified that Fe, Mn, as well as Ca, and part of Mg may be removed from the liquor at pH 3 with D2EHPA (5% v/v), while Co and remaining Mg could be separated from Ni with Cyanex 272 (15% v/v) at pH 4.5. Subsequent stripping and raffinate treatment strategies were presented. Data fitting using the slope analysis method revealed that coordinate complexes of Mn with D2EHPA, as well as Mn and Co with Cyanex 272, has the exact same MR2(RH)(2) molecular structure.
引用
收藏
页码:599 / 606
页数:8
相关论文
共 35 条
[1]   Hydrometallurgical process for the separation and recovery of nickel from sulphate heap leach liquor of nickeliferrous laterite ores [J].
Agatzini-Leonardou, S. ;
Tsakiridis, P. E. ;
Oustadakis, P. ;
Karidakis, T. ;
Katsiapi, A. .
MINERALS ENGINEERING, 2009, 22 (14) :1181-1192
[2]   Removal of iron from acidic leach liquor of lateritic nickel ore by goethite precipitate [J].
Chang, Yongfeng ;
Zhai, Xiujing ;
Li, Binchuan ;
Fu, Yan .
HYDROMETALLURGY, 2010, 101 (1-2) :84-87
[3]   Purification of synthetic laterite leach solution by solvent extraction using D2EHPA [J].
Cheng, CY .
HYDROMETALLURGY, 2000, 56 (03) :369-386
[4]   Selective reductive leaching of oxidised cobalt containing residue [J].
Chong, Sebastian ;
Hawker, William ;
Vaughan, James .
MINERALS ENGINEERING, 2013, 54 :82-87
[5]   Iron Precipitation Strategies from Nickel Laterite Ore Sulfuric Acid Leach Liquor [J].
da Silva, Marcelle de Fatima ;
de Sousa Oliveira, Mateus Rodrigues ;
dos Santos, Iranildes Daniel ;
Radino-Rouse, Patricia ;
Mansur, Marcelo Borges .
MINERAL PROCESSING AND EXTRACTIVE METALLURGY REVIEW, 2022, 43 (01) :28-39
[6]   COMPETING SOLVENT EXTRACTION OF CALCIUM AND/OR NICKEL WITH CYANEX 272 AND/OR D2EHPA [J].
de Souza, Marcel F. A. ;
Mansur, Marcelo B. .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2019, 36 (01) :541-547
[7]   Direct solvent extraction of nickel at Bulong operations [J].
Donegan, S. .
MINERALS ENGINEERING, 2006, 19 (12) :1234-1245
[9]   Recovery of cobalt and nickel in the presence of magnesium and calcium from sulfate solutions by Versatic 10 and mixtures of Versatic 10 and Cyanex 301 [J].
Guan, Qing-jun ;
Sun, Wei ;
Zhou, Gui-ying ;
Liu, Jia-peng ;
Yin, Zhi-gang .
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2016, 26 (03) :865-873
[10]   Selection of a synergistic solvent extraction system to remove calcium and magnesium from concentrated nickel sulfate solutions [J].
Guimaraes, Alexandre Silva ;
Mansur, Marcelo Borges .
HYDROMETALLURGY, 2018, 175 :250-256