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Volume 24 Issue 1
Jan.  2017
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文章导航 >  矿物冶金与材料学报（英文）  > 2017  >  24(1): 37-46
Zela T. Ichlasand Don C. Ibana, Process development for the direct solvent extraction of nickel and cobalt from nitrate solution:aluminum, cobalt, and nickel separation using Cyanex 272, Int. J. Miner. Metall. Mater., 24(2017), No. 1, pp. 37-46. https://doi.org/10.1007/s12613-017-1376-7
Cite this article as:
Zela T. Ichlasand Don C. Ibana, Process development for the direct solvent extraction of nickel and cobalt from nitrate solution:aluminum, cobalt, and nickel separation using Cyanex 272, Int. J. Miner. Metall. Mater., 24(2017), No. 1, pp. 37-46. https://doi.org/10.1007/s12613-017-1376-7
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研究论文

Process development for the direct solvent extraction of nickel and cobalt from nitrate solution:aluminum, cobalt, and nickel separation using Cyanex 272

  • Leaching and Separation Technologies Group, Department of Mining Engineering and Metallurgical Engineering, WA School of Mines, Curtin University, Kalgoorlie, WA 6430, Australia

  • 通讯作者:

    Zela T. Ichlas    E-mail: tanlega.zela@gmail.com

  • A direct solvent extraction (DSX) process for purifying nickel and cobalt from the nitric acid leach solution of nickel laterite ores was conceived and experimentally probed. The proposed process consists of two solvent extraction (SX) steps but with only one extractant-bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex® 272)-used in both steps. The first extraction step involved the removal of aluminum and zinc, whereas the second extraction step involved the separation of cobalt along with manganese from nickel. The experimental results showed essentially quantitative removal of aluminum (>97%) and zinc (>99%) in a single extraction stage using 20vol% Cyanex 272 at pH 2.1. Some cobalt (32%) and manganese (55%) were co-extracted but were easily scrubbed out completely from the loaded organic phase using dilute sulfuric acid at pH ≤ 1.38. Cobalt and manganese in the first extraction raffinate were extracted completely in four extraction stages at staggered pH values of 4.0, 4.4, 4.5, and 4.0 in the first, second, third, and fourth stages, respectively, using also 20vol% Cyanex 272. A small amount of nickel (up to 6.6%) was co-extracted but was easily scrubbed out completely with dilute sulfuric acid at pH 2.0. A flow diagram showing the input and output conditions and the metals separated under the deduced optimum conditions is presented.
    • Research Article

    Process development for the direct solvent extraction of nickel and cobalt from nitrate solution:aluminum, cobalt, and nickel separation using Cyanex 272

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      Abstract
    • A direct solvent extraction (DSX) process for purifying nickel and cobalt from the nitric acid leach solution of nickel laterite ores was conceived and experimentally probed. The proposed process consists of two solvent extraction (SX) steps but with only one extractant-bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex® 272)-used in both steps. The first extraction step involved the removal of aluminum and zinc, whereas the second extraction step involved the separation of cobalt along with manganese from nickel. The experimental results showed essentially quantitative removal of aluminum (>97%) and zinc (>99%) in a single extraction stage using 20vol% Cyanex 272 at pH 2.1. Some cobalt (32%) and manganese (55%) were co-extracted but were easily scrubbed out completely from the loaded organic phase using dilute sulfuric acid at pH ≤ 1.38. Cobalt and manganese in the first extraction raffinate were extracted completely in four extraction stages at staggered pH values of 4.0, 4.4, 4.5, and 4.0 in the first, second, third, and fourth stages, respectively, using also 20vol% Cyanex 272. A small amount of nickel (up to 6.6%) was co-extracted but was easily scrubbed out completely with dilute sulfuric acid at pH 2.0. A flow diagram showing the input and output conditions and the metals separated under the deduced optimum conditions is presented.
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    • [1]
      F. McCarthy and G. Brock, The direct nickel process continued progress on the pathway to commercialisation,[in] Proceedings of the ALTA Nickel/Cobalt/Copper Conference 2011, Perth, 2011, p. 2.
      [2]
      T. Agacayak and V. Zedef, Mine Planning and Equipment Selection, Edited by C. Drebenstedt and R. Singhal, Springer, Dresden, 2014, p. 1039.
      [3]
      F. McCarthy and G. Brock, Direct nickel test plant program:2013 in review,[in] Proceedings of the ALTA Nickel/Cobalt/Copper Conference 2011, Perth, 2014.
      [4]
      B. Z. Ma, W. J. Yang, B. Yang, C. Y. Wang, Y. Q. Chen, and Y. L. Zhang, Pilot-scale plant study on the innovative nitric acid pressure leaching technology for laterite ores, Hydrometallurgy, 155(2015), p. 88.
      [5]
      B. Ma, C. Y. Wang, W. J. Yang, F. Yin, and Y. Q. Chen, Aluminum removal from leach liquor of nitric acid pressure leaching laterite ores, Adv. Mater. Res., 634-638(2013), p. 3191.
      [6]
      Direct Nickel Ltd., Nickel Production Demonstration Program, Direct Nickel Ltd., Waterford, 2014, p. 7.
      [7]
      G. M. Ritcey, Solvent Extraction Principles and Practice, Edited by J. Rydberg, M. Cox, C. Musikas, and G. R. Chopping, Marcel Dekker, Inc., New York, 2004, p. 277.
      [8]
      J. Young, G. Fawdry and R. Bosman, Experimental study of the influence of diluent characteristics on performance in metal extraction,[in] Proceedings of the ISEC 1990, Kyoto, 1990, p. 327.
      [9]
      P. E. Tsakiridis and S. Agatzini-Leonardou, Solvent extraction of aluminium in the presence of cobalt, nickel and magnesium from sulphate solutions by Cyanex 272, Hydrometallurgy, 80(2005), No. 1-2, p. 90.
      [10]
      K. H. Park, D. Mohapatra, and C. W. Nam, Two stage leaching of activated spent HDS catalyst and solvent extraction of aluminium using organo-phosphinic extractant, Cyanex 272, J. Hazard. Mater., 148(2007), No. 1-2, p. 287.
      [11]
      D. P. Mantuano, G. Dorella, R. C. A. Elias, and M. B. Mansur, Analysis of a hydrometallurgical route to recover base metals from spent rechargeable batteries by liquid-liquid extraction with Cyanex 272, J. Power Sources, 159(2006), No. 2, p. 1510.
      [12]
      M. M. Orive, M. A. Olazabal, L. A. Fernandez, and J. M. Madariaga, The recovery of cobalt and nickel from acidic sulphate solutions in the presence of aluminum, Solvent Extr. Ion Exch., 10(1992), No. 5, p. 787.
      [13]
      J. S. Preston, Solvent extraction of cobalt and nickel by organophosphorus acids I. Comparison of phosphoric, phosphonic and phosphonic acid systems, Hydrometallurgy, 9(1982), No. 2, p. 115.
      [14]
      M. D. Lanagan and D. C. Ibana, The solvent extraction and stripping of chromium with Cyanex® 272, Miner. Eng., 16(2003), No. 3, p. 237.
      [15]
      M. Hutton-Ashkenny, D. Ibana, and K. Barnard, Evidence for a predictable difference between nitrate and sulphate anions in the solvent extraction of base metals by acidic extractants,[in] Proceedings of the ISEC 2014, Würzburg, 2014, p. 855.
      [16]
      D. Mohapatra, K. Hong-In, C. W. Nam, and K. H. Park, Liquid-liquid extraction of aluminium (Ⅲ) from mixed sulphate solutions using sodium salts of Cyanex 272 and D2EHPA, Sep. Purif. Technol., 56(2007), No. 3, p. 311.
      [17]
      M. Virnig, M. Eyzaguirre, M. Jo, and J. Calderon, Effect of nitrate on copper SX circuits:a case study,[in] Proceedings of the Copper 2003-Cobre 2003, Santiago, 2003, p. 795.
      [18]
      H. J. Bart, R. Marr, A. Bauer, R. Schein, and E. Marageter, Copper extraction in nitrate media, Hydrometallurgy, 23(1990), No. 2-3, p. 281.
      [19]
      K. C. Sole, J. Brent Hiskey, and T. L. Ferguson, An assessment of the long-term stabilities of Cyanex 302 and Cyanex 301 in sulfuric and nitric acids, Solvent Extr. Ion Exch., 11(1993), No. 5, p. 783.
      [20]
      B. M. Munyungano, Solvent degradation-Rössing Uranium Mine, J. S. Afr. Inst. Min. Metall., 107(2007), No. 7, p. 415.
      [21]
      Y. Sze, T. E. McDougall, and C. G. Martin, Chemical degradation of tri-n-butyl phosphate/diluent solvents TM used in Candu thorium fuels reprocessing development, Solvent Extr. Ion Exch. 5(1987), No. 1, p. 129.
      [22]
      J. O'Callaghan, Process improvements at Bulong Operations Pty Ltd,[in] Proceedings of the ALTA Nickel/Cobalt Conference 2003, Perth, WA, 2003.
      [23]
      M. Adams, D. Van Der Meulen, C. Czerny, P. Adamini, J. Turner, S. Jayasekera, J. Amaranti, J. Mosher, M. Miller, and D. White, Piloting of the beneficiation and EPAL circuits for Ravensthorpe nickel operations,[in] Proceedings of the International Laterite Nickel Symposium 2004(as held during the 2004 TMS Annual Meeting), North Carolina, 2004, p. 193.
      [24]
      D. T. White, M. J. Miller, and A. C. Napier, Impurity disposition and control in the Ravensthorpe acid leaching process,[in] Proceedings of the Iron Control Technologies-3rd International Symposium on Iron Control in Hydrometallurgy, Montreal, 2006, p. 591.
      [25]
      D. Mohapatra and K. H. Park, Solvent extraction of Al (Ⅲ) from sulfate solutions using bis (2,4,4-trimethylpentyl) phosphinic acid-mechanism and complexation, Miner. Metall. Process., 25(2008), No. 2, p. 73.
      [26]
      J. S. Preston, Solvent extraction of metals by carboxylic acids, Hydrometallurgy, 14(1985), No. 2, p. 171.
      [27]
      D. F. Peppard, J. R. Ferraro, and G. W. Mason, Possible hydrogen bonding in certain interactions of organic phosphorus compounds, J. Inorg. Nucl. Chem., 4(1957), No. 5, p. 371.
      [28]
      Z. Kolarik, Critical evaluation of some equilibrium constants involving acidic organophosphorus extractants, Pure Appl. Chem., 54(1982), No. 12, p. 2593.
      [29]
      P. R. Danesi, L. Reichley-Yinger, G. Mason, L. Kaplan, E. P. Horwltz, and H. Diamond, Selectivity-structure trends in the extraction of Co (Ⅱ) and Ni (Ⅱ) by dialkyl phosphoric, alkyl alkylphosphonic, and dialkylphosphinic acids, Solvent Extr. Ion Exch., 3(1985), No. 4, p. 435.
      [30]
      J. Rydberg, G. R. Choppin, C. Musikas, and T. Sekine, Solvent Extraction Principles and Practice, CRC Press, 2004, p. 146.
      [31]
      B. K. Tait, Cobalt-nickel separation:the extraction of cobalt (Ⅱ) and nickel (Ⅱ) by Cyanex 301, Cyanex 302 and Cyanex 272, Hydrometallurgy, 32(1993), No. 3, p. 365.
      [32]
      P. E. Tsakiridis and S. Agatzini-Leonardou, Process for the recovery of cobalt and nickel in the presence of magnesium from sulphate solutions by Cyanex 272 and Cyanex 302, Miner. Eng., 17(2004), No. 7-8, p. 913.
      [33]
      J. M. Zhao, X. Y. Shen, F. L. Deng, F. C. Wang, Y. Wu, and H. Z. Liu, Synergistic extraction and separation of valuable metals from waste cathodic material of lithium ion batteries using Cyanex272 and PC-88A, Sep. Purif. Technol., 78(2011), No. 3, p. 345.
      [34]
      S. D. Dogmane, R. K. Singh, D. D. Bajpai, and J. N. Mathur, Extraction of U (VI) by Cyanex-272, J. Radioanal. Nucl. Chem., 253(2002), No. 3, p. 477.
      [35]
      N. Miralles, A. M. Sastre, E. Figuerola, and M. Martinez, Solvent extraction of iron (Ⅲ) by bis (2,4,4-trimethylpentyl) phosphinic acid:experimental equilibrium study, Hydrometallurgy, 31(1992), No. 1-2, p. 1.
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