留言板

尊敬的读者、作者、审稿人, 关于本刊的投稿、审稿、编辑和出版的任何问题, 您可以本页添加留言。我们将尽快给您答复。谢谢您的支持!

姓名
邮箱
手机号码
标题
留言内容
验证码
Volume 25 Issue 11
Nov.  2018
数据统计

分享

计量
  • 文章访问数:  558
  • HTML全文浏览量:  83
  • PDF下载量:  24
  • 被引次数: 0
Elham Hosseini, Fereshteh Rashchi, and Abolghasem Ataie, Ti leaching from activated ilmenite-Fe mixture at different milling energy levels, Int. J. Miner. Metall. Mater., 25(2018), No. 11, pp. 1263-1274. https://doi.org/10.1007/s12613-018-1679-3
Cite this article as:
Elham Hosseini, Fereshteh Rashchi, and Abolghasem Ataie, Ti leaching from activated ilmenite-Fe mixture at different milling energy levels, Int. J. Miner. Metall. Mater., 25(2018), No. 11, pp. 1263-1274. https://doi.org/10.1007/s12613-018-1679-3
引用本文 PDF XML SpringerLink
研究论文

Ti leaching from activated ilmenite-Fe mixture at different milling energy levels

  • 通讯作者:

    Fereshteh Rashchi    E-mail: rashchi@ut.ac.ir

  • Mechanical activation processes on ilmenite concentrate were performed in three different energy levels. Iron powder as a reducing agent was added to ilmenite in the milling stage and the mechanically activated mixture was subjected to acid leaching. The leaching experiments were designed using the Taguchi method, and the optimum ranges were obtained. Furthermore, response surface methodology (RSM) was used to optimize the critical parameters in the leaching system to achieve the highest titanium (Ti) leachability. Based on the inductively coupled plasma-optical emission spectrometry (ICP-OES) results, maximum leaching recovery of Ti (80%) was obtained using activated Ti concentrates at a medium activation energy level, which is calculated to be 25.38 kJ/g, using 15vol% hydrochloric acid (HCl), a temperature of 70℃, leaching time of 3 h, and a solid-to-liquid ratio of 0.05 g·mL-1. Intensifying the milling energy from a low to high level led to a decrease in the mean crystallite size and also structure homogenization at the high energy level. According to the transmission electron microscopy (TEM) images, the mean grain size of the ilmenite/Fe nanocomposite was about 30 nm at the medium energy level sample. Finally, solvent extraction by tributyl phosphate (TBP) was performed on the leach liquor to separate dissolved Fe (the major impurity) from Ti, which led to 83% extraction recovery of Ti.
  • Research Article

    Ti leaching from activated ilmenite-Fe mixture at different milling energy levels

    + Author Affiliations
    • Mechanical activation processes on ilmenite concentrate were performed in three different energy levels. Iron powder as a reducing agent was added to ilmenite in the milling stage and the mechanically activated mixture was subjected to acid leaching. The leaching experiments were designed using the Taguchi method, and the optimum ranges were obtained. Furthermore, response surface methodology (RSM) was used to optimize the critical parameters in the leaching system to achieve the highest titanium (Ti) leachability. Based on the inductively coupled plasma-optical emission spectrometry (ICP-OES) results, maximum leaching recovery of Ti (80%) was obtained using activated Ti concentrates at a medium activation energy level, which is calculated to be 25.38 kJ/g, using 15vol% hydrochloric acid (HCl), a temperature of 70℃, leaching time of 3 h, and a solid-to-liquid ratio of 0.05 g·mL-1. Intensifying the milling energy from a low to high level led to a decrease in the mean crystallite size and also structure homogenization at the high energy level. According to the transmission electron microscopy (TEM) images, the mean grain size of the ilmenite/Fe nanocomposite was about 30 nm at the medium energy level sample. Finally, solvent extraction by tributyl phosphate (TBP) was performed on the leach liquor to separate dissolved Fe (the major impurity) from Ti, which led to 83% extraction recovery of Ti.
    • loading
    • [1]
      U. Diebold, The surface science of titanium dioxide, Surf. Sci. Rep., 48(2003), No. 5-8, p. 53.
      [2]
      T.S. Mackey, Acid leaching of ilmenite into synthetic rutile, Ind. Eng. Chem. Prod. Res. Dev., 13(1974), No. 1, p. 9.
      [3]
      T. Chernet, Applied mineralogical studies on Australian sand ilmenite concentrate with special reference to its behavior in the sulphate process, Miner. Eng., 12(1999), No. 5, p. 485.
      [4]
      C. Sasikumar, D.S. Rao, S. Srikanth, B. Ravikumar, N.K. Mukhopadhvay, and S.P. Mehrotra, Effect of mechanical activation on the kinetics of sulfuric acid leaching of beach sand ilmenite from Orissa, India, Hydrometallurgy, 75(2004), No. 1-4, p. 189.
      [5]
      M. Jabłoński and A. Przepiera, Kinetic model for the reaction of ilmenite with sulphuric acid, J. Therm. Anal. Calorim., 65(2001), No. 2, p. 583.
      [6]
      E.A. Abdel-Aal, I.A. Ibrahim, A.A.I. Afifi, and A.K. Ismail, Production of synthetic rutile from Egyptian ilmenite ore by a direct hydrometallurgical process,[in] 2nd International Conference on Processing Materials for Properties, San Francisco, 2000, p. 955.
      [7]
      C. Li, B. Liang, H. Song, J.Q. Xu, and X.Q. Wang, Preparation of porous rutile titania from ilmenite by mechanical activation and subsequent sulfuric acid leaching, Microporous Mesoporous Mater., 115(2008), No. 3, p. 293.
      [8]
      K.K. Sahu, T.C. Alex, D. Mishra, and A. Agrawal, An overview on the production of pigment grade titania from titania-rich slag, Waste Manage. Res., 24(2006), No. 1, p. 74.
      [9]
      M.H.H. Mahmoud, A.A.I. Afifi, and I.A. Ibrahim, Reductive leaching of ilmenite ore in hydrochloric acid for preparation of synthetic rutile, Hydrometallurgy, 73(2004), No. 1-2, p. 99.
      [10]
      B.N. Akhgar, M. Pazouki, B.N. Akhgar, M. Ranjbar, and A. Hosseinnia, Preparation of micro and nanostructured titania compounds from ilmenite concentrate, Int. J. Miner. Process. 124(2013), p. 138.
      [11]
      J.Y. Xiang, S.L. Liu, X.W. Lv, and C.G. Bai, Preparation of rutile from ilmenite concentrate through pressure leaching with hydrochloric acid, Metall. Mater. Trans. B, 48(2017), No. 2, p. 1333.
      [12]
      N.Y. Mostafa, M.H.H. Mahmoud, and Z.K. Heiba, Hydrolysis of TiOCl2 leached and purified from low-grade ilmenite mineral, Hydrometallurgy, 139(2013), p. 88.
      [13]
      E.J. Kelley, Modern Aspects of Electrochemistry, J.O'M. Bockris, B.E. Conway, and R.E. White, eds., Springer, Boston, 1982, p. 319.
      [14]
      F.A. Cotton and G. Wilkinson, Advanced Inorganic Chemistry:A Comprehensive Text, 4th Ed., John Wiley & Sons Inc., New York, 1980, p. 692.
      [15]
      K.C. Sole, Recovery of titanium from the leach liquors of titaniferous magnetites by solvent extraction:Part 1. Review of the literature and aqueous thermodynamics, Hydrometallurgy, 51(1999), No. 2, p. 239.
      [16]
      I. Cservenyák, G.H. Kelsall, and W. Wang, Reduction of TiIV species in aqueous sulfuric and hydrochloric acid I:Titanium speciation, Electrochim. Acta, 41(1996), No. 4, p. 563.
      [17]
      C. Suryanarayana, Mechanical alloying and milling, Prog. Mater. Sci., 46(2001), No. 1-2, p. 1.
      [18]
      N. Burgio, A. Iasonna, M. Magini, S. Martelli, and F. Padella, Mechanical alloying of the Fe-Zr system, Correlation between input energy and end products, IL Nuovo Cimento D, 13(1991), No. 4, p. 459.
      [19]
      M. Magini, A. Iasonna, and F. Padella, Ball milling:an experimental support to the energy transfer evaluated by the collision model, Scripta Mater., 34(1996), No. 1, p. 13.
      [20]
      B.S. Murty, M. Mohan Rao, and S. Ranganathan, Milling maps and amorphization during mechanical alloying, Acta Metal. Mater., 43(1995), No. 6, p. 2443.
      [21]
      S. Kehoe, M. Ardhaoui, and J. Stokes, Design of experiments study of hydroxyapatite synthesis for orthopaedic application using fractional factorial design, J. Mater. Eng. Perform., 20(2011), No. 8, p. 1423.
      [22]
      M. Ghadiri, A. Vatanara, D. Doroud, and A.R. Najafabadi, Paromomycin loaded solid lipid nanoparticles:Characterization of production parameters, Biotechnol. Bioprocess Eng., 16(2011), No. 3, p. 617.
      [23]
      G.M. Venkatesh, J.A.N. Coleman, T.J. Wrzosek, S. Duddu, N.R. Palepu, R. Bandyopadhyay, and D.J.W. Grant, Fractional factorial designs for optimizing experimental conditions for Hiestand's Indices of Tableting Performance, Powder Technol., 97(1998), No. 2, p. 151.
      [24]
      G.H. Jeffery, J. Bassett, J. Mendham, and R.C. Denney, Vogel's Textbook of Quantitative Chemical Analysis, 5th Ed., John Wiley & Sons Inc., New York, 1989, p. 376.
      [25]
      E. Narita, H. Takeuchi, H. Ichikawa, T. Odagawa, and T. Okabe, Manufacture of pure titanium(IV) oxide by the chloride process:Ⅱ. Selective extraction of titanium (IV) and iron(Ⅲ) from hydrochloric acid leach liquor of ilmenite ore by tributyl phosphate, Bull. Chem. Soc. Jpn., 56(1983), No. 6, p. 1832.
      [26]
      S. Kotrly and L. Sucha, Handbook of Chemical Equilibria in Analytical Chemistry, Ellis Horwood Ltd., Chichester, 1985, p. 414.
      [27]
      K.M. Allal, D. Hauchard, M. Stambouli, D. Pareau, and G. Durand, Solvent extraction of titanium by tributyl phosphate, trioctylphosphine oxide and decanol from chloride media, Hydrometallurgy, 45(1997), No. 1-2, p. 113.

    Catalog


    • /

      返回文章
      返回