, Volume 68, Issue 5, pp 1476–1484 | Cite as

Kinetics of Hydrochloric Acid Leaching of Titanium from Titanium-Bearing Electric Furnace Slag

  • Fuqiang Zheng
  • Feng Chen
  • Yufeng GuoEmail author
  • Tao Jiang
  • Andrew Yakovlevich Travyanov
  • Guanzhou Qiu


The hydrochloric acid leaching of titanium from titanium-bearing electric furnace slag was investigated under different experimental conditions. The results indicate that particle size, hydrochloric acid concentration and reaction temperature were of significance to the leaching kinetics. Specifically, reaction temperature was the most important factor followed by hydrochloric acid concentration and particle size. The shrinking core model was used to describe the leaching process which was controlled by surface chemical reaction. The kinetic equation was obtained and the activation energy was found to be 43.16 kJ/mol. Iron and calcium species were almost completely dissolved in the acid when the extraction degree of titanium reached 99.84%. MgO (19.34 wt.%) and Al2O3 (32.45 wt.%) in the spinel were still in the leaching residue and SiO2 (43.53 wt.%) in the form of quartz remained in the leaching residue.


Vanadium Average Particle Size Blast Furnace Diopside Leaching Residue 
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The authors are grateful to the Program for New Century Excellent Talents in University from Chinese Ministry of Education (NCET-10-0834) and the Visiting Scholar Program from China Scholarship Council ([2013]3018) for supporting this research.


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Copyright information

© The Minerals, Metals & Materials Society 2016

Authors and Affiliations

  • Fuqiang Zheng
    • 1
  • Feng Chen
    • 1
  • Yufeng Guo
    • 1
    Email author
  • Tao Jiang
    • 1
  • Andrew Yakovlevich Travyanov
    • 2
  • Guanzhou Qiu
    • 1
  1. 1.School of Minerals Processing and BioengineeringCentral South UniversityChangshaChina
  2. 2.National University of Science and Technology “MISIS”MoscowRussia

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