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author:

Yu, K.-P. (Yu, K.-P..) [1] | Chen, B. (Chen, B..) [2] | Zhang, H.-L. (Zhang, H.-L..) [3] | Zhu, G.-J. (Zhu, G.-J..) [4] | Xu, H.-B. (Xu, H.-B..) [5] | Zhang, Y. (Zhang, Y..) [6]

Indexed by:

Scopus

Abstract:

An efficient process was proposed for extracting chromium from chromium-containing slag after desilication with aqueous NaOH solution. The effect of the NaOH concentration, liquid-to-solid mass ratio, and leaching temperature on the leaching rate of silicon was investigated. The results showed that 83.78% of the silicon, 41.87% of the aluminum, and 46.42% of the vanadium were removed from the slag under suitable conditions. The kinetic analysis results showed that the leaching rate of silicon is controlled by a chemical reaction under two regimes due to the two silicon-bearing minerals presented in the slag. The first stage is limited by the reaction between NaOH and SiO2, whereas the second stage is subject to the reaction between NaOH and 2MgO·2Al2O3·5SiO2. The corresponding apparent activation energies were calculated to be 67.27 kJ/mol and 35.82 kJ/mol, respectively. The extraction rate of chromium from the leaching residue using lime-free roasting reached 98.41%, which was highly superior to the 9.85% obtained from the slag without desilication. © 2016 Elsevier B.V. All rights reserved.

Keyword:

Chromium-containing slag; Desilication; Kinetics; Lime-free roasting

Community:

  • [ 1 ] [Yu, K.-P.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 2 ] [Yu, K.-P.]Key Laboratory of Green Process and Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 3 ] [Yu, K.-P.]College of Zijin Mining, Fuzhou University, Fuzhou, Fujian 350108, China
  • [ 4 ] [Chen, B.]College of Zijin Mining, Fuzhou University, Fuzhou, Fujian 350108, China
  • [ 5 ] [Zhang, H.-L.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 6 ] [Zhang, H.-L.]Key Laboratory of Green Process and Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 7 ] [Zhu, G.-J.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 8 ] [Zhu, G.-J.]Key Laboratory of Green Process and Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 9 ] [Xu, H.-B.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 10 ] [Xu, H.-B.]Key Laboratory of Green Process and Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 11 ] [Zhang, Y.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, 100190, China
  • [ 12 ] [Zhang, Y.]Key Laboratory of Green Process and Engineering, Chinese Academy of Sciences, Beijing, 100190, China

Reprint 's Address:

  • [Zhang, H.-L.]National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of SciencesChina

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Source :

Hydrometallurgy

ISSN: 0304-386X

Year: 2016

Volume: 162

Page: 86-93

2 . 6 0 5

JCR@2016

4 . 8 0 0

JCR@2023

ESI HC Threshold:324

JCR Journal Grade:1

CAS Journal Grade:2

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count:

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 3

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