Activation pretreatment of limonitic laterite ores by alkali-roasting using NaOH

Qiang Guo, Jing-kui Qu, Tao Qi, Guang-ye Wei, Bing-bing Han

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    Qiang Guo, Jing-kui Qu, Tao Qi, Guang-ye Wei, and Bing-bing Han, Activation pretreatment of limonitic laterite ores by alkali-roasting using NaOH, Int. J. Miner. Metall. Mater., 19(2012), No. 2, pp.100-105. https://dx.doi.org/10.1007/s12613-012-0522-5
    Qiang Guo, Jing-kui Qu, Tao Qi, Guang-ye Wei, and Bing-bing Han, Activation pretreatment of limonitic laterite ores by alkali-roasting using NaOH, Int. J. Miner. Metall. Mater., 19(2012), No. 2, pp.100-105. https://dx.doi.org/10.1007/s12613-012-0522-5
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    Activation pretreatment of limonitic laterite ores by alkali-roasting using NaOH

    • National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Beijing 100190, China

    • Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China

    • Graduate School of Chinese Academy of Sciences, Beijing 100190, China

    • School of Materials Science and Engineering, University of Science and Technology Beijing, Beijing 100083, China

    基金项目: 

    This work was financially supported by the National Key Technology R&D Program (No.2011BAC06B07).

      通信作者:

      Tao Qi E-mail: tqgreen@home.ipe.ac.cn

    中文摘要

    Activation pretreatment of Cr-containing limonitic laterite ores by NaOH roasting to remove Cr, Al, and Si, as well as its effect on Ni and Co extraction in the subsequent pressure acid leaching process was investigated. Characterization results of X-ray diffraction (XRD) and scanning electron microscopy/X-ray energy dispersive spectroscopy (SEM/XEDS) show that goethite is the major Ni-bearing mineral, and chromite is the minor one. Experimental results show that the leaching rates of Cr, Al, and Si are 95.6wt%, 83.8wt%, and 40.1wt%, respectively, under the optimal alkali-roasting conditions. Compared with the direct pressure acid leaching of laterite ores, the leaching rates of Ni and Co increase from 80.1wt% to 96.9wt% and 70.2wt% to 95.1wt% after pretreatment, respectively. Meanwhile, the grade of acid leaching iron residues increases from 54.4wt% to 62.5wt%, and these residues with low Cr content are more suitable raw materials for iron making.

     

    Activation pretreatment of limonitic laterite ores by alkali-roasting using NaOH

    Author Affilications

      • National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Beijing 100190, China

      • Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China

      • Graduate School of Chinese Academy of Sciences, Beijing 100190, China

      • School of Materials Science and Engineering, University of Science and Technology Beijing, Beijing 100083, China

    • Funds: 

      This work was financially supported by the National Key Technology R&D Program (No.2011BAC06B07).

    • Received: 08 December 2010; Revised: 16 January 2011; Accepted: 24 January 2011;
    Activation pretreatment of Cr-containing limonitic laterite ores by NaOH roasting to remove Cr, Al, and Si, as well as its effect on Ni and Co extraction in the subsequent pressure acid leaching process was investigated. Characterization results of X-ray diffraction (XRD) and scanning electron microscopy/X-ray energy dispersive spectroscopy (SEM/XEDS) show that goethite is the major Ni-bearing mineral, and chromite is the minor one. Experimental results show that the leaching rates of Cr, Al, and Si are 95.6wt%, 83.8wt%, and 40.1wt%, respectively, under the optimal alkali-roasting conditions. Compared with the direct pressure acid leaching of laterite ores, the leaching rates of Ni and Co increase from 80.1wt% to 96.9wt% and 70.2wt% to 95.1wt% after pretreatment, respectively. Meanwhile, the grade of acid leaching iron residues increases from 54.4wt% to 62.5wt%, and these residues with low Cr content are more suitable raw materials for iron making.

     

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