Published at : 30 Sep 2026
Volume : IJtech
Vol 17, No 5 (2026)
DOI : https://doi.org/10.14716/ijtech.v17i5.8880
| Rustam Sharipov | 1. School of Materials Science and Green Technologies, Kazakh-British Technical University, Almaty 050000, Kazakhstan 2. National Center on Complex Processing of Mineral Raw Materials of the Republic |
| Galymzhan Maldybayev | 1. School of Materials Science and Green Technologies, Kazakh-British Technical University, Almaty 050000, Kazakhstan 2. National Center on Complex Processing of Mineral Raw Materials of the Republic |
| Assel Dagubayeva | 1. School of Materials Science and Green Technologies, Kazakh-British Technical University, Almaty 050000, Kazakhstan 2. National Center on Complex Processing of Mineral Raw Materials of the Republic |
| Mohd Dzul Hakim Wirzal | Chemical Engineering Department, Universiti Teknologi PETRONAS, Seri Iskandar, Perak 32610, Malaysia |
| Setyo Budi Kurniawan | Research Centre for Environment and Clean Technologies, National Research and Innovation Agency (BRIN), Jakarta Pusat 10340, Indonesia |
| Zaher Mundher Yaseen | Civil and Environmental Engineering Department, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia |
| Omirserik Baigenzhenov | Department of Metallurgical Engineering, Satbayev University, Almaty 050013, Kazakhstan |
| Ahmad Hosseini-Bandegharaei | 1. Faculty of Chemistry, Semnan University, Semnan 35131-19111, Iran 2. Scientific Research Center, Al-Ayen Iraqi University (AUIQ), Nasiriyah, Thi-Qar 64001, Iraq 3. Department of Sustainable Engin |
Chrysotile asbestos beneficiation waste poses a significant environmental challenge while representing an underutilized secondary source of nickel. In this study, we investigated the selective leaching of a nickel-enriched magnetic fraction using citric, acetic, oxalic, and tartaric acids combined with comparative kinetic modeling. Citric acid achieved the highest nickel extraction (82.6%), outperforming acetic (61.8%), oxalic (39.2%), and tartaric (26.1%) acids. Kinetic analysis showed that the Drozdov–Rotinyan model best described the process ( = 0.9837), indicating a mixed reaction–diffusion mechanism with an apparent activation energy of 21.0 kJ mol-1. Iron dissolution remained low (2.1%–13.5%), producing Ni/Fe selectivity up to 19.2. The extraction and kinetic results indicate that nickel recovery involves proton-assisted mineral dissolution, ligand stabilization of dissolved Ni2+, and diffusion-related resistance. This study provides mechanistic insight into selective nickel extraction from iron-rich technogenic materials and demonstrates the potential of organic-acid leaching for chrysotile asbestos beneficiation waste valorization.
Nickel recovery; Organic-acid leaching; Reaction–diffusion mechanism; Selective dissolution; Technogenic waste
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