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Use of oxidation roasting to control NiO reduction in Ni-bearing limonitic laterite
Affiliation:1. Institute of Ferrous Technology, POSTECH, Pohang 790-784, Republic of Korea;2. Ironmaking/FINEX Research Group, POSCO, Pohang 790-783, Republic of Korea;1. Mineral Processing Dept., Tarbiat Modares University, Tehran, Iran;2. Oil and Gas Engineering Dept., University of Tehran, Tehran, Iran;1. State Key Laboratory of Complex Nonferrous Metal Resources Clean Utilization, Kunming University of Science and Technology, Kunming, 650093, China;2. Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, Kunming, 650093, China;3. School of Metallurgical and Ecological Engineering, University of Science and Technology Beijing, Beijing, 100083, China;1. School of Materials Science and Engineering, University of New South Wales, Sydney, NSW 2052, Australia;2. School of Mechanical Materials and Mechatronic Engineering, University of Wollongong, Wollongong, NSW 2522, Australia;3. Meta-Logical Solutions Pty Ltd, Armadale, Victoria 3143, Australia
Abstract:Use of limonitic laterite as an iron source in conventional ironmaking is restricted due to its gangue composition and small particle size. Even direct reduction cannot effectively produce direct reduced iron (DRI) because NiO would be reduced together with iron oxide to form Fe–Ni. A small amount of Ni (about 2 wt.%) in DRI degrades the physical properties of final steel products. The current study investigated how oxidation roasting of limonitic laterite ores affected NiO reduction, with the goal of producing Ni-free DRI and Ni-bearing slag. Ni-bearing slag can be a good secondary Ni resource. Oxidation roasting made NiO inert under H2 reduction at 900 °C by forming Ni-olivine. Optimum roasting temperature was proposed by examining phase transformation of limonitic laterite ores during heating and by FactSage calculation of the equilibrium Ni fraction in Ni-bearing phases. Furthermore, the effect of Mg–silicate forming additives on the control of NiO reducibility was clarified to maximize the suppression of NiO reduction. Among various additives such as MgSiO3, Mg2SiO4 and Fe–Ni smelting slag, Ni-free olivine-typed flux was found to be the most effective form of Ni-olivine because Ni–Mg ion exchange between Ni-bearing phase and Ni-free olivine occurs more readily than other Ni-olivine formation schemes. Finally, the mechanism of Ni-olivine formation during roasting was studied using a diffusion couple test. Calculated diffusivity values of Ni in Mg2SiO4 indicated that the two major routes of Ni-olivine formation while roasting limonitic laterite ore are (1) Ni partitioning within Mg–Ni silicate before crystallization and (2) Ni diffusion from spinel to Ni free olivine after crystallization.
Keywords:Limonitic laterite  Direct reduced iron (DRI)  Ferronickel  Olivine  Roasting
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