Abstract

Nickel laterite ore is divided into three layers and the garnierite examined in this study belongs to the third layer. Garnierite is characterized by high magnesium and silicon contents. The main contents of garnierite are silicates, and nickel, iron, and magnesium exist in silicates in the form of lattice exchange. Silicate minerals are difficult to destroy so are suitable for smelting using high-temperature pyrometallurgy. To solve the problem of the large amounts of slag produced and the inability to recycle the magnesium in the traditional pyrometallurgical process, we propose a vacuum carbothermal reduction and magnetic separation process to recover nickel, iron, and magnesium from garnierite, and the behavior of the additive CaF2 in the reduction process was investigated. Experiments were conducted under pressures ranging from 10 to 50 Pa with different proportions of CaF2 at different temperatures. The experimental data were obtained by various methods, such as thermogravimetry, differential scanning calorimetry, scanning electron microscopy, energy dispersive spectrometry, X-ray diffraction, and inductively coupled plasma atomic emission spectroscopy. The analysis results indicate that CaF2 directly reacted with Mg2SiO4, MgSiO3, Ni2SiO4, and Fe2SiO4, which were isolated from the bearing minerals, to produce low-melting-point compounds (FeF2, MgF2, NiF2, etc.) at 1315 and 1400 K. This promoted the conversion of the raw materials from a solid–solid reaction to a liquid–liquid reaction, accelerating the mass transfer and the heat transfer of Fe–Ni particles, and formed Si–Ni–Fe alloy particles with diameters of approximately of 20 mm. The smelting materials appeared stratified, hindering the reduction of magnesium. The results of the experiments indicate that at 1723 K, the molar ratio of ore/C was 1:1.2, the addition of CaF2 was 3%, the recovery of Fe and Ni reached 82.97% and 98.21% in the vacuum carbothermal reduction–magnetic separation process, respectively, and the enrichment ratios of Fe and Ni were maximized, reaching 3.18 and 9.35, respectively.

Highlights

  • Hydrometallurgical techniques are techniquespyrometallurgical are more applicable to limonitic ore, which includes ammonia–ammonium carbonate more applicable to acid limonitic ore, (PAL), which includes ammonia–ammonium leaching,Garnierite pressure leaching, pressure leaching and high-pressure acid leachingcarbonate (HPAL) [14,15,16,17,18,19,20]

  • The X-ray diffraction (XRD) analysis and the chemical analysis of the sample are shown in Figure 2 and Table 1

  • K, as shown in Figureat4.the end of the experiment; no melting occurred at the experimental temperature when the addition of CaF2 was 0%

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Summary

Introduction

Nickel is an important metal in the modern world, used in stainless steel, electroplating, Nickel isbatteries, an important metal in the world, used quality in stainless electroplating, rechargeable and super alloys [1,2]modern to improve peoples’of life,steel, and widely used in rechargeable batteries, and super alloys [1,2]to improve peoples’quality of life, and widely used in improving human health in nickel-containing medical devices, medical artificial bones, stents, and improving human health in nickel-containing devices, medical artificial bones, stents, of and new new anticancer drugs [3,4,5,6].With the increasemedical of demand for nickel and the rapid depletion nickel anticancerWith the increase of demand for nickel andlaterite the rapid of nickel sulfide sulfide ore,drugs more[3,4,5,6].attention is being paid to low-grade nickel oredepletion [7,8,9]. Nickel ore, more is beinginto paid to low-grade laterite [7,8,9]. Nickel laterite ore laterite oreattention can be divided three categories:nickel limonitic ore,ore transition ore, and garnierite [10,11,12]. Can be divided into three categories: limonitic ore,layer, transition ore, and garnierite [10,11,12].using. Hydrometallurgical techniques are techniquespyrometallurgical are more applicable to limonitic ore, which includes ammonia–ammonium carbonate more applicable to acid limonitic ore, (PAL), which includes ammonia–ammonium leaching,Garnierite pressure leaching, pressure leaching and high-pressure acid leachingcarbonate (HPAL) [14,15,16,17,18,19,20].

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