Migration and Aggregation Behavior of Nickel and Iron in Low Grade Laterite Ore with New Additives

: This study focused on the preparation of high-grade ferronickel concentrate, the behavior of efﬁcient migration and the polymerization of ferronickel particles during reduction roasting, by adding calcium ﬂuoride and a ferronickel concentrate to low-grade laterite ore from Yunnan. The effects of temperature, holding time, reductant content, ferronickel concentrate content and magnetic ﬁeld intensity on the preparation of the ferronickel concentrate were studied and the optimum conditions were determined as follows: 30% ferronickel concentrate (metal Ni-4.68%, metal Fe-45.0%), 8% coal, 7% calcium ﬂuoride, reduction temperature of 1250 ◦ C, reduction time of 60 min and the intensity of magnetic separation is 150 mT. The proportion of nickel and iron in ferronickel concentrate was 88.7% (metal Ni-8.62%, metal Fe-80.1%), and the recovery efﬁciency of nickel and iron are 98.8% and 82.4%, respectively. X-ray diffraction and scanning electron microscopy indicated that ferronickel-concentrate, as an activating agent, improved the aggregation effect of ferronickel particles. The efﬁcient migration and polymerization of ferronickel particles in the ore signiﬁcantly increased the size of the ferronickel particles with additives, therefore a high-grade ferronickel concentrate was prepared, and the reduction and recovery efﬁciency of laterite nickel ore was improved. iron. The recovery efﬁciency of nickel decreased to 88.38% when the temperature continued to rise to 1300 ◦ C. According to kinetics analysis, the metallization efﬁciency of nickel and iron was low at lower temperatures, and it was not conducive to the polymerization of ferronickel. When the temperature increased to 1250 ◦ C, the recovery efﬁciency of nickel and iron showed a decreasing trend. This may suggest that the formation of iron olivine at this temperature affects the polymerization and growth of the ferronickel particle. A higher reduction temperature will cause material sintering, and hinder the reaction process and magnetic separation, resulting in lower nickel grade in concentrate. The results show that a suitable reduction temperature is conducive for improving the grades of iron and nickel. So, the optimum roasting temperature is 1250 ◦ C.


Introduction
Nickel is an important strategic reserve metal and plays an extremely important role in the development of the national economy [1]. The consumption of nickel resources in China ranks first in the world, but the shortage of nickel resources has become increasingly problematic. With the rapid development of the stainless-steel industry, the demand for nickel is increasing [2]. The nickel used to produce stainless steel accounts for about 65% of global nickel production. In order to cope with the present situation of high cost in stainless steel production, it has become important to develop and utilize laterite nickel ore, and produce low-cost ferronickel raw materials [3]. With the depletion of high-grade nickel sulfide ore, low-grade laterite nickel ore has gradually become the main raw material for the nickel extraction [4][5][6][7].
Laterite nickel ore is an important nickel mineral resource, which has the characteristics of large reserves, low-grade and difficult extraction behavior. In total, 70% of the laterite nickel resources in China are distributed in Yuanjiang, Yunnan Province. The nickel laterite ore was mainly comprised of lizardite, revealing the sandwich-like morphology and quartz of irregular hexagonal granular structure, characterizing it as a complex ore. The contents of silicon dioxide and magnesium oxide in the ore are high, therefore it is considered as the typical garnierite. As discussed in the literature, reduction-roasting magnetic separation process, used for various types of laterite nickel ore has the advantages of short process, friendly environment and no pollution [8][9][10].
However, the experimental results show that the process has a low recovery efficiency of nickel and iron. Some researchers have studied the effect of accelerators on the reduction and polymerization of nickel and iron in the reduction of the roasting process of laterite nickel ore. Mainly sulfur-containing additives and sodium salt additives [11,12] have obvious effects on ferronickel recovery.
Zhou et al. [13,14] studied the effect of NaCl addition on nickel minerals in reductive roasted laterite. After adding NaCl, nickel and iron in raw ore aggregated efficiently to form ferronickel alloy particles. When the roasting time was prolonged, ferronickel alloy particles were separated from serpentine, thus nickel and iron were effectively enriched in the magnetic separation process. When 10% NaCl and 8% anthracite were added into the raw ore, the reduction process was conducted out at roasting temperature of 1200 • C for 20 min, followed by 150 mT magnetic separation. The grades of nickel and iron were 7.09% and 67.9%, which are relatively low. The recovery efficiency of nickel and iron were 98.3%, 72.1%, respectively. In this research, the grades of nickel and iron were 8.62%, 80.1%. Additionally, the recovery efficiency of nickel and iron are 98.8%, 82.4%.
Some researchers showed that the utilization of approximately 10%wt Na 2 S 2 O 3 or S, resulted in a product with about 5-14% Ni content and above 90% recovery. When the nickel and iron grades of raw ore are high, the nickel and iron grades in nickel iron concentrate are high. Both Na 2 S 2 O 3 and natural sulfur additives assisted the transformation of ore mineralogy and confirm the formation of ferronickel. Additionally, the effect of sulfur on the phase transformation has been studied carefully in the process of high-temperature reduction roasting of laterite minerals. The results showed that the addition of elemental S can inhibit the formation of forsterite in the silica-magnesium laterite nickel ore, and that melted Fe-FeS eutectic is conducive to mass transfer, which promotes the migration and polymerization of ferronickel and causes the particles of ferronickel to aggregate into larger particles. For the laterite nickel ore, sulfur can lead to the formation of FeS and Fe-Ni at 500 • C, thus achieving the selective separation of nickel and iron [15][16][17]. The addition of ferronickel concentrate has a similar function. Additionally, it further enhances the aggregation of metal nickel and iron. The ferronickel concentrate is added into low-grade laterite nickel ore as a nucleating agent, and, at the same time, a reductant and accelerator are added in the reduction-roasting process. The fine ferronickel particles that have been reduced are nucleated to nickel-iron zone under the action of interfacial energy.
The migration and enrichment of nickel and iron in the field can improve the growth of ferronickel particles, which is conducive to magnetic separation and can further improve the recovery efficiency of nickel and iron [18][19][20]. The extraction of nickel and iron from low-grade laterite nickel ore presents some issues, therefore, a new method of preparing ferronickel concentrate from low-grade laterite nickel ore is proposed in this paper. The objectives of this work were to obtain high-grade ferronickel concentrate, and the migration and aggregation behavior of ferronickel under the influence of additives.

Laterite Ore
In this study, laterite nickel ore from Yunnan Province was used as the raw material. The main components of laterite nickel ore were analyzed through chemical analysis. The phase composition of the laterite ore was analyzed using a X-ray diffractometer Cu-Kα ray source, voltage of 35 kV, current of 20 mA, scanning speed of 10 • /min, the diffraction angle (2θ) was scanned from 10 • to 90 • ). The scanning electron microscope was used to further analyze the distribution of elements in the ore. TG/DSC (Netzsch Inc., Beijing, China) was used to determine the thermal properties of nickel laterite ore.

Low-Grade Ferronickel Concentrate
The ferronickel concentrate was obtained in the experiment by reduction laterite and magnetic separation laterite reduction products. Raw ore, calcium fluoride and anthracite are fully mixed and evenly packed into corundum crucible, and then reduced in a tubular furnace (GLS-1500X, Hefei kejing Material Technology Co., LTD, Beijing, China) for 60 min at 1250 • C, and then wet-grinded for 12 min. Finally, the ferronickel concentrate was separated by a magnetic separator (DTCXG-ZN50, Tangshan Dongtang Electric CO., LTD., Tangshan, China) under a magnetic field intensity of 150 mT. The main components of ferronickel concentrate were analyzed via chemical analysis (Chemical titration).

Apparatus and Procedure
At first, the ore was dried in a drying chamber, and then crushed to less than 0.25 mm in a vibration mill. Raw ore, reductant and concentrate were fully mixed and evenly packed into a corundum crucible, then placed in the constant temperature zone of the tubular furnace. The air in the tube of the furnace was discharged and the heating program was started. The sample was heated to the set temperature at a rate of 10 • C/min. In the reduction roasting process, N 2 was used as a protective gas to prevent secondary oxidation of the sample. The sample was cooled in the furnace and removed from the furnace below 200 • C. The reduced sample was taken out for wet grinding at around 12 min, and the particle size of the sample was less than 74 microns, and then the ferronickel concentrate was separated using a magnetic separator. After liquid-solid separation, the concentrate and tailings were obtained. The concentrate was dried at 150 • C, and the weight of the concentrate was measured. The flow-chart of the reduction-roasting magnetic separation experiment of laterite nickel ore are shown in Figure 1. The content of nickel and iron was analyzed, and the corresponding recovery efficiency was calculated. The specific experimental conditions and processes are shown in Figure 1. The recovery efficiency of Ni and Fe were calculated according to the following equation: where X is the recovery efficiency of nickel or iron, m is the weight of ferronickel concentrate, w is the nickel or iron content in the ferronickel concentrate, V is the weight of concentrate, Y is the nickel or iron content in the concentrate, M is the weight of raw ore, and W is the nickel or iron content in the raw ore.

The Phase Composition of Samples
The chemical analysis and XRD pattern of laterite ore is shown in Table 1 and Figure  2. The ore contained approximately 0.82 wt.% of Ni and 9.67 wt.% of Fe. The main phases included serpentine, silica and iron oxide. In Figure 3, the occurrence of Fe and O elements in the raw ore indicates that Fe in raw ore exists in the form of iron oxides. The distribution of Mg, Si and O is highly consistent, and the aggregated particles are large, and is therefore considered as serpentine. The distribution of nickel elements is dispersive, but the relatively concentrated distribution of nickel elements in Mg, Si and O regions can be clearly observed. The TG/DSC of laterite ore are shown in Figure 4. It is a typical silicon magne- The mineral phases were characterized by X-ray diffraction (Japan Science D/max-R diffractometer, Rigagu Inc., Beijing, China). To analyze and clarify the related mechanism, the microstructure of ferronickel concentrate in reduction product and the compositions of several spots in magnetic product were observed by scanning electron microscopy (SEM; HITACHI-S3400 N, Hitachi Inc., Tokyo, Japan).), equipped with energy dispersive X-ray spectroscopy (EDS, EDAX Inc., Beijing, China).

The Phase Composition of Samples
The chemical analysis and XRD pattern of laterite ore is shown in Table 1 and Figure 2. The ore contained approximately 0.82 wt. % of Ni and 9.67 wt. % of Fe. The main phases included serpentine, silica and iron oxide. In Figure 3, the occurrence of Fe and O elements in the raw ore indicates that Fe in raw ore exists in the form of iron oxides. The distribution of Mg, Si and O is highly consistent, and the aggregated particles are large, and is therefore considered as serpentine. The distribution of nickel elements is dispersive, but the relatively concentrated distribution of nickel elements in Mg, Si and O regions can be clearly observed. The TG/DSC of laterite ore are shown in Figure 4. It is a typical silicon magnesium laterite ore. The nickel content is approximately 1% and the iron content is less than 20% [2,12,16,21].

The Phase Composition of Samples
The chemical analysis and XRD pattern of laterite ore is shown in Table 1 and Figure  2. The ore contained approximately 0.82 wt.% of Ni and 9.67 wt.% of Fe. The main phases included serpentine, silica and iron oxide. In Figure 3, the occurrence of Fe and O elements in the raw ore indicates that Fe in raw ore exists in the form of iron oxides. The distribution of Mg, Si and O is highly consistent, and the aggregated particles are large, and is therefore considered as serpentine. The distribution of nickel elements is dispersive, but the relatively concentrated distribution of nickel elements in Mg, Si and O regions can be clearly observed. The TG/DSC of laterite ore are shown in Figure 4. It is a typical silicon magnesium laterite ore. The nickel content is approximately 1% and the iron content is less than 20% [2,12,16,21].     TG/DSC was used to determine the thermal properties of nickel laterite ore, as shown in Figure 4. It shows that the total weight-loss efficiency of the sample is around 12.7%. As a result of the endothermic and exothermic processes, two main peaks were observed in the DSC thermogram. The first main peak at 610 °C is the result of removal of the chem-  TG/DSC was used to determine the thermal properties of nickel laterite ore, as shown in Figure 4. It shows that the total weight-loss efficiency of the sample is around 12.7%. As a result of the endothermic and exothermic processes, two main peaks were observed in the DSC thermogram. The first main peak at 610 • C is the result of removal of the chemically bound water from the ore. The dehydration process is an endothermic reaction, the sample quality decreases slightly, and no phase transition occurs. The second main peak at 820 • C is the result of serpentine phase change from amorphous material to olivine phase with good crystallinity [22,23]. This phase transition process is an exothermic reaction, which was verified by XRD in previous experiments.
The chemical analysis results of ferronickel concentrate are shown in Table 2. The ferronickel concentrate contained approximately 4.68 wt. % of Ni and 45.0 wt. % of Fe. Anthracite was used as the reducing agent. An industrial analysis of anthracite is shown in Table 3. The calcium fluoride used in the experiment is analytically pure. The effect of the ferronickel concentrate dosage on the reduction and magnetic separation of low-grade nickel laterite ore is shown in Figure 5. The experimental conditions were determined as follows: reduction temperature of 1250 • C, roasting time of 60 min, anthracite content of 8%, calcium fluoride content of 7%, magnetic separation intensity of 150 mT. As can be seen from Figure 5, when the concentrate dosage increased from 10% to 50%, the nickel grade increased from 5.35% to 6.82%, and the recovery efficiency of the nickel increased from 96.8% to 98.3%, then decreased to 93.3%. The effect of concentrate on promoting the growth of ferronickel particles is not clear as the recovery efficiency of nickel decreases with the increase of the amount of ferronickel concentrate added. The grade and recovery efficiency of iron first increased and then decreased. The addition of concentrate can effectively reduce the content of silicon and magnesium. In addition, ferronickel concentrate, as an activating agent, can promote the growth of ferronickel grains, and effectively separate the ferronickel alloy from the sample reduced by a magnetic separation process, and improve the grade of nickel in the alloy. Given these results, the optimum dosage of concentrate is 30%.
The effect of the ferronickel concentrate dosage on the reduction and m ration of low-grade nickel laterite ore is shown in Figure 5. The experimen were determined as follows: reduction temperature of 1250 °C, roasting t anthracite content of 8%, calcium fluoride content of 7%, magnetic separati 150 mT. As can be seen from Figure 5, when the concentrate dosage increa to 50%, the nickel grade increased from 5.35% to 6.82%, and the recovery ef nickel increased from 96.8% to 98.3%, then decreased to 93.3%. The effect on promoting the growth of ferronickel particles is not clear as the recover nickel decreases with the increase of the amount of ferronickel concentra grade and recovery efficiency of iron first increased and then decreased. T concentrate can effectively reduce the content of silicon and magnesium. In ronickel concentrate, as an activating agent, can promote the growth of ferr and effectively separate the ferronickel alloy from the sample reduced by a aration process, and improve the grade of nickel in the alloy. Given these r timum dosage of concentrate is 30%. Figure 5. The effect of ferronickel concentrate dosage on the grade and recovery of (The reducing temperature was 1250 °C, the roasting duration was 60 min, the re was 8 wt.%, the magnetic separation was 150 mT).

Effects of Roasting Temperature
The effect of roasting temperature on the reduction and magnetic separation of lowgrade nickel laterite ore is shown in Figure 6. The experimental conditions were determined as follows: ferronickel concentrate dosage of 30%, roasting time of 60 min, anthracite content of 8%, calcium fluoride content of 7%, and magnetic separation intensity of 150 mT. As can be seen from Figure 6, the reduction temperature has an obvious effect on the grade and recovery efficiency of iron and nickel. With an increase in the reduction temperature, the grades of nickel and iron clearly increase and then tend to become stable, while the recovery efficiency of iron and nickel increases and then decreases. When the temperature increased from 1100 to 1250 • C, the grade of nickel had no obvious change, but the grade of iron increased from 44.0% to 63.8%, and the recovery efficiency of nickel and iron were 98.3% and 95.2%, respectively. This indicates that the reduction efficiency increased with the increase in temperature and more nickel-iron oxides were reduced to metal nickel and iron. The recovery efficiency of nickel decreased to 88.38% when the temperature continued to rise to 1300 • C. According to kinetics analysis, the metallization efficiency of nickel and iron was low at lower temperatures, and it was not conducive to the polymerization of ferronickel. When the temperature increased to 1250 • C, the recovery efficiency of nickel and iron showed a decreasing trend. This may suggest that the formation of iron olivine at this temperature affects the polymerization and growth of the ferronickel particle. A higher reduction temperature will cause material sintering, and hinder the reaction process and magnetic separation, resulting in lower nickel grade in concentrate. The results show that a suitable reduction temperature is conducive for improving the grades of iron and nickel. So, the optimum roasting temperature is 1250 • C.
while the recovery efficiency of iron and nickel increases and then decreases. W temperature increased from 1100 to 1250 °C, the grade of nickel had no obvious but the grade of iron increased from 44.0% to 63.8%, and the recovery efficiency and iron were 98.3% and 95.2%, respectively. This indicates that the reduction e increased with the increase in temperature and more nickel-iron oxides were red metal nickel and iron. The recovery efficiency of nickel decreased to 88.38% w temperature continued to rise to 1300 °C. According to kinetics analysis, the meta efficiency of nickel and iron was low at lower temperatures, and it was not cond the polymerization of ferronickel. When the temperature increased to 1250 °C, th ery efficiency of nickel and iron showed a decreasing trend. This may suggest formation of iron olivine at this temperature affects the polymerization and grow ferronickel particle. A higher reduction temperature will cause material sinter hinder the reaction process and magnetic separation, resulting in lower nickel concentrate. The results show that a suitable reduction temperature is conduciv proving the grades of iron and nickel. So, the optimum roasting temperature is 1 Figure 6. The effect of temperature on the grade and recovery of nickel and iron in ferron centrate. (The ferronickel concentrate dosage was 30 wt.%, the roasting duration was 60 reductant dosage was 8 wt.%, the magnetic separation was 150 mT).

Effects of Roasting Time
The effect of the roasting time on the reduction and magnetic separation of lo nickel laterite ore is shown in Figure 7. The experimental conditions were determ follows: ferronickel concentrate dosage of 30%, reduction temperature of 1250 °C cite content of 8%, calcium fluoride content of 7%, and magnetic separation inte 150 mT. As can be seen from Figure 7, with the increase in the roasting time, the g nickel and iron first increased and then decreased. The grades of nickel and iron

Effects of Roasting Time
The effect of the roasting time on the reduction and magnetic separation of low-grade nickel laterite ore is shown in Figure 7. The experimental conditions were determined as follows: ferronickel concentrate dosage of 30%, reduction temperature of 1250 • C, anthracite content of 8%, calcium fluoride content of 7%, and magnetic separation intensity of 150 mT. As can be seen from Figure 7, with the increase in the roasting time, the grades of nickel and iron first increased and then decreased. The grades of nickel and iron reached their peak at approximately 60 min. With the increase in roasting time, more nickel oxides were reduced to nickel metal, which made the grade of nickel increase in the ferronickel concentrate. Considering the energy consumption, the optimum roasting time was found to be 60 min. their peak at approximately 60 min. With the increase in roasting time, more n were reduced to nickel metal, which made the grade of nickel increase in the concentrate. Considering the energy consumption, the optimum roasting time to be 60 min. The effect of reductant dosage on the reduction and magnetic separat grade nickel laterite ore is shown in Figure 8. The experimental conditions mined as follows：ferronickel concentrate dosage of 30%, reduction tempera °C, roasting time of 60 min, calcium fluoride content of 7%, magnetic separati of 150 mT. As can be seen from Figure 8, with the increase of reductant dosag of nickel in ferronickel-concentrate first increased and then decreased, while t iron increased. When reductant dosage increased from 4% to 10%, the nick creased from 5.66% to 7.45%, and the recovery efficiency of nickel increased to 96.3%. However, when the reductant dosage increased to 12%, the grade o decreased to 6.44%, and the recovery efficiency of nickel was 90.5%. Increasing ant dosage can reduce the metal oxides, but excessive residual anthracite will amount of residual carbon, and produce more ash, which leads to the difficul tion and aggregation of ferronickel after reduction. Therefore, the smaller ferr ticles are wrapped by impurities and cannot be separated effectively by magn tion. In addition, a large amount of iron oxide becomes reduced to the concent sive residual anthracite causes the decrease of the nickel grade in concentrat the optimum amount of reductant is 8%. The effect of reductant dosage on the reduction and magnetic separation of low-grade nickel laterite ore is shown in Figure 8. The experimental conditions were determined as follows: ferronickel concentrate dosage of 30%, reduction temperature of 1250 • C, roasting time of 60 min, calcium fluoride content of 7%, magnetic separation intensity of 150 mT. As can be seen from Figure 8, with the increase of reductant dosage, the grade of nickel in ferronickel-concentrate first increased and then decreased, while the grade of iron increased. When reductant dosage increased from 4% to 10%, the nickel grade increased from 5.66% to 7.45%, and the recovery efficiency of nickel increased from 67.0% to 96.3%. However, when the reductant dosage increased to 12%, the grade of the nickel decreased to 6.44%, and the recovery efficiency of nickel was 90.5%. Increasing the reductant dosage can reduce the metal oxides, but excessive residual anthracite will increase the amount of residual carbon, and produce more ash, which leads to the difficulty of migration and aggregation of ferronickel after reduction. Therefore, the smaller ferronickel particles are wrapped by impurities and cannot be separated effectively by magnetic separation. In addition, a large amount of iron oxide becomes reduced to the concentrate. Excessive residual anthracite causes the decrease of the nickel grade in concentrate, therefore the optimum amount of reductant is 8%.

Effects of Magnetic Separation
The effect of magnetic separation on the reduction and magnetic separa grade nickel laterite ore is shown in Figure 9. The experimental conditions mined as follows: ferronickel concentrate dosage of 30%, reduction tempera °C, roasting time of 60 min, reductant dosage of 8%, calcium fluoride conten can be seen from Figure 9, with an increase in the magnetic field intensity, th iron and nickel in ferronickel concentrate decreased, but the corresponding re ciency increased. This is because that the different size of nickel-iron particle in the roasting process caused different forces of these particles in a ma thereby affecting the magnetic separation effect. The larger particles were easi for the magnetic field. When the magnetic field was weak, the small ferronic and some metallic iron inclusions did not become adsorbed by the magnetic ing that the grades of iron and nickel were higher, but the recovery efficien With the increase in magnetic field intensity, these weak magnetic materials e ronickel concentrate, which reduces the grades of iron and nickel, but the re ciency of iron and nickel increased. Based on the grades and recovery effici and nickel in ferronickel concentrate, magnetic field intensity of 150 mT is op dition.

Effects of Magnetic Separation
The effect of magnetic separation on the reduction and magnetic separation of lowgrade nickel laterite ore is shown in Figure 9. The experimental conditions were determined as follows: ferronickel concentrate dosage of 30%, reduction temperature of 1250 • C, roasting time of 60 min, reductant dosage of 8%, calcium fluoride content of 7%. As can be seen from Figure 9, with an increase in the magnetic field intensity, the grades of iron and nickel in ferronickel concentrate decreased, but the corresponding recovery efficiency increased. This is because that the different size of nickel-iron particles generated in the roasting process caused different forces of these particles in a magnetic field, thereby affecting the magnetic separation effect. The larger particles were easier to adsorb for the magnetic field. When the magnetic field was weak, the small ferronickel particles and some metallic iron inclusions did not become adsorbed by the magnetic field, meaning that the grades of iron and nickel were higher, but the recovery efficiency was low. With the increase in magnetic field intensity, these weak magnetic materials enter the ferronickel concentrate, which reduces the grades of iron and nickel, but the recovery efficiency of iron and nickel increased. Based on the grades and recovery efficiency of iron and nickel in ferronickel concentrate, magnetic field intensity of 150 mT is optimum condition. In conclusion, the optimum technological conditions for preparing high grade ferro nickel concentrate, through the addition of ferronickel concentrate using a reductio roasting-magnetic separation method are as follows: concentrate dosage of 30% and an thracite dosage of 8%, reduction temperature of 1250 °C, roasting time of 60 min, magnet separation intensity of 150 mT. Under these conditions, the grades of nickel and iron i ferronickel concentrate were 8.62% and 80.1%, and the recovery efficiency of nickel an iron were 98.8% and 82.4%. Compared with the nickel grade in the raw ore (Ni-0.820% Fe-9.67%), it is increased by about 10 times and about 8 times compared with the iro grade.
According to a literature review [13][14][15][16][17], when the additive was Na2S2O3 or S, th laterite nickel ore (1.59% of Ni and 42.0% of Fe) was reduced and melted. It was gotte that 14.3% Ni content and 93.2% recovery, the iron content was 64% and the recovery wa about 19.0%. The grade of nickel increased by 9 times and grade of iron increased by 1 times. When the additive is sulfur, it yielded a product with 13.6% Ni content and its re covery reaching 97.9%. Additionally, the iron content was 53.4% and the recovery wa around 20%. The grade of nickel increased by 8.5 times and the grade of iron increased b 1.2 times. When the additive was NaCl, laterite ore (0.820% of Ni and 9.67% of Fe) wa reduced and melted. The results indicate that for a ferronickel content of 7.09% Ni, 70% Fe, a nickel recovery of 98.3%, a Fe recovery of 72.1%. The grade of nickel in-creased b 8.6 times and grade of iron increased by 7.2 times. In this case, the aggregation efficienc and recovery of nickel and iron in this study are higher. Figure 10 shows an SEM image of the reduction sample under the action of the pro moter CaF2. After adding CaF2, part of the nickel and iron oxides was reduced, and th ferronickel concentrate was distributed in a bright white granular form. The grey area FeO, and the darker area is forsterite [Mg2SiO4]. The study suggested that CaF2, as a pro moter, can effectively destroy the mineral lattice which loaded nickel and iron, and reduc the surface tension of the mineral, and promote the metallization and reduction of nick In conclusion, the optimum technological conditions for preparing high grade ferronickel concentrate, through the addition of ferronickel concentrate using a reduction roasting-magnetic separation method are as follows: concentrate dosage of 30% and anthracite dosage of 8%, reduction temperature of 1250 • C, roasting time of 60 min, magnetic separation intensity of 150 mT. Under these conditions, the grades of nickel and iron in ferronickel concentrate were 8.62% and 80.1%, and the recovery efficiency of nickel and iron were 98.8% and 82.4%. Compared with the nickel grade in the raw ore (Ni-0.820%, Fe-9.67%), it is increased by about 10 times and about 8 times compared with the iron grade.

Polymerization and Growth of Ferronickel Particles
According to a literature review [13][14][15][16][17], when the additive was Na 2 S 2 O 3 or S, the laterite nickel ore (1.59% of Ni and 42.0% of Fe) was reduced and melted. It was gotten that 14.3% Ni content and 93.2% recovery, the iron content was 64% and the recovery was about 19.0%. The grade of nickel increased by 9 times and grade of iron increased by 1.5 times. When the additive is sulfur, it yielded a product with 13.6% Ni content and its recovery reaching 97.9%. Additionally, the iron content was 53.4% and the recovery was around 20%. The grade of nickel increased by 8.5 times and the grade of iron increased by 1.2 times. When the additive was NaCl, laterite ore (0.820% of Ni and 9.67% of Fe) was reduced and melted. The results indicate that for a ferronickel content of 7.09% Ni, 70% Fe, a nickel recovery of 98.3%, a Fe recovery of 72.1%. The grade of nickel in-creased by 8.6 times and grade of iron increased by 7.2 times. In this case, the aggregation efficiency and recovery of nickel and iron in this study are higher. Figure 10 shows an SEM image of the reduction sample under the action of the promoter CaF 2 . After adding CaF 2 , part of the nickel and iron oxides was reduced, and the ferronickel concentrate was distributed in a bright white granular form. The grey area is FeO, and the darker area is forsterite [Mg 2 SiO 4 ]. The study suggested that CaF 2 , as a promoter, can effectively destroy the mineral lattice which loaded nickel and iron, and reduce the surface tension of the mineral, and promote the metallization and reduction of nickel and iron. Figure 11 shows an SEM image of the reduction sample during the addition of ferronickel concentrate. It can be clearly seen from Figure 11 that the nickel-iron solid solution changes from the original granular distribution to the band shape, indicating that the addition of the ferronickel concentrate can significantly promote the accumulation of ferronickel particles. Figure 12 shows an SEM image of the reduction roasting sample after adding CaF 2 and the ferronickel concentrate. It can be clearly seen from Figure 12 that there are a large number of bright white-banded solids of nickel and iron, indicating that the combined action of calcium fluoride and ferronickel concentrate can significantly improve the reduction roasting effect. An EDS analysis of the reduction samples shows that the contents of nickel and iron in the ferronickel concentrate phase were higher under the condition of adding ferronickel concentrate, which further indicates that the addition of the ferronickel concentrate can effectively promote the aggregation and growth of ferronickel particles.

Polymerization and Growth of Ferronickel Particles
Metals 2021, 11, x FOR PEER REVIEW 11 of 16 ferronickel concentrate. It can be clearly seen from Figure 11 that the nickel-iron solid solution changes from the original granular distribution to the band shape, indicating that the addition of the ferronickel concentrate can significantly promote the accumulation of ferronickel particles. Figure 12 shows an SEM image of the reduction roasting sample after adding CaF2 and the ferronickel concentrate. It can be clearly seen from Figure 12 that there are a large number of bright white-banded solids of nickel and iron, indicating that the combined action of calcium fluoride and ferronickel concentrate can significantly improve the reduction roasting effect. An EDS analysis of the reduction samples shows that the contents of nickel and iron in the ferronickel concentrate phase were higher under the condition of adding ferronickel concentrate, which further indicates that the addition of the ferronickel concentrate can effectively promote the aggregation and growth of ferronickel particles.    ferronickel concentrate. It can be clearly seen from Figure 11 that the nickel-iron solid solution changes from the original granular distribution to the band shape, indicating that the addition of the ferronickel concentrate can significantly promote the accumulation of ferronickel particles. Figure 12 shows an SEM image of the reduction roasting sample after adding CaF2 and the ferronickel concentrate. It can be clearly seen from Figure 12 that there are a large number of bright white-banded solids of nickel and iron, indicating that the combined action of calcium fluoride and ferronickel concentrate can significantly improve the reduction roasting effect. An EDS analysis of the reduction samples shows that the contents of nickel and iron in the ferronickel concentrate phase were higher under the condition of adding ferronickel concentrate, which further indicates that the addition of the ferronickel concentrate can effectively promote the aggregation and growth of ferronickel particles.    As shown in Figure 12, after CaF2 and ferronickel concentrate were added, nickel and iron became clearly aggregated. Additionally, CaF2 plays an important role. The CaF2 decomposes into Ca 2+ and F − at high temperature. F − and O 2− have the same ionic radius. In the reduction process, F − enters into the silicate structure, which is composed of a Si-O tetrahedral structure. Reducing the bond energy of Si-O makes it more susceptible to fracturing at high temperatures, therefore, reducing the melting point of silicate. In the actual reduction process, the CaF2 react complicatedly with the serpentine (Mg3Si2O5(OH)4) of the gangue phase to form tremolite (CaxMgy (Si4O11)2F2, X 2; y 5), which has a low melting point. Then, the decrease of the melting point of the whole reduction system can increase the diffusion coefficient of atoms, accelerate the atomic movement rate between reactants and promote the precipitation of metal particles along the boundary, and the rapid aggregation between particles. Figure 13 shows the schematic diagram of a diffusion experiment sample. the first and third layers were raw ore, mixed with anthracite and additives, and the second layer was concentrated. The prepared samples were reduced in a tubular furnace under the reduction conditions for 60 min at 1250 °C, and the reduction samples were analyzed.  Figure 14 shows an SEM of reduced concentrate samples. Figure 14a shows the SEM of the DC1 interface layer on the surface of the reduced concentrate samples. Nickel and As shown in Figure 12, after CaF 2 and ferronickel concentrate were added, nickel and iron became clearly aggregated. Additionally, CaF 2 plays an important role. The CaF 2 decomposes into Ca 2+ and F − at high temperature. F − and O 2− have the same ionic radius. In the reduction process, F − enters into the silicate structure, which is composed of a Si-O tetrahedral structure. Reducing the bond energy of Si-O makes it more susceptible to fracturing at high temperatures, therefore, reducing the melting point of silicate. In the actual reduction process, the CaF 2 react complicatedly with the serpentine (Mg 3 Si 2 O 5 (OH) 4 ) of the gangue phase to form tremolite (Ca x Mg y (Si 4 O 11 ) 2 F 2 , X ≈ 2; y ≈ 5), which has a low melting point. Then, the decrease of the melting point of the whole reduction system can increase the diffusion coefficient of atoms, accelerate the atomic movement rate between reactants and promote the precipitation of metal particles along the boundary, and the rapid aggregation between particles. Figure 13 shows the schematic diagram of a diffusion experiment sample. the first and third layers were raw ore, mixed with anthracite and additives, and the second layer was concentrated. The prepared samples were reduced in a tubular furnace under the reduction conditions for 60 min at 1250 • C, and the reduction samples were analyzed. As shown in Figure 12, after CaF2 and ferronickel concentrate were added, nickel and iron became clearly aggregated. Additionally, CaF2 plays an important role. The CaF2 decomposes into Ca 2+ and F − at high temperature. F − and O 2− have the same ionic radius. In the reduction process, F − enters into the silicate structure, which is composed of a Si-O tetrahedral structure. Reducing the bond energy of Si-O makes it more susceptible to fracturing at high temperatures, therefore, reducing the melting point of silicate. In the actual reduction process, the CaF2 react complicatedly with the serpentine (Mg3Si2O5(OH)4) of the gangue phase to form tremolite (CaxMgy (Si4O11)2F2, X 2; y 5), which has a low melting point. Then, the decrease of the melting point of the whole reduction system can increase the diffusion coefficient of atoms, accelerate the atomic movement rate between reactants and promote the precipitation of metal particles along the boundary, and the rapid aggregation between particles. Figure 13 shows the schematic diagram of a diffusion experiment sample. the first and third layers were raw ore, mixed with anthracite and additives, and the second layer was concentrated. The prepared samples were reduced in a tubular furnace under the reduction conditions for 60 min at 1250 °C, and the reduction samples were analyzed.  Figure 14 shows an SEM of reduced concentrate samples. Figure 14a shows the SEM of the DC1 interface layer on the surface of the reduced concentrate samples. Nickel and  Figure 14 shows an SEM of reduced concentrate samples. Figure 14a shows the SEM of the DC1 interface layer on the surface of the reduced concentrate samples. Nickel and iron oxides were reduced and metallized, and the ferronickel were migrated and aggregated, but the effect of aggregation and growth is not obvious. It is difficult to enrich the fine ferronickel phase by magnetic separation. Figure 14b shows an SEM of the DC2 interface layer on the cross section of the contact between raw ore and concentrate. A large number of bright white and light gray particles are visible in Figure 14b. A large number of bright white bands were formed, as illustrated. The new mineral phases were aggregated to the ferronickel phase. The energy spectrum analysis shows that the main phase in the bright white area of the roasted ore was ferronickel alloy, the main phase in the light gray area was spinel, and the main phase in the light black area was mafic olivine. This indicates that the metallic nickel and iron in the ore migrates and enriches the ferronickel concentrate during reduction roasting, and the size of ferronickel particles significantly increased, which effectively promotes the formation of ferronickel alloy. iron oxides were reduced and metallized, and the ferronickel were migrated and aggregated, but the effect of aggregation and growth is not obvious. It is difficult to enrich the fine ferronickel phase by magnetic separation. Figure 14b shows an SEM of the DC2 interface layer on the cross section of the contact between raw ore and concentrate. A large number of bright white and light gray particles are visible in Figure 14b. A large number of bright white bands were formed, as illustrated. The new mineral phases were aggregated to the ferronickel phase. The energy spectrum analysis shows that the main phase in the bright white area of the roasted ore was ferronickel alloy, the main phase in the light gray area was spinel, and the main phase in the light black area was mafic olivine. This indicates that the metallic nickel and iron in the ore migrates and enriches the ferronickel concentrate during reduction roasting, and the size of ferronickel particles significantly increased, which effectively promotes the formation of ferronickel alloy.  Figure 15 shows the SEM of the cross section of DC3. Figure 16 shows the elemental mapping results of DC3. The enrichment of ferronickel particles in the boundary layer between raw ore and concentrate is evident.   Figure 15 shows the SEM of the cross section of DC3. Figure 16 shows the elemental mapping results of DC3. The enrichment of ferronickel particles in the boundary layer between raw ore and concentrate is evident. The Ni and Fe contents along a line of selected points were obtained by electron probe shown in Figure 17. When the points of interest were selected, positions that included high contents of nickel and iron were not considered, because these positions represented the alloy phase area. The results show that the nickel and iron contents are highest near the boundary line, and the further away from the boundary line, the lower the contents of nickel and iron at the selected point line. This result is consistent with the elemental mapping results of DC3. The ferronickel particles in the raw ore diffused and migrated to the side of the ferronickel concentrate in the reaction process. The Ni and Fe contents along a line of selected points were obtained by electron probe shown in Figure 17. When the points of interest were selected, positions that included high contents of nickel and iron were not considered, because these positions represented the alloy phase area. The results show that the nickel and iron contents are highest near the boundary line, and the further away from the boundary line, the lower the contents of nickel and iron at the selected point line. This result is consistent with the elemental mapping results of DC3. The ferronickel particles in the raw ore diffused and migrated to the side of the ferronickel concentrate in the reaction process.

Conclusions
In this study, ferronickel concentrate from low-grade laterite nickel ore in Yunnan Province was prepared, and the migration and accumulation behavior of ferronickel particles in the reduction process were studied. The conclusions are as follows: (1) The ferronickel concentrate, with 8.62% Ni and 80.1% Fe was prepared through reduction roasting at 1250 °C for 60 min in the presence of 30% ferronickel concentrate  The Ni and Fe contents along a line of selected points were obtained by shown in Figure 17. When the points of interest were selected, positions high contents of nickel and iron were not considered, because these positio the alloy phase area. The results show that the nickel and iron contents a the boundary line, and the further away from the boundary line, the lower nickel and iron at the selected point line. This result is consistent with the e ping results of DC3. The ferronickel particles in the raw ore diffused and m side of the ferronickel concentrate in the reaction process.

Conclusions
In this study, ferronickel concentrate from low-grade laterite nickel Province was prepared, and the migration and accumulation behavior of f ticles in the reduction process were studied. The conclusions are as follow (1) The ferronickel concentrate, with 8.62% Ni and 80.1% Fe was prepar duction roasting at 1250 °C for 60 min in the presence of 30% ferronic

Conclusions
In this study, ferronickel concentrate from low-grade laterite nickel ore in Yunnan Province was prepared, and the migration and accumulation behavior of ferronickel particles in the reduction process were studied. The conclusions are as follows: (1) The ferronickel concentrate, with 8.62% Ni and 80.1% Fe was prepared through reduction roasting at 1250 • C for 60 min in the presence of 30% ferronickel concentrate and 8% anthracite, followed by 150 mT wet magnetic separation. The corresponding recovery efficiency of Ni and Fe were 98.8% and 82.4%, respectively. (2) Ferronickel concentrate, used as an activating agent, can clearly improve the migration, aggregation and growth of the metal phase in the reduction process of laterite nickel ore. The effective separation of the ferronickel alloy from forsterite is achieved, and the grades and recovery efficiency of nickel and iron elements in raw ore are significantly improved. (3) An SEM and EDS analysis indicated that ferronickel concentrate, acting as an activating agent, enhanced ferronickel-particle growth. The nickel and iron in the ore migrated to the ferronickel concentrate and significantly increased the size of the ferronickel particles to prepare higher grade ferronickel concentrate.