Thermal Beneﬁciation of Sra Ouertane (Tunisia) Low-Grade Phosphate Rock

: Low-grade phosphate rock from Sra Ouertane (Tunisia) was beneﬁciated using a thermal treatment consisting of calcination, quenching, and disliming. Untreated phosphate rock samples (group 1), calcined phosphate rock samples (group 2), as well as calcined, quenched, and dislimed (group 3) phosphate rock samples, were investigated using inductively-coupled plasma atomic emission spectroscopy (ICP-AES), inductively-coupled plasma mass spectrometry (ICP-MS), thermogravimetric analysis (TGA), and X-ray powder di ﬀ raction (XRD). Besides, the particle size distribution of the aforementioned three groups was determined. The proposed thermal treatment successfully increased the P 2 O 5 content of the untreated phosphate rock from 20.01 wt% (group 1) to 24.24 wt% (group 2) after calcination and, ﬁnally, 27.24 wt% (group 3) after calcination, quenching, and disliming. It was further found that the concentration of relevant accompanying rare earth elements (Ce, La, Nd, Pr, Sm, and Y) was increased and that the concentration of Cd could be signiﬁcantly reduced from 30 mg / kg to 14 mg / kg with the proposed treatment. The resulting phosphate concentrate showed relatively high concentrations in metal oxides: Σ MgO, Fe 2 O 3 , Al 2 O 3 = 3.63 wt% and silica (9.81 wt%) so that it did not meet the merchant grade speciﬁcations of a minimum P 2 O 5 content of 30 wt% yet. Removal of these elements could be achieved using additional appropriate separation techniques. calcination, quenching, and disliming.


Introduction
Phosphate rock plays a critical economic role in Tunisia and other countries worldwide. The increasing demand for phosphate rock for fertilizer production and its importance in animal feedstocks, as well as food-grade phosphates and other industrial uses, further solidifies the importance of the phosphate industry in these countries. The demand for phosphate rock is typically fulfilled through phosphate rock mining. The phosphate industry mined nearly 250 million tons of phosphate rock in 2018 [1]. In Tunisia, the phosphate rock industry is of considerable importance to the country's economy. Since the discovery of Tunisian phosphate deposits in the 19th century, phosphate production is controlled and operated by the Gafsa Phosphate Company (CPG, Compagnie des Phosphates de Gafsa, Gafsa, Tunisia). Tunisia has three major phosphate rock deposits: the Northern Basin, the Eastern Basin, and the Gafsa Basin. Figure 1 provides a brief overview of the major phosphate rock deposits in Tunisia. Currently, more than 90% of the phosphate rock produced in Tunisia is mined from the Gafsa Basin. Tunisia possesses other large phosphate rock deposits with reserves matching those of the Gafsa Basin in quantity but not in quality with regards to the phosphorous (P) content [2]. These deposits are in Sra Ouertane, which is part of the Northern Basin. Up to date, these reserves have not been exploited [3]. With the increased interest in mining of phosphate rock and other monetarily valuable accompanying elements, such as rare earth elements (REEs) and uranium [4][5][6][7][8][9][10][11], presently considered low P-grade deposits are becoming increasingly relevant. Table 1 provides an overview of the typical P2O5, REEs, and uranium concentrations of some mine sites in the Northern-, Eastern-, and Gafsa Basin for which detailed data was made available for this study. The Sra Ouertane low-grade phosphate rock deposit in northern Tunisia can be characterized as a deposit with relatively high uranium and REE content compared to other deposits in Tunisia [12][13][14][15][16][17][18]. The relatively large amount of impurities found in the Sra Ouertane deposit make beneficiation using flotation technically challenging [21][22][23]. Calcination is, therefore, considered here for P2O5 concentration. Calcination can largely remove carbonates and organic matter from the phosphate rocks. Organic matter can lead to increased use of sulfuric acid for the digestion process that consequently increases overall production costs [24][25][26]. In this basic technical study, the economics of such a calcination system were not considered yet. The location in Tunisia provides excellent conditions for concentrated solar power, and we hope that phosphate rock from Sra Ouertane could ultimately be heat treated using solar-powered calcination systems. Reliable cost estimations of the Currently, more than 90% of the phosphate rock produced in Tunisia is mined from the Gafsa Basin. Tunisia possesses other large phosphate rock deposits with reserves matching those of the Gafsa Basin in quantity but not in quality with regards to the phosphorous (P) content [2]. These deposits are in Sra Ouertane, which is part of the Northern Basin. Up to date, these reserves have not been exploited [3]. With the increased interest in mining of phosphate rock and other monetarily valuable accompanying elements, such as rare earth elements (REEs) and uranium [4][5][6][7][8][9][10][11], presently considered low P-grade deposits are becoming increasingly relevant. Table 1 provides an overview of the typical P 2 O 5 , REEs, and uranium concentrations of some mine sites in the Northern-, Eastern-, and Gafsa Basin for which detailed data was made available for this study. The Sra Ouertane low-grade phosphate rock deposit in northern Tunisia can be characterized as a deposit with relatively high uranium and REE content compared to other deposits in Tunisia [12][13][14][15][16][17][18]. The relatively large amount of impurities found in the Sra Ouertane deposit make beneficiation using flotation technically challenging [21][22][23]. Calcination is, therefore, considered here for P 2 O 5 concentration. Calcination can largely remove carbonates and organic matter from the phosphate rocks. Organic matter can lead to increased use of sulfuric acid for the digestion process that consequently increases overall production costs [24][25][26]. In this basic technical study, the economics of such a calcination system were not considered yet. The location in Tunisia provides excellent conditions for concentrated solar power, and we hope that phosphate rock from Sra Ouertane could ultimately be heat treated using solar-powered calcination systems. Reliable cost estimations of the total treatment costs with such solar-powered systems can be provided at a higher technology readiness level.
Currently, approximately 10% of the phosphate rock processed worldwide is calcined [27]. Further depletion of higher grade phosphate rock resources, as well as technical innovations, such as solar-driven calcination of phosphate rocks [28,29], may increase the percentage of phosphate rocks that will be calcined in the future. Previously thermal beneficiation of Tunisian phosphate rock with aluminum silicates [30] and ammonium sulfate [31] has been studied. Furthermore, calcination of Gafsa-Metloui: Jebel Oum El Khacheb deposit [32] and Ras-Dhara deposit [33], as well as M'dhilla [34] phosphate rock, has been investigated, and Jaballi et al. [35] analyzed the thermal behavior of phosphate rocks from the Ypresian phosphate deposit. Besides, Daik et al. [36] and Dabbebi et al. [37] looked into the calcination of phosphate washing waste from the Gafsa-Metloui deposit. The objective of this work was to examine the technical feasibility of a thermal beneficiation path for Sra Ouertane low-grade phosphate rock using calcination, quenching, and disliming.

Materials and Methods
The Sra Ouertane deposit consists of three phosphate rock layers (A1, A2, and C). Stratigraphic information of the Sra Ouertane deposit is provided in Figure 2. Samples from layers A1, A2, and C were made available for this study. The usual P 2 O 5 concentration of the different layers is as follows: A1 (15-21 wt% P 2 O 5 ), A2 (8-13 wt% P 2 O 5 ), and C (10-13 wt% P 2 O 5 ).
Minerals 2020, 10 3 of 13 total treatment costs with such solar-powered systems can be provided at a higher technology readiness level.
Currently, approximately 10% of the phosphate rock processed worldwide is calcined [27]. Further depletion of higher grade phosphate rock resources, as well as technical innovations, such as solar-driven calcination of phosphate rocks [28,29], may increase the percentage of phosphate rocks that will be calcined in the future. Previously thermal beneficiation of Tunisian phosphate rock with aluminum silicates [30] and ammonium sulfate [31] has been studied. Furthermore, calcination of Gafsa-Metloui: Jebel Oum El Khacheb deposit [32] and Ras-Dhara deposit [33], as well as M'dhilla [34] phosphate rock, has been investigated, and Jaballi et al. [35] analyzed the thermal behavior of phosphate rocks from the Ypresian phosphate deposit. Besides, Daik et al. [36] and Dabbebi et al. [37] looked into the calcination of phosphate washing waste from the Gafsa-Metloui deposit. The objective of this work was to examine the technical feasibility of a thermal beneficiation path for Sra Ouertane low-grade phosphate rock using calcination, quenching, and disliming.
Samples from layers A1, A2, and C of the Sra Ouertane phosphate rock deposit were used for the thermogravimetric analysis (TGA). Later, a detailed sample analysis was performed with samples from the layer A1. The samples were provided by the National Office of Mines (ONM) of Tunisia and homogenized following the French regulation for the preparation of soil samples (NF X31-101) [38]. Samples from layers A1, A2, and C of the Sra Ouertane phosphate rock deposit were used for the thermogravimetric analysis (TGA). Later, a detailed sample analysis was performed with samples from the layer A1. The samples were provided by the National Office of Mines (ONM) of Tunisia and homogenized following the French regulation for the preparation of soil samples (NF X31-101) [38]. The received samples were washed with water, dried at 110 • C overnight, and sieved to give a size fraction less than 250 µm using ASTM (American Society for Testing and Materials) sieves.
Elemental analysis of the samples from layer A1 was conducted using inductively-coupled plasma mass spectrometry (ICP-MS, Perkin Elmer, Woodbridge, ON, Canada) to determine the uranium, thorium, and REE content and inductively-coupled plasma atomic emission spectroscopy (ICP-AES, HORIBA Jobin Yvon, France) for all other constituents. All chemical analyses were conducted with experimental errors below 5%. The particle size distribution was determined using laser diffraction techniques on a Malvern Master Sizer S (Spectris plc, Egham, UK) in the wet mode. X-ray powder diffraction (XRD) analysis was performed using a "Philips MPD1880-PW1710" diffractometer (Philipps, Eindhoven, The Netherlands) that uses CuKα radiation (λ = 0.15418 nm) in the 2-80 • interval with a step size of 0.02 • and counting time of 20 s/step at room temperature. The identification of the phases was determined using the ICDD-PDF2004 standard database [39].
Of particular relevance for this study was the required calcination temperature and residence time of the phosphate rock that should be processed so that the suitability of solar-driven systems can be determined. Depending on the given phosphate rock, calcination temperatures can vary from as high as 900 • C to as low as 500 • C [40,41]. In this first attempt, the thermal analysis of the samples from layer A1 (9.66 mg sample weight), layer A2 (16.75 mg sample weight), and layer C (12.35 mg sample weight) (particle distribution: 1 mm, 500 µm and 250 µm) was conducted. The characteristic TGA curves for layers A1, A2, and C of the Sra Ouertane phosphate rock are shown in Figure 3. Experiments were conducted at a temperature of up to 800 • C.
Minerals 2020, 10 4 of 13 The received samples were washed with water, dried at 110 °C overnight, and sieved to give a size fraction less than 250 μm using ASTM (American Society for Testing and Materials) sieves. Elemental analysis of the samples from layer A1 was conducted using inductively-coupled plasma mass spectrometry (ICP-MS, Perkin Elmer, Woodbridge, ON Canada) to determine the uranium, thorium, and REE content and inductively-coupled plasma atomic emission spectroscopy (ICP-AES, HORIBA Jobin Yvon, France) for all other constituents. All chemical analyses were conducted with experimental errors below 5%. The particle size distribution was determined using laser diffraction techniques on a Malvern Master Sizer S (Spectris plc, Egham, UK) in the wet mode. X-ray powder diffraction (XRD) analysis was performed using a "Philips MPD1880-PW1710" diffractometer (Philipps, Eindhoven, NL) that uses CuKα radiation (λ = 0.15418 nm) in the 2-80° interval with a step size of 0.02° and counting time of 20 s/step at room temperature. The identification of the phases was determined using the ICDD-PDF2004 standard database [39].
Of particular relevance for this study was the required calcination temperature and residence time of the phosphate rock that should be processed so that the suitability of solar-driven systems can be determined. Depending on the given phosphate rock, calcination temperatures can vary from as high as 900 °C to as low as 500 °C [40,41]. In this first attempt, the thermal analysis of the samples from layer A1 (9.66 mg sample weight), layer A2 (16.75 mg sample weight), and layer C (12.35 mg sample weight) (particle distribution: 1 mm, 500 μm, and 250 μm) was conducted. The characteristic TGA curves for layers A1, A2, and C of the Sra Ouertane phosphate rock are shown in Figure 3. Experiments were conducted at a temperature of up to 800 °C. Three peaks, typical of the calcination of phosphate rock, could be identified. The first mass loss at approximately 80 °C corresponded to the removal of adsorbed water. A second weak peak could be identified at approximately 550 °C. Elgharbi et al. [33] attributed this peak to the simultaneous elimination of chemical water in the rock structure and oxidation of organic matter. As most phosphate rocks contain organic matter rich in sulfur, sulfur gas was released. The most pronounced peak was found at 650-750 °C, where carbonate dissociated, and CO2 was released. Based on the TGA results, the calcination temperature was set to 720 °C. The weight loss at 720 °C was 11.88% (layer A1), 9.72% (layer A2), and 7.90% (layer C), respectively. Best practice experience with conventional kilns in Tunisia recommends a calcination time of 3 h. Thus, calcination experiments were performed at 720 °C for 3 h. It is worth noting that the thermal dissociation of carbonates is an endothermic reaction with a significant energy requirement: CaCO + Heat → CaO + CO ΔH = 965 kcal/kg CO2 or 42.9 kcal/mol CO2 The calcine was further quenched in 5% ammonium nitrate solution with 25% solid content. The calcine was kept in the ammonium nitrate solution for 2 h. In a subsequent disliming process, particles of less than 60 μm were removed using a hydro-cyclone. The preliminary flow sheet of the alternative beneficiation process for Sra Ouertane phosphate rock is provided in Figure 4. Three peaks, typical of the calcination of phosphate rock, could be identified. The first mass loss at approximately 80 • C corresponded to the removal of adsorbed water. A second weak peak could be identified at approximately 550 • C. Elgharbi et al. [33] attributed this peak to the simultaneous elimination of chemical water in the rock structure and oxidation of organic matter. As most phosphate rocks contain organic matter rich in sulfur, sulfur gas was released. The most pronounced peak was found at 650-750 • C, where carbonate dissociated, and CO 2 was released. Based on the TGA results, the calcination temperature was set to 720 • C. The weight loss at 720 • C was 11.88% (layer A1), 9.72% (layer A2), and 7.90% (layer C), respectively. Best practice experience with conventional kilns in Tunisia recommends a calcination time of 3 h. Thus, calcination experiments were performed at 720 • C for 3 h. It is worth noting that the thermal dissociation of carbonates is an endothermic reaction with a significant energy requirement: CaCO 3 + Heat → CaO + CO 2 ∆H = 965 kcal/kg CO 2 or 42.9 kcal/mol CO 2 (1) The calcine was further quenched in 5% ammonium nitrate solution with 25% solid content. The calcine was kept in the ammonium nitrate solution for 2 h. In a subsequent disliming process, particles of less than 60 µm were removed using a hydro-cyclone. The preliminary flow sheet of the alternative beneficiation process for Sra Ouertane phosphate rock is provided in Figure 4.

Results and Discussion
The elemental components relevant for further fertilizer processing of samples from layer A1 are provided in Table 2. The P2O5 content of the untreated phosphate rock was successfully increased from 20.01 wt% to 24.24 wt% after calcination. Further treatment consisting of quenching and disliming increased the P2O5 content to 27.24 wt%. Merchant grade phosphate rock should show P2O5 concentrations of at least 30 wt%. Besides, it is important to mention that the atomic ratio CaO/P2O5 = 1.94 of the untreated phosphate rock was still higher than the stoichiometric value of francolite with very low carbonate substitution (CaO/P2O5 = 1.65). Besides, the metal element ratio (MER) of 0.18 = (MgO + Fe2O3 + Al2O3)/P2O5 was just slightly below the maximum acceptable value of 0.2.
The calcined and treated phosphate rock, on the other hand, could be associated with the fluorapatite phase. The CaO/P2O5 = 1.68 was now very close to that of francolite. Besides, the MER of 0.13 was well below the acceptable value of 0.2.
A loss of 39 wt% Al2O3 and 30 wt% MgO from untreated phosphate rock to calcined and treated phosphate rock can be observed in Table 2. This loss could be associated with clays that were in a fraction of fewer than 60 microns. It is known that Mg is correlated with CO3 2− apatite, and it could thus be estimated that a portion of MgO was associated with the departure of CO3 2− during calcination. SO3 increased by 18% in the calcined and treated sample (Table 2). Francolite, the phosphoric mineral of almost all sedimentary phosphorites, has a variable chemical composition that can be represented by (Ca, Mg, Sr, Na)10 (PO4, SO4, CO3)6 F2-3. We hypothesized that a part of the CO3 2− of francolite was substituted by SO4 2− during calcination in addition to the conventional substitution between PO4 3− and CO3 2− . Relevant trace element concentrations are provided in Table 3. During the beneficiation process, the cadmium content was significantly reduced from 30 mg/kg to 14 mg/kg. Many countries have legal limits for the cadmium content in fertilizers [42,43] so that reducing the cadmium content early on in

Results and Discussion
The elemental components relevant for further fertilizer processing of samples from layer A1 are provided in Table 2 The calcined and treated phosphate rock, on the other hand, could be associated with the fluorapatite phase. The CaO/P 2 O 5 = 1.68 was now very close to that of francolite. Besides, the MER of 0.13 was well below the acceptable value of 0.2.
A loss of 39 wt% Al 2 O 3 and 30 wt% MgO from untreated phosphate rock to calcined and treated phosphate rock can be observed in Table 2. This loss could be associated with clays that were in a fraction of fewer than 60 microns. It is known that Mg is correlated with CO 3 2− apatite, and it could thus be estimated that a portion of MgO was associated with the departure of CO 3 2− during calcination. SO 3 increased by 18% in the calcined and treated sample ( Relevant trace element concentrations are provided in Table 3. During the beneficiation process, the cadmium content was significantly reduced from 30 mg/kg to 14 mg/kg. Many countries have legal limits for the cadmium content in fertilizers [42,43] so that reducing the cadmium content early on in the process is a positive side effect of heat treatment of phosphate rock and can be pursued deliberately by controlling the treatment temperature and the oxygen content within the reactor [10]. At temperatures >750 • C, cadmium can be transferred to the gaseous phase and removed through the air pollution control system. Depending on the process parameters and the targeted cadmium removal rate, up to 95% cadmium can be removed from most sedimentary phosphate rock types. Electrostatic precipitation, wet scrubbing, and/or baghouse filters are usually installed for gas cleaning. The uranium and thorium contents were increased since volatile constituents in the phosphate rock were driven off. The uranium content at Sra Ouertane reported in the literature (see Table 1) could reach higher concentrations than the uranium concentration that was ultimately measured in the samples here. The uranium concentration measured here would most likely be too low to enable commercially viable uranium recovery [44][45][46][47].
Relevant REE concentrations of the Sra Ouertane low-grade phosphate rock are provided in Table 4. The Sra Ouertane phosphate rock deposit showed relatively high REE concentrations by Tunisian [48] and international [9,49] standards, and recovering REEs might be attractive when developing the ore [8,50,51]. During the beneficiation process, all REEs were concentrated as volatile constituents were driven off. The particle size distribution was another important parameter for phosphate rock calcination. The particle size of the Sra Ouertane (layer A1) phosphate rock is provided in Figure 5 after sieving with 250 µm ASTM sieves. The particle size distribution of the untreated (Figure 5), calcined (Figure 6), as well as the calcined and treated (Figure 7) phosphate rock, was provided. Calcination slightly increased particle diameters. After calcination, less than 25 vol% of the phosphate rock particles had an equivalent particle diameter below 10 µm. The characteristic peak of particles at 100 µm was present in all stages. It is important to emphasize that the lab-scale experiments conducted here might result in very different particle size distributions than the ones obtained from industrial (rotary kiln) calcination that might, for instance, impose larger friction on the material during processing. The effect of disliming or removal of particles with an equivalent diameter of 60 µm in a hydro-cyclone could best be observed by the difference in particle distribution after calcination and after disliming.
The disliming step conducted on the lab-scale here successfully removed the largest share of small particles that were unwanted in further wet acid processing.      XRD analysis was conducted to better understand the effect of the concentration procedure on the phosphate rock. The diffractogram of the XRD analysis was characterized by a number of typical peaks found in other natural sedimentary phosphate rocks (see for instance [32,33,53]) and revealed the presence of the following phases: Fluorapatite Ca10(PO4)6F2), quartz (SiO2), and carbonates, which are mostly present in the form of calcite (CaCO3). Figure 8 shows the XRD pattern of the untreated Sra Ouertane phosphate rock. Calcination reduced the CO2 content of the Sra Ouertane ore significantly. Figure 9 shows the diffractogram of the XRD analysis of the Sra Ouertane phosphate rock after calcination and without the characteristic calcite (CaCO3) peak that can be observed in Figure 8. Besides, the CaO peaks resulting from carbonate decomposition could be well-identified in the calcined phosphate rock (Figure 9). XRD analysis was conducted to better understand the effect of the concentration procedure on the phosphate rock. The diffractogram of the XRD analysis was characterized by a number of typical peaks found in other natural sedimentary phosphate rocks (see for instance [32,33,53]) and revealed the presence of the following phases: Fluorapatite (Ca 10 (PO 4 ) 6 F 2 ), quartz (SiO 2 ), and carbonates, which are mostly present in the form of calcite (CaCO 3 ). Figure 8 shows the XRD pattern of the untreated Sra Ouertane phosphate rock. XRD analysis was conducted to better understand the effect of the concentration procedure on the phosphate rock. The diffractogram of the XRD analysis was characterized by a number of typical peaks found in other natural sedimentary phosphate rocks (see for instance [32,33,53]) and revealed the presence of the following phases: Fluorapatite Ca10(PO4)6F2), quartz (SiO2), and carbonates, which are mostly present in the form of calcite (CaCO3). Figure 8 shows the XRD pattern of the untreated Sra Ouertane phosphate rock. Calcination reduced the CO2 content of the Sra Ouertane ore significantly. Figure 9 shows the diffractogram of the XRD analysis of the Sra Ouertane phosphate rock after calcination and without the characteristic calcite (CaCO3) peak that can be observed in Figure 8. Besides, the CaO peaks resulting from carbonate decomposition could be well-identified in the calcined phosphate rock (Figure 9). Calcination reduced the CO 2 content of the Sra Ouertane ore significantly. Figure 9 shows the diffractogram of the XRD analysis of the Sra Ouertane phosphate rock after calcination and without the characteristic calcite (CaCO 3 ) peak that can be observed in Figure 8. Besides, the CaO peaks resulting from carbonate decomposition could be well-identified in the calcined phosphate rock (Figure 9). During disliming, smaller particles <60 μm were removed using a hydro cyclone. The XRD pattern of the calcined and treated Sra Ouertane phosphate rock is provided in Figure 10. The absence of peaks related to CaCO3 and CaO was noticeable. The only remaining mineral species were fluorapatite, quartz, and silicates. All three XRD patterns are depicted together in Figure 11. Shown is the diffractogram of the untreated phosphate rock (SRT-DP), the calcined phosphate rock (SRT-CAL), as well as the calcined and treated (SRT-CALT) Sra Ouertane phosphate rock (bottom to top). The comparison of the different XRD patterns showed a significant reduction of calcite (CaCO3) again and thus proved that the process, on a laboratory scale, significantly increased the P2O5 content. During disliming, smaller particles <60 µm were removed using a hydro cyclone. The XRD pattern of the calcined and treated Sra Ouertane phosphate rock is provided in Figure 10. The absence of peaks related to CaCO 3 and CaO was noticeable. The only remaining mineral species were fluorapatite, quartz, and silicates. During disliming, smaller particles <60 μm were removed using a hydro cyclone. The XRD pattern of the calcined and treated Sra Ouertane phosphate rock is provided in Figure 10. The absence of peaks related to CaCO3 and CaO was noticeable. The only remaining mineral species were fluorapatite, quartz, and silicates. All three XRD patterns are depicted together in Figure 11. Shown is the diffractogram of the untreated phosphate rock (SRT-DP), the calcined phosphate rock (SRT-CAL), as well as the calcined and treated (SRT-CALT) Sra Ouertane phosphate rock (bottom to top). The comparison of the different XRD patterns showed a significant reduction of calcite (CaCO3) again and thus proved that the process, on a laboratory scale, significantly increased the P2O5 content. All three XRD patterns are depicted together in Figure 11. Shown is the diffractogram of the untreated phosphate rock (SRT-DP), the calcined phosphate rock (SRT-CAL), as well as the calcined and treated (SRT-CALT) Sra Ouertane phosphate rock (bottom to top). The comparison of the different XRD patterns showed a significant reduction of calcite (CaCO 3 ) again and thus proved that the process, on a laboratory scale, significantly increased the P 2 O 5 content.

Conclusions
In total, the P2O5 content could be increased from some 20.01 wt% (untreated ore) to 27.24 wt% (calcined and treated ore). To reach merchant grade P2O5 concentrations of at least 30 wt%, further processing steps would be required. If, for instance, the relatively high silica content of 9.81 wt% could be reduced to some 2.5 wt%, phosphate concentrate with 30.2 wt% P2O5 would result as a final product. It is important to emphasize that even though additional processing steps for further ore concentration are required, the first steps described here are valuable and may help promote the use of Sra Ouertane low-grade phosphate rock ore in a sustainable manner.

Conclusions
In total, the P 2 O 5 content could be increased from some 20.01 wt% (untreated ore) to 27.24 wt% (calcined and treated ore). To reach merchant grade P 2 O 5 concentrations of at least 30 wt%, further processing steps would be required. If, for instance, the relatively high silica content of 9.81 wt% could be reduced to some 2.5 wt%, phosphate concentrate with 30.2 wt% P 2 O 5 would result as a final product. It is important to emphasize that even though additional processing steps for further ore concentration are required, the first steps described here are valuable and may help promote the use of Sra Ouertane low-grade phosphate rock ore in a sustainable manner.