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Article

Selection of an Appropriate Depressant in Flotation Separation of Molybdenum Oxide from Fluorapatite

School of Resource Environment and Safety Engineering, University of South China, Hengyang 421001, China
*
Author to whom correspondence should be addressed.
Minerals 2021, 11(10), 1110; https://doi.org/10.3390/min11101110
Submission received: 28 August 2021 / Revised: 24 September 2021 / Accepted: 5 October 2021 / Published: 10 October 2021
(This article belongs to the Special Issue Flotation Chemistry, Volume II)

Abstract

:
The depressive efficiency of sodium silicate, sodium hexametaphosphate, and tartaric acid on the flotation separation of molybdenum oxide from fluorapatite were examined using cetylpyridinium chloride (CPC) as the collector. The corresponding depression mechanisms of all three depressants were studied with the use of laboratory measurements. Individual mineral flotation tests and adsorption studies showed that all these depressants have a higher depression effect on fluorapatite than molybdenum oxide. Sodium hexametaphosphate has the strongest depression effect on fluorapatite and can reduce the flotation recovery as low as less than 20%. Infrared spectroscopy and zeta potential tests proved the rationality of the flotation results, indicating that when CPC was used as a collector, the effect of sodium hexametaphosphate on the surface of molybdenum oxide was smaller than that on fluorapatite. The adsorption of hexametaphosphate on the surface of fluorapatite was determined to be physical adsorption.

1. Introduction

The nickel-molybdenum ore resources were found mainly in specific regions of China, such as Guizhou, Hunan, Zhejiang, and the Eastern Yunnan Province, usually associated with other metals, such as, Se, Re, Au, Ag, Pt, Pd, etc.) [1,2,3,4]. The molybdenum minerals in the Ni-Mo ore are mainly jordisite, but the mine also contains various other materials composed of molybdenum and sulfur in different ratios [5,6,7]. The molybdenum mineral distribution pattern varies throughout the region, with certain areas showing grainy, reticular, vein-like, nodular, or zonal distributions, or even distributions in conjunction with pyrite [8,9]. The nickel minerals observed in this area are mainly nickel sulfide and gersdorffite. The molybdenum minerals in the Ni-Mo ore are mostly amorphous in structure [10]. Elements with similar chemical properties (such as molybdenum, tungsten, nickel, vanadium, and iron) chemically combine with sulfur and carbon [11,12]. No uniform morphology was observed [13]. As a result, it is difficult to separate valuable metal elements from one another [14]. Nickel and molybdenum minerals are flakes or irregular shapes. The target minerals are closely combined with gangue minerals, the diameter of which are only ten micrometers. The hardness of the nickel and molybdenum minerals varies greatly. Most of the useful minerals are hard ground minerals. A large amount of fluorapatite and mica contained in the ore crumbles easily, only a small selection of flotation reagents is available for the flotation of minerals with these characteristics. Compositional analysis of the Ni-Mo ore indicates that it contains certain amounts of molybdenum oxide with minimal floatability, which adversely affects the recovery rate of the elemental molybdenum. A suitable depressant was selected for the depression of gangue minerals and is important for increasing the recovery rate of elemental molybdenum.
Fluorapatite is one of the main gangue minerals in Ni-Mo ore. Inorganic acids (phosphoric acid, sulfuric acid) are usually used as the pulp pH regulators to inhibit apatite flotation in a weak acid environment. Dong [15] used iron ions to improve the depressive efficiency of tartaric acid on the flotation separation of scheelite from calcite. Tartaric acid and Fe3+ were co-adsorbed on the surface of calcite by reacting with the calcium ion in calcite. This phenomenon indicates that tartaric acid was a very effective calcium mineral depressant. Abdel-Khalek [16] reported that PO43− exhibited characteristic adsorption of Ca2+ on the surface of apatite in an acidic system, leading to a depression effect on apatite flotation. H3PO4 can be used as both a pulp pH adjustor and apatite inhibitor by preventing the upward flotation of apatite attached to bubbles [17]. This role is mainly attributed to a decrease in the Ca2+ concentration in the acidic solution, which promotes the adsorption or formation of CaHPO4 on the surface of apatite, thereby hindering contact between reagent ions and apatite. Rodrigo [18] found that sodium hexametaphosphate and sodium silicate dispersants increase copper and molybdenum recoveries, rendering mineral particles more negatively charged by removing magnesium and calcium hydroxy complexes from mineral particles. As a result, heterocoagulation between chalcopyrite/molybdenite and mica particles is reduced, leading to high recoveries.
Therefore, this work is focused on the flotation separation of molybdenum oxide and fluorapatite, by the addition of a more appropriate depressant for fluorapatite flotation. In this regard, the depression effects of different depressants such as sodium silicate, sodium hexametaphosphate, and tartaric acid were investigated systematically, aiming at obtaining the most suitable depressant for fluorapatite flotation.

2. Experimental

2.1. Samples and Reagents

Pure molybdenum oxide and fluorapatite samples were used in this study. The former was purchased from a chemical reagent factory in Shanghai, with a granularity of 0.63 mm, and the latter was purchased from the Mineral Specimens Company of Shuiyuanshanchang in Beijing.
Molybdenum oxide is an industrial reagent containing MoO3 of 99.6% purity and was used in this study following characterization. The samples were ground in a porcelain mill (rotation grinding) for 1–2 min and then sieved to collect the −0.074 mm–+0.038 mm fraction for the flotation tests. Samples of fluorapatite were handpicked, crushed with a jaw crusher into grains measuring approximately 3 mm, ground in a porcelain mill (rotating grinding) for 3–4 min, and sieved to select the −0.074 mm–+0.038 mm fraction for the flotation tests.
Cetylpyridinium chloride (CPC) of analytical quality was used as the collector for the flotation tests. HCl and NaOH solutions were used to adjust the pH value of the system. Analytical grade sodium silicate, sodium hexametaphosphate, and tartaric acid were used as the depressants. Deionized ultrapure water was used throughout the experiments.

2.2. Methods

2.2.1. Flotation Experiments

Individual mineral micro-flotation tests were performed in a 40 mL flotation machine (Weikeduo XFG II, ganzhou, China) at a constant impeller speed of 1860 rpm. For each test, parallel experiments were set, the experimental results were determined as the average of the two sets of experiments, and the difference between the experimental results of the two sets of experiments was not more than 2%. A 2 g mineral sample was placed into the flotation cell, 35 mL of distilled water was added and stirred for 1 min, and HCl or NaOH was added and stirred for 1 min to adjust for the desired value. Then, the depressant was added and stirred for 1 min. Finally, the collector was added, and the flotation was performed for 3 min. The floating and non-floating fractions were separately dewatered, dried, and weighed for the assessment.

2.2.2. Adsorption Studies

The effects of pH and the depressant on the adsorption characteristics of the collectors on the mineral surface were measured using a TU-1810 UV-visible spectrophotometer.
For each test, 2.0 g of sample ore was placed into a 40 mL flotation cell and stirred for 2 min. Next, a flotation reagent was added under the same mixing conditions used in the individual mineral flotation tests. A centrifuge (5417R, Eppendorf, Hamburg, Germany) was used to separate the pulp over 15 min. The resulting supernatant was used for testing.
Adsorption of the flotation reagents on the mineral surface could be calculated according to the following formula:
Γ = (C0V0 − CiV0)/1000G,
where:
Γ is adsorption of flotation reagents on the mineral surface, mol/g
C0 is the original concentration of flotation reagents in solution, mol/L
V0 is the volume of the solution, mL
Ci is the concentration of flotation reagents in the supernatant, mol/L
G is the weight of sample ore, g

2.2.3. Infrared Spectroscopic Analysis

The samples were prepared by the following procedure. The pure mineral was ground in an agate mortar. One-half of the sample ore was used for infrared spectroscopic analysis, and the second half was placed into a beaker with 35 mL of deionized water and flotation reagents and then stirred for 5 min before being filtered. The remaining solid was placed in a vacuum dryer to produce a mixture of the mineral and the flotation reagents. A NEXUS-670 Fourier transform infrared spectrometer (670FT-IR, NEXUS, Madison, USA) was used to test the three samples: (1) the mineral, (2) the reagent, and (3) a mixture of 1 and 2.

2.2.4. Determination of Zeta Potentials

The zeta potential analysis was performed using a Delsa-440SX analyzer (Delsa-440SX, Beckman Coulter, Brea, CA, USA). A suspension containing a mass fraction of 0.01% of molybdenum oxide mineral or fluorapatite mineral was dispersed in a beaker by ultrasonication and then stirred in a magnetic stirring apparatus for 5 min. On the other hand, 1.6 × 102 mol/L of sodium hexametaphosphate was added to the two suspensions and stirred for 2 min, respectively, to prepare the mixed samples of minerals and depressants. After the pH was measured, the suspensions were immediately transferred to a square sample vessel to record the zeta potential readings.

3. Results and Discussion

3.1. Floatability Tests of Minerals

The purities of the molybdenum oxide and fluorapatite used in this study were 99.60% and 99.00%, respectively. Using CPC as the collector, the effects of depressants on the flotation behaviors of molybdenum oxide and fluorapatite at different pH values were studied; the results are shown in Figure 1, Figure 2 and Figure 3.
The three depressants had little effect on the flotation recovery of the molybdenum oxide at pH 2–6, as indicated by the recovery rates of 73%~78%. However, the flotation recovery of fluorapatite was greatly decreased in the presence of the depressants. Figure 1a shows that the flotation recovery of fluorapatite decreased by approximately 10% compared to that without sodium silicate. Figure 1b,c shows that the flotation recovery of fluorapatite decreased after adding sodium hexametaphosphate or tartaric acid, and their recovery rate was only 10%~20% over the entire pH range.
In summary, the flotation results show that the sodium hexametaphosphate effectively suppressed the flotation of fluorapatite and thus could be used as a selective depressant in the flotation separation of molybdenum oxide and fluorapatite with CPC as the collector.

3.2. Solubility Equilibrium Analysis of Fluorapatite

Figure 1 shows that when the pH level was higher than 8, the flotation recovery of fluorapatite with CPC rose steadily, primarily due to the solubility equilibrium. The equilibrium reactions in the saturated aqueous solution of fluorapatite [17] are listed in Table 1.
The relationship between the individual concentrations of each dissolving group and the lattice ion concentrations can be determined based on the equilibrium formulas and the equilibrium constants. In the saturated fluorapatite solution, the isoelectric point, pI, can be determined by the negative logarithm of the corresponding lattice ions, I, when CaF+ and H2PO4 have the same concentration. The calculated pI values are as follows: pF = 4.5; pHPO4 = 5.8; and pCa = 4.2. All values are very similar to the test values (pF = 4.6, pHPO4 = 5.2, and pCa = 4.4); therefore, the ions in fluorapatite were determined to include Ca2+, F, CaF+, HPO42−, and H2PO4.

3.3. Adsorption Studies

Figure 2 shows the effects of inhibitors on the adsorption of CPC on the surface of molybdenum oxide at different pH values. It can be observed that the adsorption of CPC decreased gradually with an increasing pH. In the presence of each of the three depressants, CPC adsorption was lower than that without the depressants, but the difference was not more significant. The effects of the three depressants on the adsorption of CPC on the surface of molybdenum oxide followed the order tartaric acid > sodium hexametaphosphate > sodium silicate.
Figure 3 shows the effects of depressants on the adsorption of CPC on the surface of fluorapatite under different pH conditions. It can be observed that the adsorption of CPC increased gradually with increasing pH, regardless of the type of depressant used. When the pH was higher than 7, the amount of adsorption increased more rapidly, which may have been caused by the activation of fluorapatite at the higher pH values. Table 1 shows that the fluorapatite anion content increased under alkaline conditions, which enhanced the adsorption of CPC onto the mineral surface. The amount of adsorption was lower in the presence of depressants than in the absence of inhibitors over the entire pH range. The effects of the three depressants on the adsorption capacity of CPC on the fluorapatite surface were ranked as follows: sodium hexametaphosphate > tartaric acid > sodium silicate.

3.4. Infrared Spectroscopic Measurement

To investigate the adsorption mechanism of sodium hexametaphosphate on molybdenum oxide, the infrared spectra of molybdenum oxide before and after the interaction with sodium hexametaphosphate were analyzed and are shown in Figure 4.
The spectrum of molybdenum oxide (Spectrum (1)) shows characteristic bands at 988.9 cm−1, 879.6 cm−1, and 490 cm−1, which were attributed to the stretching vibrations of Mo–O1, Mo–O2, and Mo–O3, respectively [19,20].
After interacting with sodium hexametaphosphate, spectrum (2) was obtained, which exhibited no noticeable changes. As the flotation tests on individual minerals showed that sodium hexametaphosphate inhibited molybdenum oxide, which may be due to the physical adsorption of sodium hexametaphosphate on the surface of molybdenum oxide, Spectrum (3) shows the absorption bands at 2840 cm−1 and 2930 cm−1, which were the characteristic of –CH2– and –CH3, indicating that the adsorption of CPC occurred on the molybdenum oxide surface. However, the absorption bands become weaker in spectrum (4), indicating that sodium hexametaphosphate reduced the adsorption of CPC on the surface of molybdenum oxide; however, based on the flotation tests of molybdenum oxide, the depression was very weak.
To investigate the adsorption mechanism of sodium hexametaphosphate on fluorapatite, the infrared spectra of fluorapatite before and after the addition of sodium hexametaphosphate were analyzed and are shown in Figure 5.
The spectrum of fluorapatite (spectrum (1)) shows characteristic bands at 1060 cm−1, 964 cm−1, 600 cm−1, and 471 cm−1, which were attributed to the stretching vibration of PO43− [21].
After interacting with sodium hexametaphosphate, Spectrum (2) was obtained, which again exhibited no noticeable changes. Due to the fact that the flotation tests on individual minerals showed that sodium hexametaphosphate inhibited fluorapatite, its adsorption on the surface of fluorapatite was identified as physical absorption. Spectrum (3) shows absorption bands at 2840 cm−1 and 2930 cm−1, which were attributed to the stretching vibration modes of –CH2– and –CH3, indicating that the adsorption of CPC occurred on the fluorapatite surface. Spectrum (4) is nearly identical to spectrum (3). The flotation tests on fluorapatite showed that the interaction between CPC and fluorapatite was very weak; therefore, the depression of CPC adsorption on the surface of fluorapatite with the addition of sodium hexametaphosphate was not distinctly indicated from the infrared spectrograms.

3.5. Zeta Potential Measurements

To further illustrate the effect of sodium hexametaphosphate on the surface properties of molybdenum oxide and fluorapatite, the surface potentials before and after interaction with sodium hexametaphosphate were measured. Figure 6 shows the effect of sodium hexametaphosphate on the surface zeta potential of molybdenum oxide. After interacting with sodium hexametaphosphate, the surface zeta potential of molybdenum oxide was changed only slightly; therefore, the observed effect was insignificant. Figure 7 shows the effect of sodium hexametaphosphate on the surface zeta potential of fluorapatite, whose isoelectric point is approximately 4.1. The surface zeta potential of fluorapatite was decreased after adding sodium hexametaphosphate, and no point of zero charges was observed in this case at the tested pH values. When the pH was 4, the surface zeta potential of fluorapatite decreased from +0.6 to approximately −12, and the potential became more negative. Moreover, by comparing the surface zeta potentials of fluorapatite and molybdenum oxide after the interaction with sodium hexametaphosphate, it can visibly be seen that when the pH was above five, the repulsive forces between molybdenum oxide and fluorapatite were increased in magnitude, which could provide the effective separation between these minerals.

4. Conclusions

In this research work, the depression effects of different depressants such as sodium silicate, sodium hexametaphosphate, and tartaric acid were investigated, aiming at obtaining the more appropriate depressant in flotation separation of molybdenum oxide from fluorapatite. Major conclusions are summarized as follows:
(1) Sodium hexametaphosphate, tartaric acid, and sodium silicate all have a much greater depression effect on fluorapatite than molybdenum oxide, the strongest depression effect on fluorapatite compared with other depressants, reducing the flotation recovery of fluorapatite as low as less than 20%.
(2) Sodium hexametaphosphate significantly reduced the adsorption of CPC onto the fluorapatite surface. These results were in good agreement with the flotation tests. The addition of sodium hexametaphosphate reduced the intensities of the characteristic adsorption peaks of CPC on the fluorapatite surface. On the other hand, sodium hexametaphosphate showed little effect on the adsorption of CPC onto the surface of molybdenum oxide. However, the sodium hexametaphosphate underwent physical absorption to varying degrees on the surfaces of molybdenum oxide and fluorapatite.
(3) The zeta potential results showed that the sodium hexametaphosphate greatly altered the surface characteristics of fluorapatite by decreasing its surface charges. These results further indicated that the addition of sodium hexametaphosphate increased the magnitudes of the repulsive forces between molybdenum oxide and fluorapatite, which could provide an effective separation between these minerals.
Sodium hexametaphosphate was a potential depressant in the flotation separation of molybdenum oxide from fluorapatite with CPC as the collector.

Author Contributions

Conceptualization, J.L. and Z.L.; methodology, J.L., B.P. and F.B.; software, Z.L.; validation, J.L., B.P. and F.B.; formal analysis, L.Z.; investigation, L.Z.; resources, J.L.; data curation, B.P.; writing—original draft preparation, J.L.; writing—review and editing, Z.L.; visualization, J.L.; supervision, Z.L.; project administration, J.L.; funding acquisition, J.L. All authors have read and agreed to the published version of the manuscript.

Funding

This work was funded by the Natural Science Foundation of Hunan Province, No.2018JJ3446 and the Scientific research project of Hunan Provincial Department of Education project, No.17C1374.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Effect of the three depressants on the floatability of molybdenum oxide and fluorapatite at different pH values: (a) sodium silicate; (b) sodium hexametaphosphate; (c) tartaric acid.
Figure 1. Effect of the three depressants on the floatability of molybdenum oxide and fluorapatite at different pH values: (a) sodium silicate; (b) sodium hexametaphosphate; (c) tartaric acid.
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Figure 2. Effect of three inhibitors on the adsorption of CPC on the surface of molybdenum oxide at different pH values.
Figure 2. Effect of three inhibitors on the adsorption of CPC on the surface of molybdenum oxide at different pH values.
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Figure 3. Effect of inhibitors on the adsorption of CPC on the surface of fluorapatite at different pH values.
Figure 3. Effect of inhibitors on the adsorption of CPC on the surface of fluorapatite at different pH values.
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Figure 4. Infrared spectral of molybdenum oxide after its interaction with CPC and sodium hexametaphosphate.
Figure 4. Infrared spectral of molybdenum oxide after its interaction with CPC and sodium hexametaphosphate.
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Figure 5. Infrared spectra of fluorapatite before and after its interaction with CPC and sodium hexametaphosphate.
Figure 5. Infrared spectra of fluorapatite before and after its interaction with CPC and sodium hexametaphosphate.
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Figure 6. Relationship between pH and zeta potential values on the surface of molybdenum oxide before and after the addition of sodium hexametaphosphate.
Figure 6. Relationship between pH and zeta potential values on the surface of molybdenum oxide before and after the addition of sodium hexametaphosphate.
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Figure 7. Relationship between pH and zeta potential values on the surface of fluorapatite before and after the addition of sodium hexametaphosphate.
Figure 7. Relationship between pH and zeta potential values on the surface of fluorapatite before and after the addition of sodium hexametaphosphate.
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Table 1. Equilibrium reactions of fluorapatite in a saturated aqueous solution (25 °C).
Table 1. Equilibrium reactions of fluorapatite in a saturated aqueous solution (25 °C).
Chemical EquationEquilibrium Constant (log k)
Ca10(PO4)6(F)2 + 6H+ = 10 Ca2+ + 6PO43− + 2F11.8
Ca2+ + H2PO4 = CaH2PO4+1.1
Ca2+ + HPO42− = CaHPO4(aq)2.7
CaHPO4(S) = Ca2+ + HPO42−−7.0
Ca2+ + 2OH = Ca(OH)2(aq)2.77
Ca2+ + OH = CaOH+1.4
Ca2+ + PO43− = CaPO46.46
Ca2+ + F = CaF+1.9
CaF2(S) = Ca2+ + 2F−10.4
H2PO4 + H+ = H3PO42.15
H2PO4 = H+ + HPO42−−7.20
HPO42− = H+ + PO43−−12.35
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Liu, J.; Peng, B.; Zhao, L.; Bai, F.; Lei, Z. Selection of an Appropriate Depressant in Flotation Separation of Molybdenum Oxide from Fluorapatite. Minerals 2021, 11, 1110. https://doi.org/10.3390/min11101110

AMA Style

Liu J, Peng B, Zhao L, Bai F, Lei Z. Selection of an Appropriate Depressant in Flotation Separation of Molybdenum Oxide from Fluorapatite. Minerals. 2021; 11(10):1110. https://doi.org/10.3390/min11101110

Chicago/Turabian Style

Liu, Jiandong, Binbin Peng, Liping Zhao, Fengwei Bai, and Zhiwu Lei. 2021. "Selection of an Appropriate Depressant in Flotation Separation of Molybdenum Oxide from Fluorapatite" Minerals 11, no. 10: 1110. https://doi.org/10.3390/min11101110

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