Scrubbing and Inhibiting Coagulation Effect on the Purification of Natural Powder Quartz

Abstract

The low removal efficiency of fine clay impurities in natural powder quartz (NPQ) is the main problem that affects the practical utilization of this natural resource. In this work, detailed characterizations of NPQ and clay impurities in NPQ were analyzed by SEM-EDS, mineral liberation analysis (MLA) and impurities distribution analysis. A combined physical purification process, including sieving, scrubbing and centrifugation, was applied to remove the clay impurities. It was observed that the fine clay impurities adhering on quartz surface were effectively liberated by scrubbing, and the content of Fe₂O₃ and Al₂O₃ in the concentrate decreased from 0.48% and 0.40% to less than 0.01% and 0.02% at pH 9.3 or when the dosage of sodium hexametaphosphate (SHMP) was 1 × 10³ g/t. The coagulation interaction between quartz and impurities including hematite and orthoclase were analyzed based on the classical Deyaguin-Landau-Verwey-Overbeek (DLVO) theory. The results indicated that the main coagulation affecting the separation efficiency was the heterocoagulation between quartz and impurities and homocoagulation among hematite particles. Furthermore, adding regulators such as sodium hydroxide (NaOH) or SHMP could significantly decrease the zeta potential of minerals and thus increase the total interaction energy (V_T), which could effectively improve the dispersion of these fine impurity particles, and consequently improve the removal efficiency of impurities. Reverse increase of the zeta potential of minerals in strongly alkaline solutions or excessive SHMP were detected, which was likely the main factor limiting the further improvement of the purification efficiency.

1. Introduction

Quartz is a highly critical and strategic material for advanced and emerging industrial technologies, which can be used extensively in advanced manufacturing of materials such as optical fibers, semi-conduct materials, highly pure glass in aerospace, etc. [1,2]. Considering the constant demand for better living standards of the increasing population, more and more quartz resources will be required in the future. Among different natural quartz resources, crystal is still the first choice for high purity quartz preparation. However, high purity crystal resources are rare in the world. Hence, researchers have tried to purify other natural quartz resources such as quartzite, quartz sand and white sand as substitutes [3,4]. In order to remove impurities, various processing methods were used. Physical methods such as magnetic separation, reverse flotation [5,6], and chemical treatment such as acidic leaching by hydrogen fluoride (HF) combined with other different fractions strong industrial acids such as HCl, HNO₃ or H₂SO₄ [2,7] were usually employed. In addition, some other new purification methods were also proposed, including bioleaching, supersonic-enhanced leaching and microwave explosion [8,9]. Because of the scarcity of high-quality resources and the high processing costs, developing feasible and economical processing technology is especially important.

NPQ is a natural quartzose material which is widely distributed in China; it is formed by the the weathering of quartzite [10]. The characteristics of this resource include about 97–99% SiO₂, integrity granular shape and extremely fine grain (D₉₀ is approximately 67 μm and D₅₀ is around 39 μm) compared with other quartz resource. However, this resource is contaminated by different contents of impurities such as Fe₂O₃ and Al₂O₃ coming from fine clay minerals, which might significantly limit its application. Additionally, these fine clay impurities generated in the weathering course or exploitation are difficult to remove.

The traditional purification methods for NPQ include elutriation, flushing by quantitative water and spontaneous precipitation in a settling basin [11]. However, these methods have low separating efficiencies and high operation costs in practical applications. With the improvement in separation technologies, some methods such as magnetic separation and reverse flotation were applied for the purification of NPQ [12,13]. However, all these reported methods were inefficient for the removal of fine clay minerals in NPQ. The main reason for the low removal efficiency is that the impurity contents were so scarce that they could not be definitively distinguished by traditional methods, which limited advances in purification methods. On the other hand, chemical treatment with excellent desliming effect has disadvantages, such as high operation costs and acid wastewater discharge, causing environmental problems, etc. Hence, the efficient utilization of NPQ resources on a large scale was delayed. Therefore, the removal of fine clay impurities from NPQ by an effective, environmentally friendly and affordable process is particularly critical for the large scale industrial utilization of NPQ.

Attrition scrubbing has been used as a physical decontamination treatment in many fields of mineral purification, especially in the removal of clay impurities from target mineral surfaces [14,15,16]. Centrifugal separation is one of the cost-effective solutions for the treatment of waste water, flotation slurries and chemical industry [17,18]. Hence, it is expected that the scrubbing-centrifugation technology could be an ideal method for the removal of clay impurities in NPQ.

In this paper, the feasibility of a combination technique of sieving, scrubbing and centrifugal separation on the removal of clay impurities in NPQ was investigated. In order to purify NPQ more efficiently, both NaOH and SHMP were added as regulators in the purification process. Furthermore, the possible mechanisms were also proposed by studying the heterocoagulation and homocoagulation between quartz and impurity particles according to the DLVO theory.

2. Materials and Methods

2.1. Materials

The raw ore of NPQ used in this study was obtained from JiangXi province, China. The main chemical composition was measured by ICP-AES (inductively-coupled plasma atomic emission spectrometry) and the result is presented in

Table 1. Chemical analysis of the dry NPQ (wt %).

Compositions	SiO2	Al2O3	Fe2O3	TiO2	CaO	MgO	K2O	Na2O	L.O.I. a
Content (wt %)	98.88	0.48	0.19	0.03	0.06	0.04	0.04	0.05	0.24

^a Loss on ignition.

. As shown in Table 1, NPQ is mainly composed of SiO₂ (98.88%), and the main impurities are Al₂O₃ (0.48%) and Fe₂O₃ (0.19%); there are some other impurities like TiO₂, CaO, and MgO, etc. X-ray diffraction (XRD) was used to examine the purity of raw ore; the XRD pattern are presented in Figure 1. Figure 1 shows that the main peaks match well with the standard quartz peaks. However, no clear impurity peaks were observed, since the impurity content is too low, i.e., it exceeded the detection limit of XRD analysis.

All the reagents used in this study were chemically pure and purchased from Beijing Chemical Reagent Company (Beijing, China). Distilled water was used throughout the experiments.

2.2. Purification Methods

Highly concentrated (about 75%) pulp was prepared by adding 175 g water to 500 g raw ore, and then scrubbing tests were performed in vessels for about 25 min with the stirring rate of 1500 rpm. An appropriate amount of regulators (NaOH or SHMP) was pre-dissolved in 5 mL of water and then added to the scrubbing suspension at room temperature. After scrubbing, the pulp was stirred and dispersed for 5 min with extra 1750 mL water before being sieved using a 200 mesh standard screen (75 μm); the oversized product was tailing and labelled as “T1”. The under-sized product was centrifuged at 315 rpm (RCF (relative centrifugal force) =10) for 1 min. The sediment of centrifugation was concentrated and labelled “Con”, and the suspension of centrifugation was tailing and labelled “T2”. All products were dried and weighed for analysis.

2.3. Equipment

The chemical compositions of the raw NPQ and purification products were measured using an ICP-OES (Agilent730, Agilent Technologies, Santa Clara, CA, USA). The crystalline phase identification of samples were undertaken by X-ray diffraction analysis D8 ADVANCE (Bruker, Billerica, MA, USA), equipped with a Cu-Kα radiation at a goniometer rate of 2θ = 4°/min and the crystalline phase identification of trace impurities were detected by MLA. Microstructures were investigated by scanning electron microscopy (HT7700, Hitachi, Tokyo, Japan) at 10.0 KV, equipped with energy-dispersive microanalysis facilities (EDS). Zeta (ζ) potentials were measured using a Brookhaven zeta potential analyzer and three runs of measurement were conducted. The Mineral Liberation Analyser (MLA250, FEI, Hillsboro, OR, USA) was provided by Beijing General Research Institute of Mining & Metallurgy (BGRIMM, Beijing, China).

3. Results and Discussion

3.1. Impurity Analysis of NPQ

In order to analyze the distribution of impurities in different sizable fractions, NPQ were first sieved using a set of standard screens (100, 200 and 325 mesh), and then the part of −325 mesh was divided into sediment and suspension by centrifugation at 315 rpm for 1 min. The yields and contents of Fe₂O₃ and Al₂O₃ in different sizes of NPQ are summarized in

Table 2. Yields and contents of Fe₂O₃ and Al₂O₃ in different sizable of NPQ.

Particle Size/Mesh		Yield (%)	Content (%)
			Fe2O3	Al2O3
+100		1.96	0.301	0.862
−100~+200		4.51	0.132	0.157
−200~+325		26.14	0.040	0.031
−325	sediments	61.95	0.053	0.043
	suspensions	5.44	2.576	8.790

. As displayed in Table 2, the yields were 1.96%, 4.51% and 5.44% for +100 mesh, −100~+200 mesh and micro-fine (centrifugal suspension) samples, respectively. The contents of Fe₂O₃ and Al₂O₃ in coarse grains are within the range of 0.132–0.301%and 0.157–0.862%, and in micro-fine the contents of Fe₂O₃ and Al₂O₃ are 2.576% and 8.790%, respectively. On the other hand, the yields of −200~+325 mesh and the sediments of −325 mesh are 26.14% and 61.95% respectively with relatively lower content of impurities. It was concluded that the impurities of Fe₂O₃ and Al₂O₃ were mainly distributed in coarse grains (>200 mesh) and micro-fine grains.

SEM equipped with EDS analysis was used to directly observe the microstructural characteristics and confirm the elements compositions of clay particles existing in NPQ. As shown in Figure 2, the dispersion of quartz was very even and the particle sizes were approximately in the range of 20–55 μm. Meanwhile, a large number of small particles (1–3μm) were found adhering to the quartz surface. The EDS analysis showed that the main elements of particles on the quartz surface are Si, O, Al and Fe, indicating that the fine particles could be clay impurities.

Mineral liberation analysis (MLA) is a commercially available SEM-based image analysis system which has been widely applied in mineralogy and metallurgical processing [19,20]. Each mineral grain delineation inside the grain can be identified automatically with single X-ray analysis. The SEM-based image (BSE) signal in MLA has higher spatial resolution (0.1–0.2 μm) than X-ray of 2–5 μm. Hence, the mineralogy and the content of impurities in NPQ could not be determined by XRD because of the limitations of analytical accuracy, but could be determined by MLA. The representative results are displayed in Figure 3 and Figure 4, and the distribution of Fe₂O₃ and Al₂O₃ according to mineralogy semi-quantitatively is summarized in

Table 3. Distribution of Al₂O₃ and Fe₂O₃ at different minerals in NPQ detected by MLA (%).

Impurities	Hematite	Orthoclase	Anorthose	Mica	Total
Fe2O3	92.17	0	0	7.83	100
Al2O3	0	64.42	26.53	9.06	100

. It was revealed that the presence of Fe₂O₃ comes mainly from hematite, and Al₂O₃ comes from orthoclase and anorthose. In addition, impurities such as mica were present in the sample.

3.2. Effects of Scrubbing and Regulators on Impurities Removal

According to the character of impurities existing in the sample, a series of experiments were conducted as displayed in

Table 4. Experiments conditions and results.

No.	Regulator	Dosage /(g·t-1)	Product	Yield (%)	Impurity Content (%)
					Fe2O3	Al2O3
1		/	T1	6.47	0.182	0.365
	/		T2	5.44	2.551	7.76
			Con	88.09	0.048	0.04
2		/	T1	4.52	0.173	0.311
	/		T2	5.85	2.857	7.51
			Con	89.63	0.020	0.033
		500	T1	4.33	0.141	0.179
3	NaOH		T2	6.03	2.948	7.602
			Con	89.64	0.010	0.018
		500	T1	4.38	0.148	0.169
4	SHMP		T2	6.02	2.963	7.521
			Con	89.60	0.010	0.024

to explore the effect of scrubbing and regulators on impurity removal. Firstly, experiments with and without scrubbing were performed. Subsequently, different regulators were added to the pulp when scrubbing. Test No. 1 was stirred 25 min with equivalent water and separated under the same condition as the test No. 2. The yields and element contents of Fe₂O₃ and Al₂O₃ in different products are summarized in Table 4.

The results displayed that the content of Fe₂O₃ and Al₂O₃ in concentrate without scrubbing decreased from 0.048% and 0.040% to 0.020% and 0.033% after scrubbing, respectively. Adding NaOH or SHMP when scrubbing could further decrease the content of Fe₂O₃ in concentrate to around 100 μg/g (0.01%) and the content of Al₂O₃ to around 200 μg/g (0.018–0.024%). The yield of both T2 and concentrate with scrubbing increased from 5.44% and 88.09% to 5.85% and 89.63%, and the yield of T1 decreased from 6.47% to 4.52%. Compared with scrubbing without regulators, adding regulators has little effect on the yields of products.

The impurity distribution ratio (P) in different products under different conditions was calculated according Equation (1), which revealed the impurity change from a comprehensive view of content and yield, where Y_Pro and G_Pro represent the yield and the contents of Fe₂O₃ or Al₂O₃ in different products respectively, and C_raw represents the impurity content in raw ore.

$$P=\frac{Y_{Pro}\times G_{Pro}}{C_{raw}}\times 100\%$$

(1)

The results in Figure 5 suggest that P_Fe2O3 and P_Al2O3 of T1 and concentrate all decreased significantly after scrubbing, and thus, the P_Fe2O3 and P_Al2O3 of T2 both increased. It could be inferred that the physical impact and shearing actions occurring between contaminated particles and either the liquid phase or the walls and impellers stripped the clay impurities from quartz surface and crushed the coarse grains as micro-size fractions. The increase of P_Fe2O3 and P_Al2O3 of T2 indicated that more impurities were separated into T2 by centrifugation. The experimental results of test No. 3 and 4 showed that the concentrations of both P_Fe2O3 and P_Al2O3 further decreased, indicating that the separation efficiency of clay impurities from NPQ was improved by adding NaOH or SHMP.

Some representative SEM images shown in Figure 6 were applied to identify the effect of scrubbing and centrifugation on the clay impurity removal of NPQ. As displayed in Figure 6 c,d, it is obvious that the fine clay particles adhering on quartz surface disappeared, and the surface was clearer and smoother after scrubbing compared with the samples which had not undergone scrubbing (Figure 6 a,b). It could be concluded that the impurity minerals were effectively stripped from the surface of quartz through scrubbing. According to Figure 6 e,f, it was demonstrated that the fine particles were separated into the T2 by centrifugation, which is the key factor affecting the removal efficiency of the clay impurities.

3.3. Effects of pH and Dosage of SHMP on Impurities Removal

To reveal the influence of pH on the removal efficiency of clay impurities, the impurities content of Fe₂O₃ and Al₂O₃ in concentrate were illustrated as a function of pH in Figure 7. The pH of solution was adjusted through adjusting NaOH amount, and the practical pH values were measured before centrifugation. The results showed that when the pH increased from 7.1 to 9.3, both of the contents of Fe₂O₃ and Al₂O₃ decreased significantly, but the increase of pH from 9.3 to 11.7 only shows slight influence on impurities removal.

The influence of SHMP on impurities removal was studied for dosages of 100, 500, 1000, 3000 and 5000 g/t at pH = 7 and the results are given in Figure 8. As expected, the dosage of SHMP affects both of the content of Fe₂O₃ and Al₂O₃ in concentrate. The removal efficiency of impurities was improved with the dosage of SHMP increases from 100 to 1000 g/t, and an optimal effect can be obtained at 1000 g/t. However, with increasing the dosage of SHMP continuously, the content of both Fe₂O₃ and Al₂O₃ in the concentrate presented an increasing trend, which indicated that an excess of SHMP can inhibit the removal efficiency of impurities.

4. Purification Mechanism

It is obvious that scrubbing enhanced the liberation of minerals, and the separation efficiency was dominated by centrifugation. Since previous experiments revealed that adding NaOH or SHMP could improve the removal efficiency of clay impurities, the mechanism was analyzed based on the influence of NaOH or SHMP on the interaction between quartz and clay impurity particles including hematite and orthoclase. Classical DLVO theory was used to study the stability of slurry and mineral particles by many researchers [21,22]. Based on the DLVO theory, the interactions between particles in aqueous solution include the van der Waals attraction force and the electrostatic double layer repulsive force. The coagulation and dispersion behaviors of mineral particles are mainly determined by the total interaction energy (V_T), which is the sum of the London-van der Waals dispersion interaction energy (V_A) and electrostatic repulsive energy (V_R), i.e., Equation (2), and the interaction energy V_A and V_R between two spheres can be calculated by Equations (3) and (4) [23].

$$V_T= V_R+ V_A$$

(2)

$$V_R= \frac{-A_{132}}{6D}\frac{R_1{R}_2}{R_1 + R_2}$$

(3)

$$V_A=\frac{\mathsf{\pi }{\epsilon }_0ϵR_1{R}_2}{R_1 + R_2}\left\{4{\phi }_1{\phi }_{2}ln\frac{1 + e^{-kD}}{1 - e^{-kD}} + \left({\phi }_1^2 + {\phi }_2^2\right)\ln \left(1-e^{-2kD}\right)\right\}$$

(4)

where R₁ and R₂ are the radius of two spheres, D is the separation distance of two spheres. A₁₃₂ is the effective Hamaker constant of substances 1 and 2 interacting in medium 3; it can be calculated by Equation (5), using the Lifshitz approach based on quantum physics [24].${\phi }_1$ and ${\phi }_2$ are the surface potentials of substance 1 and 2, which are substituted by the measured ζ potential value, κ⁻¹ is the double layer thickness (9.6 nm in 1 mM KCl). ε is the dielectric constant of the aqueous medium (78.4 C²·m·J⁻¹), ε₀ is the dielectric constant of vacuum (8.854 × 10⁻¹² C²·m·J⁻¹), the dielectric constants of quartz, hematite and orthoclase are 4.3, 6.9 and 81, respectively [25,26].

$$A_{total}= A_{v=0} + A_{v>0}\approx \frac{3}{4}kT\left(\frac{{\epsilon }_1-{\epsilon }_3}{{\epsilon }_1+{\epsilon }_3}\right)\left(\frac{{\epsilon }_2-{\epsilon }_3}{{\epsilon }_2+{\epsilon }_3}\right)+\frac{3h{v}_e}{8\sqrt{2}}\frac{\left(n_1^2-n_3^2\right)\left(n_2^2-n_3^2\right)}{\sqrt{\left(n_1^2+n_3^2\right)}\sqrt{\left(n_2^2+n_3^2\right)}\left\{\sqrt{\left(n_1^2+n_3^2\right)}+\sqrt{\left(n_2^2+n_3^2\right)}\right\}}$$

(5)

where k_B is the Boltzmann constant (1.381 × 10⁻²³ J·K⁻¹), T is the room temperature (293.15 K), h is the Planck constant (6.626 × 10⁻³⁴ J·s), ν_e is the main electronic absorption frequency in the UV typically around 3 × 10¹⁵ s⁻¹ and n is the refractive index.

4.1. Effects of pH on the Zeta Potential

In this study, the standard minerals of hematite and orthoclase were selected as the main objects of impurity to analyze the processing mechanism. The standard minerals were obtained from commercial vendors. The quartz used in this paper was the concentrate of test No. 3, which was washed several times with distilled water. All the samples were ground and sieved by a 400 mesh for the test.

The ζ potentials of quartz, hematite and orthoclase were measured at different pHs, from neutral to alkaline, with a fixed ionic strength of 1.0 mM KNO₃. As shown in Figure 9, the ζ potentials of both hematite and orthoclase decreased as the pH increased, which were in agreement with the results reported by other researchers [27,28]. Unlike the characteristic of ζ potentials of hematite and orthoclase, one interesting feature has been observed from the plot of ζ potential of quartz. Initially, the ζ potential of quartz decreased as the pH increased from 7 to 9. However, when the NaOH was added to the slurry to increase the pH above 9, this potential of quartz gradually increased; this phenomenon also has been detected by other researchers [29]. The possible reasons for the charge changing of quartz according to the reference could be explained as follows: the metal ions in solution and the clay particles coated on the quartz surface, or the solubility of quartz rises sharply with increasing the solution pH, which could compressed the electric double layers of minerals, and thus, decreased the negative charge potentials [30,31,32].

4.2. Heterocoagulation between Quartz and Impurities

The interaction energy between quartz and impurity particles was calculated based on the DLVO theory firstly. It is important to emphasize that the impurity particles (radius 3 μm) and NPQ (radius 40 μm) were assumed as two ideal spheres and the measured ζ potential value as the surface potential. Figure 10 showed the interaction energy of V_R, V_A and V_T respectively between quartz and hematite (Q–H), quartz and orthoclase (Q–O) at different pHs. When the separation distance was above 3 nm, both of the V_T of Q–H and Q–O were dominated by V_R, and thus, the values were positive as pHs varied from 7 to 11, which suggested that the interaction between quartz and impurities was primarily repulsive in nature. It is also indicated that the V_T change to negative with the V_A tend to negative infinitely when interaction distance being much closer (less than 1 nm), which means that the interaction force was attractive when the impurity particles adhering on quartz surface. The results also illustrated the importance of scrubbing, which provided sufficient energy to overcome the strong V_A between quartz and impurities adhering on quartz surface.

Although the V_T between quartz and impurities always remained positive, the experimental results showed that the removal efficiency of impurities has a strong correlation with the changing of V_T. As can be seen, the V_T was increased gradually with the pH increase from 7 to 9, which is consistent with the changing trend of removal efficiency of impurities according to the previous experiments results. The reason could be explained that the V_T was calculated based on the assumption that the averaging particle size of impurity was 3 μm, but the practical particle size should be normally distributed. According to Equation (2), V_T is roughly proportional to the radius of impurity particle R₁ when the radius of quartz R₂ and the ζ potential of minerals are fixed. When the radius of impurity tends to 0, V_T also tends to zero, which means that there are always a certain proportion of fine impurity particles which could be attracted on the quartz surface easily, and the proportion of particles attached on quartz would decrease with the increase of V_T.

At pH 10, even though the ζ potential of quartz displayed a reverse increase, V_T keeps increasing as the ζ potentials of both hematite and orthoclase decreased, and the effect of pH from 9 to 10 on impurities removal is not notable. When pH was up to 11, V_T reduced significantly, and consequently, a worse impurity removal effect was observed. All the results indicated that increasing V_T by adjusting pH could improve the impurities removal. However, the strong alkaline environment was not beneficial for impurity removal, as the reverse increasing of the ζ potential of quartz.

4.3. Coagulation of Fine Impurity Particles

Apart from the heterocoagulation between quartz and impurity particles, the interaction among fine impurity particles was also calculated to analyze the coagulation, which could also influence impurity removal. Figure 11 indicates the interaction energy between hematite and hematite (H–H), orthoclase and orthoclase (O–O), orthoclase and hematite (O–H) under natural condition (pH = 7). The results showed that the V_T of O–O and O–H were both positive, while the V_T of H–H was negative over the whole separation distance, which indicated that the coagulation of fine particles occurred mainly by the formation of homocoagulation between H–H in the slurry.

V_T of H–H at different pHs is shown in Figure 12. As can be seen, V_T was negative at pH 7 and 8. When the pH increased to 9, V_T was close to zero and then changed to positive at pH 10 and 11. The results indicated that the homocoagulation of H–H occurred more easily when the pH was 7 and 8, and then became dispersive at pH > 9. The conclusion was reinforced by the observation about the stability of slurry of T2, as shown in Figure 13, which showed the settlement of T2 after centrifugation for 24 h at different pH values. As can be seen, when the pH was lower than 9, the fine particles in the slurry were coagulated, and consequently, they settled more easily. On the other hand, when the pH was over 9, the slurry became more stable, which was favorable to the removal of these impurities.

4.4. Effects of SHMP on the Zeta Potential and Desliming

SHMP is a kind of long-chain inorganic salt that has been used as a dispersant for clay mineral separation, which could increase the negative zeta potential of particles, and thus improve the dispersion of slurry [33,34]. The ζ potentials of quartz, hematite and orthoclase were measured at the optimized proportion of SHMP (1 × 10³ g·t⁻¹), according to the previous experiments. As can be seen from

Table 5. ζ potential of quartz, hematite and orthoclase at different dosage of SHMP at pH 7.

ζ	Dosage of SHMP /g·t-1
	0	1000	5000
Quartz	−51.31	−56.03	−38.57
Hematite	−27.01	−61.83	−51.23
Orthoclase	−25.56	−75.07	−67.57

, the addition of SHMP exhibited a remarkable effect on decreasing the ζ potential of all three minerals. As stated in the previous analysis, the ζ potentials of minerals were negative enough to lead to a good dispersion of slurry, which is agreement with the impurity removal results, as shown in Figure 8.

Moreover, ζ potentials of quartz, hematite and orthoclase at the dosage of SHMP being 5 × 10³ g·t⁻¹ were measured to explain the destabilization of impurity removal when excessive SHMP were added. When the dosage of SHMP increased from 1 × 10³ g·t⁻¹ to 5 × 10³ g·t⁻¹, as can be seen, ζ potentials of all three minerals present an inverse increase (absolute value decrease). It should also be noted that the electrical double layers of minerals were significantly compressed at high ionic strengths [35]. All the results indicate that an appropriate dosage of SHMP could improve the removal efficiency of clay impurities in NPQ, but an excessive dosage of SHMP could have a negative impact on the impurity removal, i.e., the same as adjusting pH.

5. Conclusions

In summary, scrubbing combining with centrifugation was proven to be an effective method for the desliming purification of NPQ. The removal efficiency of impurities reached an optimal value at pH 9.3, or when the dosage of SHMP reached 1 × 10³ g/t. The main impurities of Fe₂O₃ and Al₂O₃ in the concentrate decreased to less than 0.01% and 0.02%, respectively. It was concluded that the scrubbing process played an important role in the enhancement of impurities liberation. Then, the addition of regulators such as NaOH or SHMP could effectively increase the negative ζ potential of minerals, and thus increase the V_T, which could effectively decrease the possibility of the heterocoagulation between quartz and impurities, as well as the homocoagulation among hematite particles, consequently improving the removal efficiency of impurities. In conclusion, this technique could be an environment-friendly and highly efficient method for the purification of NPQ.