The Desulfurization of Magnetite Ore by Flotation with a Mixture of Xanthate and Dixanthogen

Abstract

The contamination of sulfur emanating from pyrrhotite in magnetite concentrates has been a problem in iron ore processing. This study utilized froth flotation to float pyrrhotite away from magnetite using collectors of xanthate and dixanthogen. It was found that xanthate or dixanthogen alone could not achieve selective separation between pyrrhotite and magnetite in flotation. A high loss of magnetite was obtained with xanthate, while a low desulfurization degree was obtained with dixanthogen. It was interesting that a high desulfurization ratio was achieved with little loss of magnetite when xanthate was mixed with dixanthogen as the collector. The synergistic effect of the mixed collector on pyrrhotite was studied by electrokinectic studies and FTIR measurements. It was found that xanthate was the anchor on pyrrhotite and determined its selectivity against magnetite, while dixanthogen associated with xanthate, enhancing its hydrophobicity. This study provides new insights into the separation of iron minerals.

1. Introduction

In recent decades, there has been an ever-increasing demand for iron ore because of its great demand in metallurgy industries [1]. Due to the depletion of high quality iron ores, complex ultrafine iron ores with a high content of impurities, such as sulfur, have been processed [2]. Pyrrhotite (Fe_1−xS) is a kind of common sulfide which exists in magnetite ore as an associated mineral with little industrial value. The contamination of sulfur emanating from pyrrhotite in magnetite concentrates has been a problem in iron ore smelting process. However, the magnetic separation of pyrrhotite from magnetite is problematic, due to their similar magnetic property and magnetic flocculation between pyrrhotite and magnetite [3].

Flotation has been commercially used as a method for removing pyrrhotite from magnetite for high sulfurous iron ores [4]. In this process, pyrrhotite as a primary impurity is separated from iron ore using typically potassium butyl xanthate as the primary collector. The flotation process normally adds copper sulfate as an activator which could accelerate the flotation rate of pyrrhotite. The flotation is conducted at the natural pH of the milled ore which may vary between 7.5 and 9 but it is typically closer to the higher value [5]. However, in the practice of iron ore flotation, the loss of valuable mineral in tailings is the major problem confronting the iron ore industry. Thus, the reagent suit is formulated to create the appropriate chemical environment for effective separation. The collector suit is often tuned to use mixed collectors to enhance both grade and recovery of the concentrate, and to lower cost [6].

The use of dissimilar surfactant mixtures can have a synergistic advantage over the use of individual surfactants [7,8,9,10,11]. The influence of nonionic reagents on anionic collector flotation of calcium minerals was investigated [12]. The addition of nonionic reagents to anionic collectors enhanced the flotation separation efficiency of calcium minerals due to hydrophobic chain interactions and reduction of electrostatic repulsion between ionic head groups that are shielded from each other by the nonionic surfactant molecules. A process involving the use of mixed anionic and cationic collectors for muscovite mica was studied [13]. The flotation recovery could be enhanced using a mixture of dodecylamine acetate with sodium oleate. The adsorption of both the cationic and anionic collectors was enhanced due to co-adsorption. A combined cationic (amine) and anionic collector (sodium xanthate) was also reported to be effective for the flotation of zinc oxide at pH 11 [14].

In this study, attempts were made to enhance the selective separation of pyrrhotite from magnetite. Flotation experiments were conducted with different collector suits (xanthate, dixanthogen, and their mixture). The synergetic effects of mixing dixanthogen with xanthate were also studied by zeta potential and infrared spectroscopic measurements.

2. Materials and Methods

2.1. Materials

A magnetic concentrate was obtained from Baogang plant (Neimeng, China). The principal research sample was the magnetic product of the primary iron ore containing 65.10% Fe. The results of chemical analyses of this sample are given in Table 1 and the chemical compositions of which are given in Table 2. From Table 1 and Table 2, it is observed that the magnetite, pyrrhotite, quartz, and calcite are the main compositions in this sample.

Table 1. Chemical analysis results of magnetic concentrate (mass fraction, %).

Composition	TFe *	Fe2O3	SiO2	Al2O3	K2O	CaO	MgO	P	S	TiO2
wt %	65.10	92.35	3.54	0.35	0.026	1.68	0.25	0.049	1.64	0.10

* TFe: Total iron.

Table 2. Analysis of iron chemical phase in the magnetic concentrate (mass fraction, %).

Composition	Magnetite	Pyrrhotite	Pyrite	Quartz	Calcite	Dolomite	Phyllite	Barite
wt %	86.88	4.32	0.23	3.56	2.56	1.22	0.47	0.75

The pure pyrrhotite mineral and magnetite used in this study was provided by Baogang Mine, Neimeng Province, China. The mineral compositions of pure pyrrhotite and magnetite were analyzed by Mineralogical Liberation Analysis (MLA). The analysis results in Table 3 and Table 4 show that it was of high purity with minor impurities in pyrrhotite and magnetite. The lumps of pyrrhotite and magnetite were crushed and ground to a particle size less than 74 µm in a ceramic ball mill. The powder of −74 µm was further ground to −2 µm for zeta potential and FTIR experimental studies. The mineral sample was stored in a glass drying dish for further investigations.

Table 3. Minerals compositions of pure pyrrhotite.

Minerals	Pyrrhotite	Chalcopyrite	Limonite	Dolomite	Quartz	Mica
wt %	98.51	0.32	0.10	0.35	0.08	0.40

Table 4. Minerals compositions of pure magnetite.

Minerals	Magnetite	Quartz	Calcite	Ankerite	Phyllite	Siderite
wt %	97.12	0.84	0.45	0.33	0.41	0.22

The collector used in the tests was sodium butyl xanthate (NaBX, CH₃CH₂CH₂CH₂OCS₂Na) supplied from Zhuzhou Flotation Reagents Plant (Zhuzhou, China). Dibutyl dixanthogen ((BX)₂) was used as a collector which was synthesized with xanthate and hydrogen peroxide. The Dibutyl dixanthogen was purified by extraction. Sodium fluosilicate (Na₂SiF₆) was used as an activator. Sodium carbonate, sulfuric acid, hydrochloric acid, and sodium hydroxide of analytical grade from Kemiou Chemical Reagent Co. Ltd. (Tianjin, China) were used to regulate the pH of the system. Pine oil has been used as the frother. Distilled water was used in all the experiments.

2.2. Methods

2.2.1. Grinding and Flotation Experiments

The grinding was carried out at room temperature using tap water. 400 g magnetic concentrate sample at 66.7% solid density was ground in a ball mill to gain an 85 wt % passing size of 74 μm. The mill discharge was transferred to a 1.0 dm³ XFD-type laboratory flotation cell. The air flow rate was 45 dm³/h and the agitation speed was 1800 rpm. The flotation experiments were carried out in accordance with the flow sheet shown in Figure 1. The activator (Na₂SiF₆) was added to the slurry and conditioned for 15 min. The pH regulator (H₂SO₄ or Na₂CO₃), collector, and pine oil were added successively to the slurry and conditioned for 3 min, 3 min, and 1 min, respectively before flotation. The flotation tailing (froth product) was collected for 3 min. In the study, the effect of different collectors, flotation pH values, and mixed collector rates were investigated.

Figure 1. Flow sheet of flotation tests.

The concentrates and tailings from flotation after the filtering and drying were weighed and assayed, respectively. The experiments were repeated three times, and the average values were reported. The experimental error was found to be 3%–5%. The magnetite recovery of flotation concentrate was calculated by the following equation:

$${\mathsf{\epsilon }}_{\mathrm{m}}=\frac{\mathsf{\gamma }·({\mathsf{\beta }}_1-1.59{\mathsf{\beta }}_2)}{{\mathsf{\beta }}_0-1.59{\mathsf{\beta }}_3}$$

(1)

where Ɛ_m is the magnetite recovery in concentrate, β₁ is the Fe grade of concentrate, β₂ is the S grade of concentrate, β₀ is the Fe grade of raw ore, β₃ is the S grade of raw ore, γ is yield of concentrate, and the rate of Fe to S is 1.59 in pyrrhotite. The equation is a criterion for evaluating the loss of magnetite.

The desulfurization ratio of flotation process was calculated by the following equation:

$$\mathrm{D}=1-\frac{\mathsf{\gamma }·{\mathsf{\beta }}_1}{{\mathsf{\beta }}_0}$$

(2)

where D is desulfurization ratio of flotation process, γ is yield of concentrate, β₁ is the S grade of concentrate, and β₀ is the S grade of raw ore.

2.2.2. Industrial Tests

The industrial tests were performed in the Mineral Processing Plant at the Baotou iron Mine. The experimental system S1 used mixed collector (${\mathrm{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2)$ as collector. The comparative system S2 was the original plant setup of the Baotou Plant, which used NaBX as collector in the flotation. Figure 2 shows the flotation circuit of industrial experiment in Baotou iron mine. The rougher and cleaner of the industrial experiment system are composed of 6 and 4 units of 40 m³ flotation cells, respectively. The scavenger consists of 4 units of 4 m³ flotation cells. The flotation conditions of industrial tests are also described in Figure 2. The processing capacities of S1 and S2 were 169.73 and 186.37 t/h, respectively.

Figure 2. The flow sheet of industrial flotation in the Baotou iron Mine.

2.2.3. Zeta Potential Measurements

The zeta potentials of the minerals were measured using a ZetasizerNano ZS90 (Malvern, Worcestershire, UK). A suspension containing 0.01 wt % mineral particles ground to −2 µm in an agate mortar was prepared in the KCl solution (10⁻³ M). The measurements were conducted at room temperature (25 °C). The pH value of the suspension was adjusted to a desired value using HCl or NaOH solution. Besides, measurements were also carried out with the addition of collector at a constant concentration in the presence of sodium fluosilicate (10⁻⁴ M). The average zeta potential values of at least three independent measurements were recorded with a measurement error of ±2 mV.

2.2.4. FTIR Measurements

Fourier Transform Infrared (FTIR) spectra ranging from 4000 to 400 cm⁻¹ were used to characterize the collectors and their adsorption on the mineral surface at room temperature. The pure mineral samples were ground to less than 2 µm before conditioned with the collectors (10⁻³ M). The mineral sample was reacted with collector in the presence of sodium fluosilicate (10⁻⁴ M). The pellets were prepared by mixing KBr and sample at the mass ratio of 200/1. The spectra of the samples were obtained with KBr pellets by a Fourier transform infrared spectrometer (Nicolet, WI, USA).

2.2.5. Contact Angle Measurements

The contact angle were measured using Kruss K100 instrument (KRüSS, Hamburg, Germany). The pure mineral samples (37–44 µm) were conditioned with collectors by laboratory flotation machine (1800 rpm) for 5 min. The froth product from flotation after drying (60 °C) was pressed to round tablets (d = 1 cm). Finally, the contact angle measurements were performed. The measurements were repeated three times and the average values and standard deviations were reported.

3. Results and Discussion

3.1. Flotation

3.1.1. Effect of Collector

The flotation tests were conducted with individual collector NaBX, (BX)₂ and mixed collector $\left({\mathrm{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2\right)$. The recovery-collector concentration curves of magnetite at pH 6 are presented in Figure 3. It shows that the recovery of magnetite with (BX)₂ is independent of (BX)₂ concentration and the magnetite recovery changed in the range of 97.93%–98.24% in the studied concentration range. When using NaBX as collector, the recovery of magnetite is the lowest compared with the other two groups and decreased sharply with the increase of the collector concentration. In the case of (BX)₂/NaBX, it is clear that the magnetite recovery of concentrate is higher than those of single collectors, meanwhile the magnetite recovery has little decrease with an increase of collector concentration. Figure 4 shows the desulfurization ratio of flotation performance as a function of collector concentration. For mixed collector system, the desulfurization ratio curve is similar to that of NaBX, which is much higher than that of (BX)₂. It can be concluded that a high desulfurization ratio was achieved with little loss of magnetite when xanthate was mixed with dixanthogen as the collector, indicating that the mixed collector shows better selectivity than single collectors.

Figure 3. Flotation recoveries of magnetite with individual collector NaBX, (BX)₂ and mixed collector $\left({\mathrm{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2\right)$ as a function of collector concentration (NaSiF₆ 500 g/t, pine oil 46 g/t, pH = 6).

Figure 4. Desulfurization ratio of flotation performance with individual collector NaBX, (BX)₂ and mixed collector $\left({\mathrm{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2\right)$ as a function of collector concentration (NaSiF₆ 500 g/t, pine oil 46 g/t, pH = 6).

The order of collector strength for the reagents used in this study has been reported to be NaBX > (BX)₂ based on the chemical nature of the collector’s group [15]. Results in this study match this order, as NaBX was found to have much better desulfurization performance when compared to (BX)₂. A possible explanation for this phenomenon is that NaBX is a stronger collector than (BX)₂. It has already been noted that the most significant decrease of magnetite recovery in flotation concentrate is when using NaBX compared to that of (BX)₂. A possible reason could be that the selectivity (BX)₂ is superior to NaBX. It should be also noted that the mixed collector resulted in an overall enhancement in both magnetite recovery and desulfurization performance since each individual collector plays a different role on the flotation. In the mixed system, both the adsorption of (BX)₂ and NaBX collectors are enhanced due to co-adsorption. Adsorption of NaBX may be enhanced by the presence of (BX)₂ due to hydrophobic chain interactions and the reduction of electrostatic repulsion between ionic head groups of NaBX that are shield from each other by (BX)₂ molecules.

3.1.2. Effect of Mixed Collector Ratio

The flotation capacities of the NaBX, (BX)₂, and their mixture were investigated with batch flotation tests. It is important to take into account that the weight ratio of mixed collector ((BX)₂/[NaBX + (BX)₂]) in pyrrhotite flotation tests. Figure 5 shows the flotation performances of mixed collectors with various ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ at pH = 6.0. The results show that the magnetite recovery sharply increased with increasing ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$, reaching a maximum value (98.11%) at ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ = 40% (the weight ratio of (BX)₂:NaBX = 2:3). At ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ > 40%, the magnetite recovery becomes slowly decrease. It also can be seen from Figure 5 that the desulfurization ratio of concentrate decreased slowly when the fraction of (BX)₂ increased from 0 to 40 wt % and thereafter the desulfurization ratio decreased significantly. There is a marked positive synergistic effect between NaBX and (BX)₂ on flotation of pyrrhotite. The mixed collector (BX)₂/NaBX is beneficial for the flotation of pyrrhotite, and the optimum weight ratio of (BX)₂ to NaBX is 2:3. Therefore, the mixed (BX)₂/NaBX with a weight ratio of 2:3 is selected for the following study.

Figure 5. The magnetite recovery and desulfurization ratio in flotation concentrate with mixed collector at different combinations (mixed collector 125 g/t, NaSiF₆ 500 g/t, pine oil 46 g/t, pH = 6).

3.1.3. Effect of the pH Value

As we all know, the pH plays an important role in flotation system by controlling both mineral solubility and acid-base property of mineral pulp. Figure 6 shows the flotation response of magnetite recovery and desulfurization ratio as a function of pH with mixed collectors NaBX/(BX)₂ (${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}=40\%$). The results clearly indicate that, with mixed collector, the recovery of magnetite increased from 96.66% to 99.33% when the pH value increased from 5.0 to 8.0. It also can be seen that the desulfurization ratio of flotation concentrate had little decrease with the increase of pH until around pH 6.0 and thereafter the desulfurization ratio decreased dramatically, which indicated that pyrrhotite flotation is sensitive to pH value. Therefore, the maximum flotation response of pyrrhotite away from magnetite was attained with the mixed collector at pH around 6.

Figure 6. The magnetite recovery and desulfurization ratio in flotation concentrate as a function of pH with mixed collector (NaBX 75 g/t, (BX)₂ 50 g/t, NaSiF₆ 500 g/t, pine oil 46 g/t).

It is well known that pyrrhotite is a reactive sulphide mineral and easy to be oxidized in alkaline solutions [16]. The general oxidation mechanisms may be described by the following reactions [17,18]. The formation of Fe(OH)₃ precipitation on the surface of pyrrhotite decreases surface hydrophobicity of pyrrhotite and this is why the desulfurization ratio decreased as the pH increased. In addition, another possible reason could be that the synergetic effect was poor since part of dixanthogen may transform into xanthate in an alkaline environment.

$${\text{Fe}}_{1-x}{\mathrm{S}}_{\mathrm{s}}+\left(2-\frac{1}{2}x\right){\mathrm{O}}_2+x{\mathrm{H}}_2\mathrm{O}\to \left(1-x\right){\text{Fe}}^{2+}+{\text{SO}}_4^{2-}+2x{\mathrm{H}}^{+}$$

(3)

$${\text{Fe}}^{2+}+\frac{1}{4}{\mathrm{O}}_2+{\mathrm{H}}^{+}\to {\text{Fe}}^{3+}+\frac{1}{2}{\mathrm{H}}_2\mathrm{O}$$

(4)

$${\text{Fe}}^{3+}+3{\mathrm{H}}_2\mathrm{O}\to \text{Fe}{\left(\text{OH}\right)}_3+3{\mathrm{H}}^{+}$$

(5)

3.2. Industrial Tests

Because of the good effect of mixed NaBX/(BX)₂ for pyrrhotite flotation, the mixed collector (${\mathrm{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2$) was selected in the industrial tests performed in the Mineral Processing Plant of the Baotou iron Mine. The flotation flowsheet and flotation conditions are listed in Figure 2, and the flotation results are shown in Table 5. It can be seen from the results that the grade and recovery of iron increased significantly when the industrial tests were performed in the S1 system, which indicates that mixed collector had a good selectivity on the flotation of pyrrhotite while having a similar desulfurization capacity in comparison with the system S2. Since the industrial tests, mixed collector has been commercially used in the Baotou iron Mine.

Table 5. The results of industrial flotation tests on September.

System	Products	Yield (wt %)	Grades (%)		Recoveries (%)
			Fe	S	Fe	S
S1 Mixed collector	Concentrates	91.23	69.25	0.43	92.50	19.62
	Tailings	8.77	58.42	18.75	7.50	80.38
	Feed	100.00	68.30	2.05	100.00	100.00
S2 NaBX	Concentrates	88.92	69.13	0.44	90.24	19.32
	Tailings	11.08	60.01	14.75	9.76	80.68
	Feed	100.00	68.12	2.03	100.00	100.00

3.3. Zeta-Potential Measurements

Zeta potentials of pyrrhotite in the absence and presence of NaBX, (BX)₂ and their mixture as a function of pH are illustrated in Figure 7. The results show that the zeta potential of pyrrhotite in distilled water decreased with the increase of the pH, and the isoelectric point of pyrrhotite was about 8.6 in distilled water, which is in agreement with the results obtained by other researchers [19]. The zeta potential with dixanthogen when used alone appeared to be similar at the pH range between 2 and 12. It indicated that dixanthogen had a little effect on the zeta potential at all studied pH values. This could be attributed to low ionizability of dixanthogen or low adsorption of the desired collector on the pyrrhotite surface. In the presence of NaBX, the zeta potential decreased significantly and the isoelectric point changed from 8.6 to about 4.5. It indicated that the anionic collector adsorbed onto the pyrrhotite surface by chemical bonding. In the presence of mixed NaBX/(BX)₂, the zeta potentials were more positive than that in the presence of NaBX alone, but more negative when compared to (BX)₂ alone. This might be explained by the fact that dixanthogen, a neutral and strongly hydrophobic collector, adsorbed on the pyrrhotite surface as a co-collector [14].

Figure 7. The zeta potential of pyrrhotite in the absence and presence of NaBX, (BX)₂, and their mixture as a function of pH value, respectively.

It can be seen in Figure 8 that the zeta potential of magnetite in distilled water decreased with the increase of the pH, and the isoelectric point of magnetite was about 6.5 in distilled water. When magnetite interacts with NaBX, (BX)₂, and their mixture respectively, zeta-potential values are very close to that in water. Thereby, it may be concluded that no significant NaBX, (BX)₂, and their mixture are adsorbed on magnetite.

Figure 8. The zeta potential of magnetite in the absence and presence of NaBX, (BX)₂, and their mixture as a function of pH value, respectively.

3.4. FTIR Analysis

In order to investigate the adsorption mechanism of NaBX, (BX)₂, and their mixture on the mineral surfaces, the collectors, minerals, and minerals after reacting with collectors were characterized by infrared spectrometry at 298 K. The IR spectra of NaBX and (BX)₂ are shown in Figure 9 and Figure 10, respectively. The spectra are given for the region 600–1600 cm⁻¹ where all the absorption bands are characteristic of the NaBX and (BX)₂ polar groups. The characteristic IR spectral peaks of these collectors are very similar to that gained by other researcher [20]. In Figure 9, the characteristic peaks at 1168.92 and 1191.95 cm⁻¹ arise from asymmetric stretching vibration of C–O–C in NaBX. The peak frequency at 1111.20 cm⁻¹ originates from symmetric stretching vibration of C–O–C in NaBX. The peak at 1062.06 cm⁻¹ is assigned to the stretching vibration of the C=S group of NaBX.

Figure 9. FTIR spectrum of sodium butyl xanthate.

Figure 10. FTIR spectrum of dibutyl dixanthogen.

In Figure 10, the IR spectrum of (BX)₂ contains intensive symmetric stretching vibration of C–O–C with peak frequencies at 1157 and 1179 cm⁻¹. The peak at 1265 cm⁻¹ is assigned to the asymmetric stretching vibration of C–O–C in (BX)₂. The characteristics peak at 1027 cm⁻¹ is attributed to stretching vibration of C=S in (BX)₂. It can be seen that stretching vibration frequencies of C–O–C in (BX)₂ shift toward higher frequencies when the vibration frequency of C=S shifts toward lower frequencies compared to that of NaBX. The same trend can be found in previous research [21,22].

The FTIR spectrum of pyrrhotite after reacting with NaBX is shown in Figure 11. The peak at 1048 cm⁻¹ is assigned to C=S stretching vibration of Fe(BX)₃. The weak bond at 1117.39 cm⁻¹ is attributed to stretching vibration of C–O–C in Fe(BX)₃. None of the characteristics peak of (BX)₂ can be seen in Figure 11.

Figure 11. FTIR spectra of pyrrhotite after reacting with NaBX at pH = 6.

The FTIR spectrum of pyrrhotite after reacting with mixed collector (${\text{m}}_{\text{NaBX}}:{\mathrm{m}}_{{\left(\text{BX}\right)}_2}=3:2$) is shown in Figure 12. After the interaction with the mixed collector, both the characteristic IR spectral peaks of Fe(BX)₃ and (BX)₂ can be observed on the mineral surface. The stronger characteristic peaks at 1029.01 and 1262.67 cm⁻¹ could be identified as the stretching vibration of C=S in xanthate and the C–O–C stretching vibration of (BX)₂, respectively [22,23]. The weaker peaks at 1102.15 and 1131.90 cm⁻¹ are assigned to the stretching vibration of C–O–C in xanthate. It can be found that the C=S stretching vibration of xanthate iron shifts toward to lower frequency compared to that of NaBX. The results indicate that the xanthate and dixanthogen molecules are bound directly to the pyrrhotite surface.

Figure 12. FTIR spectra of pyrrhotite after reacting with mixed collector (NaBX + (BX)₂) at pH = 6.

3.5. Wetting Characteristic of Pyrrhotite wih Mixed Collectors

The wettability nature of mixed (BX)₂/NaBX collectors on pyrrhotite and thereby synergistic effect between (BX)₂ and NaBX on solid/liquid interface were investigated by contact angle measurement. Figure 13 presents the contact angle of pyrrhotite as a function of ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$. It can be seen that there is an increase in the contact angles of pyrrhotite when (BX)₂ is added to an NaBX in the low ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ range, and the contact angle reaches the maximum value, improving up to about 70° when ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ is 45%. In other words, combined use of the reagents strengthens the hydrophobicity of pyrrhotite surface and produces greater contact angles. This phenomenon has been discovered previously by Xu [24]. It is because that the hydrophobicity of (BX)₂ is greater than NaBX, and the NaBX could increase the solubility of (BX)₂ at the same time. However, as the ${\mathsf{\alpha }}_{{\left(\text{BX}\right)}_2}$ further increases, the contact angle of pyrrhoite decreases. The reason could be explained by low solubility of (BX)₂.

Figure 13. Contact angle vs. mass fraction of (BX)₂ for pyrrhotite with mixed collectors at pH 6.0.

4. Conclusions

The synergetic effect of mixed collector systems of (BX)₂ and NaBX was investigated by flotation tests. The separation effect between pyrrhotite and magnetite was dramatically enhanced in terms of both magnetite recovery and desulfurization ratio. The ideal composition of the mixed collector was determined by batch flotation tests to be 40 wt % (BX)₂ and 60 wt % NaBX for pyrrhotite flotation. A reasonable pH value for application of the collector mixture was determined to be around 6.0.

The zeta potential experiments indicated that chemical adsorption occurred on the pyrrhotite surface. The FTIR analysis showed that the groups of NaBX and (BX)₂ participated in the chemical reaction. The contact angle results indicated there was a synergistic effect of mixed (BX)₂ and NaBX collectors at the solid-liquid interface. In the mixed systems, dixanthogen associated with xanthate, enhancing hydrophobicity of pyrrhotite due to co-adsorption.