Next Article in Journal / Special Issue
Selective Attachment of Leptospirillum ferrooxidans for Separation of Chalcopyrite and Pyrite through Bio-Flotation
Previous Article in Journal
Indications that Amorphous Calcium Carbonates Occur in Pathological Mineralisation—A Urinary Stone from a Guinea Pig
Previous Article in Special Issue
Classification of Flotation Frothers
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Depressing Iron Mineral by Metallic-Starch Complex (MSC) in Reverse Flotation and Its Mechanism

School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China
*
Author to whom correspondence should be addressed.
Minerals 2018, 8(3), 85; https://doi.org/10.3390/min8030085
Submission received: 31 January 2018 / Revised: 20 February 2018 / Accepted: 22 February 2018 / Published: 27 February 2018
(This article belongs to the Special Issue Flotation Chemistry)

Abstract

:
A series of metallic-starch complex (MSC) solutions, synthesized by mixing relevant metallic ionic solutions with the caustic starch solution, were used as the flotation depressants to investigate their depressing effects on hematite ore. The MSC is a nano-sized colloidal complex which is configured by hydrophilic metallic hydroxide as the colloidal nucleus on which starch and hydroxyl complex are adsorbed, resulting in a larger molecule than starch itself. The flotation tests showed that the depressing abilities of various MSC (Fe3+, Zn2+, Pb2+ and Mg2+) on the iron minerals were higher than the caustic starch, and the order of depression ability was: Zn2+-starch > Pb2+-starch > Fe3+-starch > Mg2+-starch > caustic starch. Based on the adsorption analysis, the high depressing ability of the MSC arose from increasing the adsorption density of starch on iron minerals and slightly reducing the absorption of the collector dodecylamine. Adsorption behaviour also indicated that the adsorption of the MSC on mineral surfaces was thicker than the caustic starch, and among various MSC the adsorption of Fe3+-starch exhibited the thickest adsorption layer while that of Mg2+-starch the thinnest. Zeta potential indicated that with a weaker electronegativity than the caustic starch, MSC adsorbed onto iron minerals more easily, and the strong electrostatic adsorption with the aid of the hydrogen bonding and chemisorption agreed well with the high depressing ability of the MSC.

1. Introduction

As to flotation of iron ores, much attention is attached to the reverse flotation as a significant commercial separation process using polysaccharide as the depressant for iron minerals and amine as the collector for silica [1,2]. Starch and its derivatives are widely used for depressing iron minerals in flotation due to their widespread source and low cost. In principle, starch usually adsorbs onto iron minerals via its active groups forming hydrophilic films, producing its depressing effect on the iron minerals [3]. Furthermore, Xia et al. [4] reported that hydrogen bonding adsorption is considered as a universal adsorption model for starch in the depressing process of the reverse flotation.
There are two main types of starch; amylopectin and amylose. The amylopectin starch usually produces strong depression on the flotation [5,6], and specially exhibits better depressing action on iron minerals. However, starch as the depressant for fine iron minerals is consumed too much due to high specific surface areas of fines. In order to strengthen the adsorption of starch on iron minerals and reduce its consumption in flotation, starch has been modified through different techniques [7,8], such as various chemical, physical, and compound modifications, etc. Among them, the chemical modification is one of the most widely used modification methods, and so are their modified products, such as dextrin, carboxyl methyl starch, the oxidized starch, and phosphate ester starch. These modified starches have been widely reported only for laboratory studies, but industrially caustic starch has been widely applied in the reverse flotation of iron ore [9,10,11,12]. In fact, the causticization technique, on one hand, is to prepare the caustic starch by conditioning the starch with some alkali solution [13,14]; on the other hand, mixtures of carboxylic acids were found in the caustic starch [15]. So besides the hydroxyl groups, the existence of active carboxylic groups could further facilitate the adsorption of starch onto iron minerals and metallic hydroxide colloids concerned in this study.
There are various active groups in caustic starch. Therefore, some new techniques derived from caustic starch could be introduced into the reverse flotation for iron ores. Yue and Wu [16] recently claimed a marked technique called as “magnetic seeding depression (MSD)” for fine flotation, i.e., adding organic depressant (such as caustic starch) and magnetic seeds and applying a low field intensity pre-magnetization for depressing target minerals in the reverse flotation. This technique was reported to have a strong depressing ability in flotation of hematite ore slimes via the chemical interactions between the magnetic seeds and caustic starch, along with the magnetic interactions between the magnetic seeds and minerals, might be also named as a compound depressor (magnetic starch). In view of this, Wu [17,18] patented a new series of depressants based on the caustic starch composed of metallic hydroxide colloids and starch, known as the metallic-starch complex (MSC) solutions. As a type of nano-sized colloid, MSC synthesized by mixing relevant metallic ionic solutions with the caustic starch solution, could be used as the flotation depressant for iron minerals, producing efficient depressing ability on target minerals with a relatively low consumption of starch. In this study, the flotation of hematite ore in the presence of the metallic-starch complex (MSC) solution was investigated and the mechanism of the strong depression was studied via various measurements.

2. Materials and Methods

2.1. Materials

The sample (86.34% less than 74 µm) used for flotation tests and adsorption analysis was obtained from an iron ore mine in Shandong province, China, and contained 51.55% Fe (Total), 69.06% hematite, and 19.35% SiO2 respectively. Pure hematite (containing 98.02% hematite) with an average size of 17.11 µm was obtained from an iron ore mine by high-intensity magnetic separation and gravity separation, being mostly used for the mechanism analysis.
Caustic starch was conditioned with a ratio of 4 parts starch (potato starch, commercial product) to 1 part sodium hydroxide by using deionized water and boiling the mixture for about 20 min while stirring in the atmosphere. The solution, so-called “caustic starch”, was prepared as a 0.02 g/mL concentration (pH 13.27) for use. In flotation the dodecylamine (DDA, CH3(CH2)11NH2 > 99.7% purity) was prepared into a solution of 0.05 g/mL concentration. The DDA solution (used as the collector) with a 1:1 mole ratio of dodecylamine to acetic acid was conditioned in the deionized water by stirring for certain time.
Metallic-starch complex (MSC) solution [17,18] was synthesized by mixing the 0.02 g/mL caustic starch solution mentioned above with relevant metallic ionic solution (such as Fe3+, Zn2+, Pb2+ and Mg2+ ions), using corresponding soluble salts of FeCl3·6H2O, ZnSO4·7H2O, Pb(NO3)2, and MgCl2·6H2O, respectively. Then, the mixture conditioned with a ratio of 1 part soluble salt to 2 parts starch was maintained at 20 °C and pH 13.27 while stirring for about 20 min. Therefore, the starch in the MSC solution can be calculated as a 0.013 g/mL concentration here. Finally, the suspension (a nano-sized colloid, as confirmed in Table 1) with good dispersion was obtained for use.

2.2. Methods

2.2.1. Reverse Cationic Flotation Tests

For each test sample, 180 g hematite ore sample was dispersed with tap water and conditioned for 3 min in a 0.5 L flotation cell with the pulp of 28.13% solids by weight, and stirred for 5 min after adding moderate depressant. Following the depressant (using caustic starch or the MSC here), collector of dodecylamine (DDA) was introduced into the pulp and conditioned for 3 min. Then, the reverse flotation test was carried out. Finally, the target mineral hematite was depressed as a sink product, and the flotation recovery was calculated from the assaying results.

2.2.2. Total Organic Carbon (TOC) Analyses for Adsorption

In order to determine the amount of starch adsorption onto the particles, the supernatant solutions after conditioning the pulp with the reagents for some time according to the flotation tests were further centrifuged by a general laboratory centrifuge equipment. Then, a 25 mL aliquot of the supernatant in the centrifuge tube was taken for TOC analysis. Finally, the adsorption amount was calculated according to the residual and initial carbon concentration in the solution, as presented in Equation (1) for starch and Equation (2) for DDA, respectively.
Γ s t a r c h = ( C i s C T S C O S C C S ) / M
Γ D D A = ( C i D ( C T D C T S ) C O D C D D A ) / M
where Γ represents the adsorption amount (mg/g), Cis or CiD is the initial concentration (mg/L) of the starch (432 mg/L) or DDA (225 mg/L) added in the suspension, COS or COD is the concentration (mg/L) of the initial starch (2 × 104 mg/L) or DDA (5 × 104 mg/L) solution, CTS or CTD is related to the TOC analysis value (mg/L) of the centrifugal supernatant after the conditioning with the starch or DDA, CCS or CDDA (mg/L) is regarded as the TOC analysis value of the initial starch or DDA solution, M (g/L) refers to the concentration of hematite ore sample (actual value is about 360 g/L).

2.2.3. Adsorption Behaviour of the Metallic-Starch Complex (MSC) on Minerals

The adsorption behaviour study of the metallic-starch complex (MSC) on mica surface was scanned by a Multimode SPM Atomic Force Microscope (AFM) via the Tapping Mode, combined with the Contact Mode. Prior to the measurements, a 120 mg/L concentration of the MSC solution was prepared firstly, and then a fresh mica plate was placed in the solution for 30 min. Finally, the mica plate conditioned with the MSC was blow-dried slightly by the nitrogen and measured by the AFM.

2.2.4. Zeta Potential Measurements

Zeta potentials of hematite and the hematite in the presence of the MSC were measured using a Coulter Delsa-440SX zeta potential analyzer (Brookhaven Corporation, Long Island, NY, USA). To prepare samples for analyses, 0.03 g pure hematite (less than 5 µm) was dispersed in a 50 mL 10−3 mol/L KCl solution by an ultrasonic cleaner, and then stirred at room temperature for 2 min. Then, the reagents were added to the suspension. The mixed suspension was conditioned for 20 min for pH adjustment using HCl or NaOH. Finally, the equilibrium pH was recorded, and a small aliquot of the supernatant in the suspension was transferred to the sample cell of the analyzer for zeta potential measurements, and the average potential values were recorded. In addition, the MSC depressant itself with its concentration of 0.013 g/mL was also analyzed for zeta potentials after pH adjustment.

2.2.5. Fourier Transform Infrared Spectroscopic (FTIR) and X-ray Diffraction (XRD) Studies

To study the adsorption characteristics of the MSC and hematite-MSC, the FTIR analysis of the samples was measured via the transmission method using an IRAffinity-1 spectrometer (Shimadzu Corporation, Kyoto, Japan). Firstly, the pure hematite (−2 μm) was conditioned with the MSC solution in a thermostatic shaker for 20 min at 25 °C. Then, a small part of the suspension was collected for centrifugation, and the precipitate was dried at 55 °C using a vacuum drying oven, and was used for the FTIR analysis. In addition, to understand the characteristics of the MSC, the X-ray diffraction (XRD) studies along with the FTIR measurements of the MSC were performed by crystallizing the MSC solution directly at 55 °C, and then the crystal was ground to less than 5 µm for measurements.

3. Results and Discussion

3.1. Characterization of the Metallic-Starch Complex (MSC)

Based on the preparation method of the MSC, it can be inferred that metallic ions (Fe3+, Zn2+, Pb2+ and Mg2+) could be transformed into corresponding hydrophilic metallic hydroxides and hydroxyl complexes under the strong alkali condition (pH > 13). In order to characterize the MSC, X-ray diffraction, FTIR, turbidity analysis, and nano-particle size testing techniques were used to understand the properties of metallic starch complexes (MSC).
Figure 1 shows the XRD spectra of the MSC and caustic starch. It can be seen that the caustic starch presents an amorphous state. In the Fe3+-starch spectrum the diffraction peaks nearing 26.78° and 55.95° can be attributed to the characteristic of β-FeOOH [19], indicating the presence of β-FeOOH crystal structure in the Fe3+-starch. Then, in the spectrum of Pb2+-starch, the characteristic diffraction peak of (PbCO3)2·Pb(OH)2 and the peak of Pb2O3 were observed at 34.18°, 26.78° and 55.95°, respectively, and these might be due to the decomposition of Pb(OH)2 and its reaction with CO2 during the crystallization of the Pb2+-starch. However, there are no characteristic peaks of Zn(OH)2 found in the Zn2+-starch spectrum; only two characteristic peaks at 36.25° and 36.53° of ZnO were observed. Finally, it was found in the Mg2+-starch spectrum, the bands around 38.04° and 58.76° can be assigned as the characteristics of Mg(OH)2, and MgCO3 was confirmed at 33.15° and 46.53°. These suggested that some metal oxides or carbonates were created during the crystallization of the MSC, indirectly reflecting the possible presence of metallic hydroxides or hydroxyl complexes in the MSC.
Figure 2 presents the FTIR result of the Fe3+-starch. It can be inferred that peaks at 1645 cm−1 and 1016 cm−1 can be assigned as the C=O stretching vibration and the O–H bending vibration, respectively, and the bands around 1160 cm−1 and 1081 cm−1 are attributed to the C–O stretching vibration, demonstrating the characteristics of starch. Then, the peak of Fe–O stretching vibration [10], which was found at 905 cm−1, might be due to the adsorption band of β-FeOOH [20]. Meanwhile, in contrast to the FTIR spectrum of Fe(OH)3 colloids seen in Figure 2, it was found that the Fe(OH)3 could not represent the characteristic component of the Fe3+-starch. These highlighted the presence of the hydrophilic metallic hydroxide (β-FeOOH) which agreed with the XRD results in Figure 1.
Figure 3 shows the FTIR spectra of the MSC. It is seen from the spectrum of Zn2+-starch that peaks of 475 cm−1 and 406 cm−1 can be attributed to the adsorption band of Zn–O [21], and bending vibrations of the hydroxyl of Zn(OH)2 were found around the peak 1087 cm−1, 1037 cm−1 and 768 cm−1. Then, in the spectrum of Pb2+-starch the band nearing the 1382 cm−1 is the O–H bending vibration of the Pb(OH)2, and the stretching vibration of Pb–O can be also observed at 461 cm−1. As shown in the Mg2+-starch spectrum, peaks of 565 cm−1 and 447 cm−1 can be considered as the adsorption band of Mg–O. Due to the high alkali pH of the MSC preparation, hydrophilic metallic hydroxides (such as Fe(OH)3 or β-FeOOH, Zn(OH)2, Pb(OH)2 and Mg(OH)2) could be dissolved into corresponding hydrophilic metallic hydroxyl complexes on their surfaces (such as [Fe(OH)4], [Zn(OH)4]2−, [Pb(OH)4]2− and [Mg(OH)4]2−).
Table 1 listed the turbidity and size of the MSC. As shown in Table 1, MSC exhibits a larger size than the caustic starch, and the size (1–1000 nm) order of them could be given as follows: Mg2+-starch > Zn2+-starch > Pb2+-starch > Fe3+-starch > caustic starch. Meanwhile, the low turbidity of the MSC reveals a high degree of dispersion as a stable solution (or colloid).
Based on the analyses mentioned above, a molecular model could be proposed as follows. To take the Fe3+-starch as an example, starch molecules adsorbed initially on the colloid nucleus (β-FeOOH), resulting in a stable “compound molecule” composed of the nucleus and covering of hydrophilic metallic hydroxyl complexes, together with the starch molecules. The colloid nucleus exhibited a low concentration of FeO+ ions on its surface at low alkali pH, and then grew into a larger nucleus at high alkali pH. Therefore, some OH- and starch molecules would adsorb into the stern layer of the colloid nucleus, forming a “large starch molecule”, surprisingly leading to a particular adsorption effect on iron particles with the aid of the bridging adsorption of the starch and the H-bonding adsorption of the hydrophilic metallic hydroxyl complexes. The proposed model of the MSC (Fe3+-starch) is given in Figure 4.

3.2. Reverse Cationic Flotation Tests

The effects of the metallic-starch complex (MSC) on the flotation performance of hematite ore were investigated at 625 g/t DDA, and the results are seen in Figure 5 and Table 2.
Figure 5 and Table 2 indicated that the flotation recovery of iron minerals increased with the increasing depressant dosage, but the iron recovery of depressant MSC was obviously higher than the caustic starch while adding the same concentration of starch. The flotation recovery using MSC as the depressant was slightly better than that using the same dosage of caustic starch, demonstrating the depressing ability of MSC (Fe3+, Zn2+, Pb2+ and Mg2+) on the iron minerals were higher than the caustic starch, and amongst them, the order of depressing ability was summarized as: Zn2+-starch > Pb2+-starch > Fe3+-starch > Mg2+-starch > caustic starch. In addition, it was also found that the Fe3+-starch displayed the best flotation selectivity among the MSC depressors.

3.3. Adsorption Amount of Reagents onto Iron Minerals in Flotation

Measurements of the adsorption amount of depressant and collector onto mineral particles in flotation pulp were carried out, and the results are presented in Table 3.
Table 3 shows that the MSC adsorbed more on the particles than the caustic starch while slightly reducing the absorption of the collector (DDA), and among them, the Fe3+-starch exhibited a high adsorption of starch and relatively low adsorption of DDA. It can be also inferred that the adsorption abilities of the MSC agreed well with the flotation results in Table 2. Therefore, based on the adsorption analysis, it was confirmed that the MSC produced a high depressing ability through increasing the adsorption amount of starch on iron minerals and slightly reducing the absorption of the collector.

3.4. Adsorption Characteristics of the MSC onto Mica

Figure 6 shows the adsorption behaviour of various MSC on mica surface. It can be seen from Figure 6a that the adsorption effect of the caustic starch was especially weak on the mica surface with a sparse adsorption layer of only 5 nm. However, the Fe3+-starch exhibits up to 50 nm thick and a uniform adsorption layer in Figure 6b. In addition, Figure 6c shows the adsorption behaviour of Zn2+-starch onto mica with a moderate adsorption of 10–15 nm thickness, and in Figure 6d,e both the Pb2+-starch and Mg2+-starch display the adsorption coverage with about 10 nm thickness on the mica surface. It could be demonstrated that all the depressants of the MSC created a higher adsorption thickness on the minerals than the caustic starch, and especially the Fe3+-starch displayed a thicker and smoother adsorption coverage than the other MSC. Therefore, the adsorption difference of the MSC from the traditional caustic starch could partly explain the flotation depressing gap between the two.

3.5. Zeta Potential Measurements

Zeta potential measurements of the MSC and hematite in the presence of the MSC were carried out, and the results are shown in Figure 7 and Figure 8, respectively.
As shown in Figure 7, both the MSC and caustic starch were negatively charged at neutral and alkali pH, but the MSC presents a weaker electronegativity than the caustic starch at the same pH value, and amongst the results of the MSC, the Fe3+-starch exhibits the lowest negative charge while the Zn2+-starch displays the largest negative charge. Therefore, it can be also revealed that the MSC (especially the Fe3+-starch) could adsorb onto iron minerals more easily than the caustic starch while in some cases iron minerals were negatively charged. Figure 8 found that the iso-electric point (iep) of hematite is around pH 6.5 and the hematite has a negative potential at neutral and alkali pH. Meanwhile, the absolute value of hematite potential was raised after adding a certain concentration of caustic starch, however, was weaker by using the Fe3+-starch. In this case, therefore, the adsorption of Fe3+-starch on hematite could facilitate agglomeration of particles more easily than the caustic starch, resulting in a good flotation effect.

3.6. FTIR Spectra of the Hematite Conditioned with the MSC (Fe3+-Starch)

Figure 9 shows the FTIR spectra of hematite in the presence of the MSC (Fe3+-starch). It can be observed in the spectrum of hematite conditioned with the Fe3+-starch that the adsorption peak around 1031 cm−1 is due to the C–O stretching and C–OH bending vibration, and the small adsorption at 1070 cm−1 can be attributed to the C–H bending vibration, and then the COO asymmetric and symmetric stretching bands [10] are also found nearing 1625 cm−1 and 1404 cm−1. The band at 3420 cm−1 can be considered as the stretching vibration of O–H group, suggesting the presence of hydrogen adsorption on the hematite. In addition, the adsorption bands around 561 cm−1 and 467 cm−1 are shifted to 538 cm−1 and 457 cm−1, respectively, indicating the hematite–starch interaction. Therefore, the Fe3+-starch absorbed onto the hematite through the hydrogen bonding adsorption and chemisorption, however, the adsorption characteristic of β-FeOOH in that spectrum was not found at 905 cm−1 probably due to its low concentration in the mixture of the hematite-Fe3+ starch.

4. Conclusions

The MSC is a type of nano-sized colloidal complex which is configured by hydrophilic metallic hydroxide as the colloidal nucleus on which starch and hydroxyl complex are adsorbed, resulting in a larger molecule than starch itself. Amongst the MSC colloids, the Fe3+-starch presented its specific characteristics using β-FeOOH as the colloid nucleus while the other MSC colloid nuclei are synthesized by the corresponding metallic hydroxides (such as Pb(OH)2, Zn(OH)2 and Mg(OH)2).
MSC produced higher depressing ability on the flotation of iron ores than the caustic starch, and different types of the MSC showed some different depressing ability as follows: Zn2+-starch > Pb2+-starch > Fe3+-starch > Mg2+-starch > caustic starch, and the Fe3+-starch displayed the best flotation selectivity among the MSC depressors.
The high depressing ability of the MSC arose from increasing the adsorption density of starch on iron minerals and slightly reducing the absorption of the collector (DDA). All the MSC depressants created a thicker adsorption layer on the minerals than the caustic starch, and especially the adsorption of the Fe3+-starch displayed a thicker and smoother adsorption layer than the other MSC depressants. The strong adsorption ability of the MSC lies in the fact that the MSC exhibited a weaker electronegativity than the caustic starch, therefore leading to a better adsorption result of the starch onto iron minerals. In addition, the absolute value of hematite potential was raised after adding a certain concentration of caustic starch but it was, however, lowered by using the Fe3+-starch.

Acknowledgments

The authors would like to acknowledge the financial support from the National Natural Science Foundation of China (No. 51274256).

Author Contributions

Xiqing Wu and Tao Yue conceived and designed the ideas; Tao Yue performed the experiments; Xiqing Wu and Tao Yue analyzed the data; Xiqing Wu and Tao Yue contributed reagents/materials/analysis tools; Tao Yue and Xiqing Wu wrote the paper.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Ma, X.; Marques, M.; Gontijo, C. Comparative studies of reverse cationic/anionic flotation of Vale iron ore. Int. J. Miner. Process. 2011, 100, 179–183. [Google Scholar] [CrossRef]
  2. Filippov, L.O.; Filippova, I.V.; Severov, V.V. The use of collectors mixture in the reverse cationic flotation of magnetite ore: The role of Fe-bearing silicates. Miner. Eng. 2010, 23, 91–98. [Google Scholar] [CrossRef]
  3. Turrer, H.D.G.; Peres, A.E.C. Investigation on alternative depressants for iron ore flotation. Miner. Eng. 2010, 23, 1066–1069. [Google Scholar] [CrossRef]
  4. Xia, L.; Zhong, H.; Liu, G.; Wang, S. Utilization of soluble starch as a depressant for the reverse flotation of diaspore from kaolinite. Miner. Eng. 2009, 22, 560–565. [Google Scholar] [CrossRef]
  5. Weissborn, P.K.; Warren, L.J.; Dunn, J.G. Selective flocculation of ultrafine iron ore. Mechanism of adsorption of starch onto hematite. Colloids Surf. A 1995, 99, 11–27. [Google Scholar] [CrossRef]
  6. Kar, B.; Sahoo, H.; Rath, S.S.; Das, B. Investigations on different starches as depressants for iron ore flotation. Miner. Eng. 2013, 49, 1–6. [Google Scholar] [CrossRef]
  7. Tharanathan, R.N. Starch—Value addition by modification; Food Hydrocoll. Crit. Rev. Food Sci. Nutr. 2005, 45, 371–384. [Google Scholar] [CrossRef] [PubMed]
  8. Liu, Q.; Wannas, D.; Peng, Y. Exploiting the dual functions of polymer depressants in fine particle flotation. Int. J. Miner. Process. 2006, 80, 244–254. [Google Scholar] [CrossRef]
  9. Filippov, L.O.; Severov, V.V.; Filippova, I.V. An overview of the beneficiation of iron ores via reverse cationic flotation. Int. J. Miner. Process. 2014, 127, 62–69. [Google Scholar] [CrossRef]
  10. Tang, M.; Liu, Q. The acidity of caustic digested starch and its role in starch adsorption on mineral surfaces. Int. J. Miner. Process. 2012, 112, 94–100. [Google Scholar] [CrossRef]
  11. Tang, M.; Wen, S.; Liu, D. Effects of Heating-or Caustic-Digested Starch on its Flocculation on Hematite. Miner. Process. Extr. Metall. Rev. 2016, 37, 49–57. [Google Scholar] [CrossRef]
  12. Peres, A.E.C.; Correa, M.I. Depression of iron oxides with corn starches. Miner. Eng. 1996, 9, 1227–1234. [Google Scholar] [CrossRef]
  13. Weissenborn, P.K. Behaviour of amylopectin and amylose components of starch in the selective flocculation of ultrafine iron ore. Int. J. Miner. Process. 1996, 47, 197–211. [Google Scholar] [CrossRef]
  14. Niemelä, K. Conversion of xylan, starch, and chitin into carboxylic acids by treatment with alkali. Carbohydr. Res. 1990, 204, 37–49. [Google Scholar] [CrossRef]
  15. Jebber, K.A.; Zhang, K.; Cassady, C.J.; Chung-Phillips, A. Ab initio and experimental studies on the protonation of glucose in the gas phase. J. Am. Chem. Soc. 1996, 118, 10515–10524. [Google Scholar] [CrossRef]
  16. Yue, T.; Wu, X.Q. Magnetic seeding depression in flotation of hematite ore slimes. Physicochem. Probl. Miner. Process. 2018, in press. [Google Scholar]
  17. Wu, X.Q.; Yue, T.; Wang, Z.X. Preparation Method and Application of Metallic-Starch Compound Depressants: China. Patent No. 201710049853.8, 23 January 2017. [Google Scholar]
  18. Wu, X.Q.; Wang, Z.X.; Yue, T. Study on depressing effect and mechanism of ferric-starch complex in reverse flotation of an iron mine. Met. Mine 2017, 497, 70–74. (In Chinese) [Google Scholar]
  19. Zhang, M.; Zhang, P.C.; Ni, S.J.; Huang, Y. Experimental study of hydrothermal synthesis of β-FeOOH and removal of Cr (VI). J. Miner. Petrol. 2016, 36, 115–120. (In Chinese) [Google Scholar]
  20. Xu, Y.Q.; Yang, M.; He, C.D.; Xiong, H.X. Characterization and spectral analysis of the stable mineral phases α,β-FeOOH included in iron oxyhydroxides. Spectrosc. Spect. Anal. 2013, 33, 3330–3333. (In Chinese) [Google Scholar]
  21. Chen, S.Z.; Zhong, S.H. Studies on the photo stimulated surface-catalytic reaction of carbon dioxide and water over Cu/ZnO-NiO. Chem. J. Chin. Univ. 2003, 24, 135–139. (In Chinese) [Google Scholar]
Figure 1. XRD spectra of the metallic-starch complex (MSC) and caustic starch.
Figure 1. XRD spectra of the metallic-starch complex (MSC) and caustic starch.
Minerals 08 00085 g001
Figure 2. FTIR spectra of Fe3+-starch.
Figure 2. FTIR spectra of Fe3+-starch.
Minerals 08 00085 g002
Figure 3. FTIR spectra of MSC.
Figure 3. FTIR spectra of MSC.
Minerals 08 00085 g003
Figure 4. The proposed molecular model of the MSC (such as the Fe3+-starch).
Figure 4. The proposed molecular model of the MSC (such as the Fe3+-starch).
Minerals 08 00085 g004
Figure 5. Effect of depressant dosage on the floatation recovery at pH 7.5 (DDA 625 g/t).
Figure 5. Effect of depressant dosage on the floatation recovery at pH 7.5 (DDA 625 g/t).
Minerals 08 00085 g005
Figure 6. Effect of 120 mg/L MSC on the adsorption characteristic: (a,a’) caustic starch; (b,b’) Fe3+ starch; (c,c’) Zn2+ starch; (d,d’) Pb2+ starch; (e,e’) Mg2+ starch.
Figure 6. Effect of 120 mg/L MSC on the adsorption characteristic: (a,a’) caustic starch; (b,b’) Fe3+ starch; (c,c’) Zn2+ starch; (d,d’) Pb2+ starch; (e,e’) Mg2+ starch.
Minerals 08 00085 g006
Figure 7. Zeta potential of various depressants (0.013 g/mL) as a function of pH.
Figure 7. Zeta potential of various depressants (0.013 g/mL) as a function of pH.
Minerals 08 00085 g007
Figure 8. Zeta potential of hematite in the presence of the Fe3+-starch as a function of pH.
Figure 8. Zeta potential of hematite in the presence of the Fe3+-starch as a function of pH.
Minerals 08 00085 g008
Figure 9. FTIR spectra of hematite conditioned with the Fe3+-starch (MSC).
Figure 9. FTIR spectra of hematite conditioned with the Fe3+-starch (MSC).
Minerals 08 00085 g009
Table 1. Turbidity and average size of the MSC at pH 13.27 (NTU: Nephelometric Turbidity Unit).
Table 1. Turbidity and average size of the MSC at pH 13.27 (NTU: Nephelometric Turbidity Unit).
MSC Caustic StarchFe3+-StarchZn2+-StarchPb2+-StarchMg2+-Starch
Turbidity/NTU28.32144.21230.63187.41346.83
Average size/nm97.47202.22464.34326.70645.18
Table 2. Effect of MSC on the flotation performance (depressant 1200 g/t, DDA 625 g/t, pH 7.5).
Table 2. Effect of MSC on the flotation performance (depressant 1200 g/t, DDA 625 g/t, pH 7.5).
DepressantMass Recovery/%Grade Total Fe/%Recovery of Total Fe/%
Caustic starch72.5558.1181.79
Fe3+-starch76.6558.1886.50
Zn2+-starch80.1657.4989.40
Pb2+-starch78.7057.7488.15
Mg2+-starch76.0257.9685.47
Table 3. Effect of MSC on the adsorption of flotation reagents (depressant 1200 g/t, DDA 625 g/t, pH 7.5).
Table 3. Effect of MSC on the adsorption of flotation reagents (depressant 1200 g/t, DDA 625 g/t, pH 7.5).
DepressantRecovery of TFe/%Adsorption of Starch/mg/gAdsorption of DDA/mg/g
Caustic starch81.790.2105 0.2317
Fe3+-starch86.500.2496 0.2187
Zn2+-starch89.400.3103 0.2206
Pb2+-starch88.150.2788 0.2216
Mg2+-starch85.470.2598 0.2253

Share and Cite

MDPI and ACS Style

Yue, T.; Wu, X. Depressing Iron Mineral by Metallic-Starch Complex (MSC) in Reverse Flotation and Its Mechanism. Minerals 2018, 8, 85. https://doi.org/10.3390/min8030085

AMA Style

Yue T, Wu X. Depressing Iron Mineral by Metallic-Starch Complex (MSC) in Reverse Flotation and Its Mechanism. Minerals. 2018; 8(3):85. https://doi.org/10.3390/min8030085

Chicago/Turabian Style

Yue, Tao, and Xiqing Wu. 2018. "Depressing Iron Mineral by Metallic-Starch Complex (MSC) in Reverse Flotation and Its Mechanism" Minerals 8, no. 3: 85. https://doi.org/10.3390/min8030085

APA Style

Yue, T., & Wu, X. (2018). Depressing Iron Mineral by Metallic-Starch Complex (MSC) in Reverse Flotation and Its Mechanism. Minerals, 8(3), 85. https://doi.org/10.3390/min8030085

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop