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Rem: Revista Escola de Minas

Print version ISSN 0370-4467On-line version ISSN 1807-0353

Rem: Rev. Esc. Minas vol.68 no.3 Ouro Preto July/Sept. 2015

https://doi.org/10.1590/0370-44672015680051 

Mining

Influence of Mn2+ ion in reverse cationic flotation of iron ore

Daniel Geraldo Cruz 1  

Rosa Malena Fernandes Lima 2  

1Engenheiro metalurgista e mestre pelo PPGEM Universidade Federal de Ouro Preto Escola de Minas - Engenharia de Minas Ouro Preto – Minas Gerais – Brasil danyelgc@yahoo.com.br

2Professora Associada Universidade Federal de Ouro Preto Escola de Minas - Engenharia de Minas Ouro Preto – Minas Gerais – Brasil rosa@demin.ufop.br


ABSTRACT

This paper presents the study results of Mn2+ ion influence on reverse cationic flotation of iron ore at pH 10.5. A small influence was observed on all response variables evaluated: mass recovery, Fe metallurgical recovery, grade of Fe and SiO2 in obtained concentrates for dosages of MnCl2 from 600 g/ton. The conditioning of pulp with ethylene diamine tetraacetic acid - EDTA complexing agent (720 g/ton) in presence of MnCl2 (600 g/ton) at natural pH, before the addition and conditioning with corn starch (400 g/ton) and amine (50 g/ton) at pH 10.5, produced a concentrate with 63% Fe, 5.1% SiO2, which is similar to results obtained in flotation test without manganese species present in pulp.

Key words: Iron ore; reverse cationic flotation; Mn2+ ion; EDTA

1. Introduction

The Brazilian iron ore reserves correspond to 13.6% of the total world reserves. The world production of iron ore in 2013 was estimated at 3 billion tons (similar to the previous year). The Brazilian production was of 386.3 Mt with an average content of 63.6% Fe (third largest world production) split into pebble ore (10.7 %) and fine products (pellet feed and sinter feed) (89.3 %). About 70 % of Brazilian production comes from Minas Gerais State (60 Mt in 2012) (DNPM, 2014).

It is a common practice in Iron Quadrangle – Minas Gerais State to concentrate the fraction fines of iron ore by gravimetric, magnetic separation and flotation methods. As well known, the method choice to concentrate a specific iron ore depends on several factors such as its physical and mineralogical properties, and the liberation fraction size of quartz (Araujo et al., 2003; Filippov et al., 2014).

The cationic reverse flotation at pH 10.5, using corn starch as iron minerals depressant and amine as silicate gangue collector, is the most successful route used to concentrate fines of iron ores (Filippov et al., 2014, Araujo et al., 2005). However, the particles in fraction size smaller than 4 µm hamper the selectivity of this process route. To solve this problem a previous deslaming operation is used, which causes metal loss (Houot, 1983; Ma et al., 2011; Filippov et al., 2014).

Multivalent cations and its hydroxy-complexes formed in water can adsorb on the surface of minerals in pulp, modifying their surface charges and thus interfering in the action of flotation reagents, causing the loss of selectivity in the process. Therefore, it is necessary to treat the process water or to complex the multivalent metallic cations present in the pulp before addition of depressant and collector reagents (Pinheiro et al. 2012, Lelis, 2014).

Lelis (2014) studied the effect of Mn2+ species on recoveries of hematite and quartz at pH 10.5 without and with previous complexion by EDTA. In this basic, study the researcher observed that the depression of quartz by manganese species was effective only for dosages from 100 mg/L. In this pH value the dominant manganese species is Mn(OH)2(s), which settled on both mineral surfaces. The recoveries of both minerals studied were restored by previous complexation of manganese species by EDTA.

In this paper are presented the results of the effect of MnCl2 on bench cationic reverse flotation carried out with an iron ore at pH10.5 and the use of EDTA as complexing agent of Mn2+ ions in pulp.

2. Materials and methods

2.1 Materials

The iron ore from conventional flotation feed of industrial flow sheet of Samarco A. S. was used in bench flotation tests at pH 10.5. The d80 of the ore was equal to 135µm. The mineral phases identified by X-ray diffractometry were quartz, hematite and goethite. The contents of Fe and SiO2 were respectively 44.7% and 31.8% (Cruz, 2015).

In the flotation tests, the following reagents were used: commercial etheramine acetate (Flotigam EDA) with 50% of neutralization degree (Clariant A.S.) as collector; MnCl2.4H2O (Mn2+ ions source) and EDTA complexing (C10H14N2O8Na2.2H2O) of analytical purity provided by Sinth (Labsynth Products for laboratories LTDA), commercial corn starch (Unilever A.S) as depressant; NaOH and HCl of analytical purity (VETEC A.S.) as pH control.

2.2 Methods

The bench flotation tests, using tap water, were performed using a CDC flotation cell, at 1200 rpm speed , pulp density of 45 %wt., using a vessel of volume 2L. All tests were carried out at pH 10.5, 400 g/ton of corn starch and 50 g/ton of amine, which was determined by Cruz (2015).

The procedure adopted for bench flotation tests was (Cruz, 2015):

i. Preparation of a pulp with 45 %wt. density (1800 mL of water at pH 10.5 and 1500g of ore).

ii. Setting speed cell at 1200rpm.

iii. Addition of the appropriate solution volume with ions Mn2+, corresponding to the established dosage for each test, and conditioning for 6 minutes.

iv. Addition of starch solution (1 %wt.), corresponding to 400g/ton dosage.

v. Pulp pH setting to 10.5 and conditioning for 5 minutes.

vi. Addition of amine solution (1 %wt.), corresponding to the dosage of 50g/ton.

vii. pH correction, if necessary, and conditioning for 3 more minutes.

viii. Opening of the air injection valve and flotation for 3 minutes.

ix. Collecting of the flotation products, drying and weighing.

In the flotation tests, using EDTA as complexing agent of Mn2+ species, the MnCl2 dosage was fixed at 600g/ton and the conditioning was performed in the pulp natural pH (~7.5). Then, EDTA was added, which lowered the pulp pH for approximately 4.0 (depending on dosage added), and it was conditioned for 6 minutes. Subsequently, starch (400g/ton) and amine (50g/ton) were added, following the standard procedure, steps from iv to ix described previously.

3 Results and discussion

Figure 1 presents the mass recoveries and Fe metallurgical recoveries of flotation tests in function of MnCl2 dosages. Figure 2 presents the Fe and SiO2grades in the obtained concentrates in function of MnCl2 dosage.

Figure 1 Mass recovery and Fe metallurgical recovery vs MnCl2 dosages (400g/ton starch, 50g/ton amine, pH 10.5). 

Figure 2 Fe and SiO2 grades in the concentrates vs dosage of MnCl2 (400g/ton starch, 50g/ ton amine, pH 10.5). 

The mass recovery reached value around 75 % for the dosage of 2,400g/ton MnCl2. The Fe metallurgical recovery reached value of 96 %. It means an increase of little more than 10% for mass recovery and 6% for Fe metallurgical recovery compared to the test performed without Mn2+ ion (mass recovery = 62.6 %, Fe metallurgical recovery = 90.4 %). The increase in both mass recovery and Fe metallurgical recovery was more evident from 600 g/ton MnCl2. See Figure 1. These results are coherent with Lelis (2014), which verified decrease in recoveries in micro-flotation tests of hematite and quartz, carried out at pH 10.5 and 5 mg/L amine, with increase of MnCl2 dosage.

As can be observed in Figure 2, both Fe and SiO2 grades have almost the same values up 300 g/ton MnCl2. Only from 600 g/ton on, was there observed a decrease of Fe grades and increase in SiO2 grades in obtained concentrates.

In accordance with manganese diagram species (Fuerstenau, 1985), at pH 10.5, the concentrations of Mn2+ and MnOH+ are very low. The predominant specie is Mn(OH)2(s). At the maximum dosage of MnCl2 (2,400g/ton), a dark aspect of the pulp was observed. Duarte (2012) and Lelis (2014) also highlighted the formation of a brown precipitate, due to the Mn(OH)2(s) and MnO(OH)2(s) precipitation on the mineral surfaces, which was responsible for the decrease in their floatabilities, due the "slime coating" phenomenon. Thus, the increased mass recovery, observed in Figure 1 is related mainly to precipitation of the specie Mn(OH)2 on surfaces of quartz and iron minerals.

Figure 3 presents the mass recovery and Fe metallurgical recovery in function of EDTA dosage and Figure 4 presents the Fe and SiO2 grades in the obtained concentrates in function of EDTA dosage at fixed dosage of 600 g/ton MnCl2.

Figure 3 Mass recovery and Fe metallurgical recovery vs EDTA dosages (MnCl2600 g/ton, 400g/ton starch, 50g/ton amine, pH 10.5). 

Figure 4 Fe and SiO2 grades in the concentrates vs dosage of EDTA (MnCl2 600 g/ton, 400g/ ton starch, 50g/ton amine, pH 10.5). 

As can be observed in Figures 3 and 4, the metallurgical recoveries and grades of Fe were around 90% and 63%, respectively. The SiO2 grades in obtained concentrates remained in the range of 5% independent of EDTA dosage (in the absence of EDTA, the SiO2 grade was 7.5%). Such grades are within the range of commercial specifications required for sinter feed (~63.5% Fe, 4-6% SiO2) (Lima, 1997).

4 Conclusions

Based on results of cationic reverse flotation tests at pH 10.5, performed with an iron ore sample in the presence of manganese species, it is concluded that the presence of ions Mn2+ increased the mass recoveries, Fe metallurgical recoveries, SiO2 grades and decreased the Fe grades in obtained concentrate only from 600 g/ton MnCl2. With addition of EDTA at 600 g/ton MnCl2 before addition and conditioning with corn starch and amine, concentrates with greater Fe grade (~63.5%) and lower SiO2 grade (~5%) were obtained, which are close to the commercial specifications of pellet feed, generally lower than 5% SiO2 and higher than 60% Fe.

5. Acknowledgments

The authors would like to thank CNPq by financial support and a scholarship for one of the authors, CAPES for a scholarship for one of the authors, Samarco A.S. by iron ore sample supply, Clariant A. S. by amine reagent supply and DEGEO/UFOP by chemical and mineralogical analysis.

6. References

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ARAUJO, A. C. et alii. Reagents in iron ore flotation. Minerals Engineering v. 18, p. 219-224, 2005. [ Links ]

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DEPARTAMENTO NACIONAL DE PRODUÇÃO MINERAL. Sumário Mineral 2014. v. 34. p.1-25 e p. 72-73. Disponível em: http://www.dnpm.gov.br/dnpm/sumarios/sumario-mineral-2014 Acesso em: 12/03/2015. [ Links ]

DUARTE, R. S. Estudo da flotação de finos de minério de manganês sílico-carbonatado com amina,Ouro Preto: Escola de Minas, Universidade Federal de Ouro Preto 2012. 82 f. (Dissertação de Mestrado em Engenharia Mineral). [ Links ]

FILIPPOV, L. O. et alii. An overview of the beneficiation of iron ores via reverse cationic flotation. International Journal of Mineral Processing, v. 127, p. 62-69, 2014. [ Links ]

FUERSTENAU, M. C. et alii. Chemistry of Flotation. New York: Society of Mining Engineers of the American Institute of Mining, Metallurgical and Petroleum Engineers, Inc., p. 1985. 177 p. [ Links ]

HOUOT, R. Beneficiation of iron ore by flotation: review of industrial and potencial applications. International Journal of Mineral Processing , v. 10, p. 183-204, 1983. [ Links ]

LELIS, D. F. Influência de cátions polivalentes na flotação catiônica de minério de ferro: estudos fundamentaisOuro Preto: Escola de Minas, Universidade Federal de Ouro Preto, 2014. 88 f. (Dissertação de Mestrado em Engenharia Mineral). [ Links ]

LIMA, R. M. F. Adsorção de amido e amina sobre as superfícies da hematita e quartzo e sua influência na flotatção. Belo Horizonte: Escola de Engenharia, Universidade Federal de Minas Gerais, 1997. 238 f. (Tese de doutorado). [ Links ]

MA, X. et alii.. Comparative studies of reverse cationic/ anionic flotation of Vale iron ore. International Journal of Mineral Processing, v. 100, p.179-183, 2011. [ Links ]

PINHEIRO, V.S. et alii. Flotação com amina: a importância da qualidade da água. REM: R. Esc. Minas, Ouro Preto, v. 65, n. 4, p. 549-552, 2012. [ Links ]

Received: March 23, 2015; Accepted: May 15, 2015

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