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Iron: a versatile element to produce materials for environmental applications

Abstracts

Iron is a versatile element forming several phases with different oxidation states and structures, such as Feº, FeO, Fe3O4, γ-Fe2O3, α-Fe2O3 and FeOOH. All these phases have unique physicochemical properties which can be used for different applications. In this work, it is described the use of different iron compounds, synthetic and also from natural and waste sources, in environmental and technological applications. Two main research areas are described. The first one is related to strategies to increase the reactivity of Fe phases, mainly by the formation of Feº/iron oxide composites and by the introduction of new metals in the iron oxide structure to promote new surface reactions. The second area is the use of the magnetic properties of some iron phases to produce versatile magnetic materials with focus in adsorption, catalysis and emulsions.

iron; environmental applications; magnetite; composites


Ferro é um elemento versátil que forma várias fases com diferentes estados de oxidação e estruturas, tais como Feº, FeO, Fe3O4, γ-Fe2O3, α-Fe2O3 e FeOOH. Todas estas fases têm propriedades físico-químicas únicas que podem ser usadas para diferentes aplicações. Neste trabalho, descreve-se o uso de diferentes compostos de ferro, sintéticos e também naturais ou de rejeitos, em aplicações ambientais e tecnológicas. Duas áreas principais de pesquisa são descritas. A primeira é relacionada às estratégias para aumentar a reatividade de fases de ferro pela formação de compósitos Feº/Fe óxido e pela introdução de novos metais na estrutura de óxidos de ferro para promover novas reações superficiais. A segunda área de pesquisa é o uso das propriedades magnéticas de algumas fases de ferro para produzir materiais magnéticos versáteis com aplicações focadas em adsorção, catálise e emulsões.


Iron: a versatile element to produce materials for environmental applications

Ana Paula C. TeixeiraI,* * e-mail: rochel@ufmg.br, anapct@ufmg.br, juliana@ufv.br ; Juliana C. TristãoII,* * e-mail: rochel@ufmg.br, anapct@ufmg.br, juliana@ufv.br ; Maria H. AraujoI; Luiz C. A. OliveiraI; Flávia C. C. MouraI; José D. ArdissonIII; Camila C. AmorimIV; Rochel M. LagoI,* * e-mail: rochel@ufmg.br, anapct@ufmg.br, juliana@ufv.br

IDepartamento de Química, Universidade Federal de Minas Gerais, 31270-901 Belo Horizonte-MG, Brazil

IIUniversidade Federal de Viçosa, Rodovia LMG, 818, km 6, Campus Florestal, 35690-000 Florestal-MG, Brazil

IIILaboratório de Física Aplicada, Centro de Desenvolvimento da Tecnologia Nuclear, 30123-970 Belo Horizonte-MG, Brazil

IVDepartamento de Engenharia Sanitária e Ambiental, Universidade Federal de Minas Gerais, 31270-901 Belo Horizonte-MG, Brazil

ABSTRACT

Iron is a versatile element forming several phases with different oxidation states and structures, such as Feº, FeO, Fe3O4, γ-Fe2O3, α-Fe2O3 and FeOOH. All these phases have unique physicochemical properties which can be used for different applications. In this work, it is described the use of different iron compounds, synthetic and also from natural and waste sources, in environmental and technological applications. Two main research areas are described. The first one is related to strategies to increase the reactivity of Fe phases, mainly by the formation of Feº/iron oxide composites and by the introduction of new metals in the iron oxide structure to promote new surface reactions. The second area is the use of the magnetic properties of some iron phases to produce versatile magnetic materials with focus in adsorption, catalysis and emulsions.

Keywords: iron, environmental applications, magnetite, composites

RESUMO

Ferro é um elemento versátil que forma várias fases com diferentes estados de oxidação e estruturas, tais como Feº, FeO, Fe3O4, γ-Fe2O3, α-Fe2O3 e FeOOH. Todas estas fases têm propriedades físico-químicas únicas que podem ser usadas para diferentes aplicações. Neste trabalho, descreve-se o uso de diferentes compostos de ferro, sintéticos e também naturais ou de rejeitos, em aplicações ambientais e tecnológicas. Duas áreas principais de pesquisa são descritas. A primeira é relacionada às estratégias para aumentar a reatividade de fases de ferro pela formação de compósitos Feº/Fe óxido e pela introdução de novos metais na estrutura de óxidos de ferro para promover novas reações superficiais. A segunda área de pesquisa é o uso das propriedades magnéticas de algumas fases de ferro para produzir materiais magnéticos versáteis com aplicações focadas em adsorção, catálise e emulsões.

1. Introduction

Iron is a versatile element and can form several phases with different oxidation states and structures, such as Feº, FeO (wüstite), Fe3O4 (magnetite), γ-Fe2O3 (maghemite), α-Fe2O3 (hematite) and FeOOH (oxyhydroxy) (equation 1).

All these phases have unique physicochemical properties which can be used for a wide range of technological and environmental applications. Most of the important chemistry of these iron phases has been very well described in the classical book of Cornel and Schwertmann.1

Besides all the uses of Fe metal in the steel industry, zero valent iron has been extensively investigated for environmental remediation due to its reducing properties. Several contaminants such as organochloro compounds, nitrates, dyes, Cr(VI) and arsenic species can be treated by simple reduction with Feº.

Magnetite (Fe3O4) is an inverse spinel structured oxide with several important features for environmental applications, e.g., (i) it is magnetic, (ii) it contains Fe2+ in the structure which is an important electron donor, and (iii) the octahedral site in the magnetite structure can easily accommodate both Fe2+ and Fe3+, producing a very interesting redox chemistry within the solid structure (Figure 1). If the Fe2+ is completely oxidized, magnetite is converted to the magnetic maghemite (γ-Fe2O3) with the same spinel structure. At temperatures higher than 500 ºC, maghemite is converted to the hexagonal hematite (α-Fe2O3) with the loss of the magnetic properties. Also, different forms of iron oxy/hydroxyl FeO(OH) can be prepared such as goethite, lepidocrocite and akaganeite.


Other important features for the industrial and environmental application of iron compounds are the low cost, low toxicity and relatively good stability of the Fe phases. Iron is a very abundant element available in nature, mainly as magnetite (Fe3O4), maghemite (γ-Fe2O3) and hematite (α-Fe2O3). Other very interesting sources of iron are the wastes produced in large quantities by different industrial activities such as aluminum production (red mud), foundry (sand waste) and steel production.

In this account, it is described our efforts to use different iron compounds, e.g., synthetic and also from natural and waste sources, in environmental and technological applications. Two main research areas are described. The first one is related to strategies to increase the reactivity of Fe phases, mainly (i) by the formation of Feº/Fe oxide composites and (ii) by the introduction of new metals in the iron oxide structure to promote new surface reactions. The second area is the use of the magnetic properties of some iron phases to produce versatile magnetic composites with focus in adsorption, catalysis and emulsions.

2. Application of Iron Oxides and Metal for Waste Water Treatment

Use of iron phases and heterogeneous Fenton systems

The Fenton reagent, a mixture of Fe2+ and H2O2, is one of the most efficient systems to destroy organic contaminants in water. The efficiency of the Fenton reagent is due to the in situ generation of highly oxidative species, i.e., hydroxyl radicals, according to the simplified process (equation 2):

The Fenton reaction operates at an optimum pH of 3 and requires stoichiometric amounts of Fe2+. After the process, the effluent must be neutralized generating significant amounts of iron hydroxide sludge, which is an important drawback of the process due to disposal problems.2,3

Active heterogeneous Fenton systems, in which soluble Fe2+ does not precipitate since it is replaced by Fe-containing solids, show several very interesting advantages over the classical homogeneous reaction, such as operation at near neutral pH, no sludge formation and the possibility to recycle the iron promoter. Some of the irons containing solids that were investigated were goethite, hematite, clay minerals, iron hydroxide and iron supported on silica and on alumina.4-9 However, these iron promoters showed low activities or strong iron leaching due to low pH which produced mainly homogeneous reactions.

Our group has been investigating the use of the inverse spinel magnetite, Fe3O4, for the Fenton reaction due to its remarkable features, e.g., (i) it contains Fe2+ in the structure which should play an important role as an electron donor to initiate the Fenton process according to the classical Haber-Weiss mechanism (equation 2), and (ii) the octahedral site in the magnetite structure can easily accommodate both Fe2+ and Fe3+, producing a very dynamic redox chemistry within the solid structure.

The spinel structure also allows isostructural substitution of iron by different transition metals which can completely modify the physicochemical properties of the solid to produce more active systems. For example, the introduction on Mn and Co to produce Fe3-xMnxO4 and Fe3-xCoxO4 resulted in a remarkable increase in the activity for H2O2 decomposition and the oxidation of the organic molecules. The reaction apparently takes place via radical species generated by Fe2+, Co2+ and Mn2+ (Figure 2). The high activity has been discussed in terms of a thermodynamically favorable regenerative reduction of Co3+ and Mn3+ by Fe2+ by an electron transfer within the semiconductor oxide.11,12


Also, chromium was introduced in the magnetite structure to produce a Cr-Fe spinel active heterogeneous Fenton system. The presence of chromium also strongly increased the activity for the Fenton chemistry. It is proposed that this higher activity is related to the coupling of the redox pairs Fe3+/Fe2+ with Cr2+/Cr3+, which can regenerate the Fenton active specie Fe2+ more efficiently.11,12

The use of Feº to promote the Fenton reaction can be more efficient since the metal can potentially participate in the reaction with 3 e- whereas Fe2+ can donate only 1 e-. However, due to kinetic limitations, Feº alone is not active for the Fenton reaction at pH 7.13 Some of the works developed in our group showed that the combination of Feº with Fe3O4 by a metal-oxide interface produces very active Fenton systems. The understanding of these interface phenomena and the development of processes to increase the electron transfer rate from the iron compounds to the reaction medium is of great interest in order to improve the efficiency and to widen the application of these systems in environmental remediation processes.3 For example, the combination of Fe3O4 with Feº metal by simple mechanical grinding showed remarkable increase in the activity for the Fenton reaction.13 Transmission electron microscopy (TEM) studies showed the formation of a nanocomposite with evident interface between the Fe3O4 and Feº particles (Figure 3).


This result was discussed in terms of an electron transfer mechanism from Feº to Fe3+surf during the Fenton reaction to regenerate the Fe2+surf active species (Figure 4).13,14


The mechanistic details studied by electrospray ionization mass spectrometry (ESI-MS) confirmed the formation of OH radicals by the various hydroxylated intermediates.15

Reactive systems are also produced by the mechanical grinding and thermal treatment of Feº/α-Fe2O3 and Feº/γ-Fe2O3, however with much lower activity towards H2O2 compared with Feº/Fe3O4 mixtures.3

Iron metal was also mixed with perovskite (Feº/LaMnO3) and used as catalysts in the Fenton reaction.16,17 LaMnO3 can transfer oxygen to Feº by an interface reaction producing a partially reduced perovskite LaMnO3-δ and highly dispersed iron oxides, mainly Fe3O4, on the Feº surface (Figure 5). As the mixtures Feº/LaMnO3 are treated at 200, 400 and 600 ºC, the reactivity towards H2O2 decomposition decreases, whereas the activity for the oxidation of methylene blue increases. These results have been discussed in terms of a decrease on the concentration of Mn4+surf and Mn3+surf (active for H2O2 decomposition) with an increase on the Mn2+surf and Fe2+surf species, active for the Fenton reaction.


Use of iron phases for the reduction of Cr(VI) contaminants

The reduction of Cr(VI) to Cr(III) is a basic measure for groundwater remediation processes. Chromium(VI) compounds are contaminants of special concern due to carcinogenic and mutagenic activities.18 In the environment Cr(VI) comes most from industrial activities, e.g., in electroplating, leather tanning, pulp production, ore and petroleum refining processes, and from the high mobility of their oxyanions, e.g., CrO42- and Cr2O72- in water.19

Iron metal has been intensively investigated as Cr(VI) reducing agent.18,20,21 During this reaction, metallic iron is oxidized to Fe(III) while Cr(VI) is reduced to Cr(III), forming insoluble hydroxides. However, under environmental conditions, metallic iron shows a kinetic limitation with low reaction rates and rapid deactivation due to passivation of the metallic surface.22

Our group has found that Feº/Fe3O4 composites produced by simple grinding mixtures showed much higher efficiency to reduce Cr(VI) compared to the Fe and magnetite phases isolated.13,14,22-24 The reduction mechanism was discussed similar to the Fenton reaction, in which the Fe2+oct (magnetite) acts as a reducing site producing the oxidized Fe3+ and the reduced Cr species. The Fe3+oct can then be easily reduced back to Fe2+oct with no structural constraint by the thermodynamically favorable electron transfer from Feº via the metal-oxide interface (Figure 6).


Another approach to produce a more efficient system for the reduction of Cr(VI) was to create highly dispersed Fe phases on the surface of activated carbon.23 These Fe/AC composites show some innovative aspects: (i) the high surface area carbon support significantly increases the amount of reactive Fe-bearing chemical species, dispersed as very small particles, (ii) after deactivation, the oxidized iron in the composite can be regenerated by a simple thermal treatment in which Fe3+ species react with carbon to regenerate the reduced active phases Feº and Fe3O4 (Figure 7).


Another novel approach to produce reduced active Fe phases was to use tar, a well-known waste from the charcoal industry, for the reduction of Fe2O3.24 Upon thermal treatment, tar decomposes on the iron oxide Fe2O3 surface to produce elemental carbon, which readily reacts with Fe3+ to produce reduced Fe species (Figure 8).


After use and deactivation during Cr(VI) reduction, the oxidized iron in the composite can be easily regenerated by simple thermal treatment. In this treatment, Fe3+ species react with carbon to regenerate the initially active mixture of Feº and Fe3O4.

3. Application of Iron Phases to Produce Magnetic Materials as Adsorbents and Catalyst Support

Several iron phases such as Feº, Fe3O4 and γ-Fe2O3 (maghemite) show magnetic properties that can be used to produce magnetic materials. Some works in the literature have proposed the direct use of these iron phases as magnetic adsorbent for contaminants from aqueous or gaseous effluents.25-27 However, very low surface area or small adsorption capacities strongly limit their application. Some of the works in our group have been directed to prepare low cost efficient magnetic adsorbents by combining the adsorption properties of some materials with the magnetic properties of iron phases.

Activated carbon is an excellent adsorbent, especially for organic molecules and for some inorganic species. Activated carbon has high surface area and porous structure, high adsorption capacity and can be easily functionalized and used as an efficient adsorbent for heavy metal contaminants.28 The combination of magnetic iron phases with activated carbon offers an attractive and inexpensive option for the removal of different contaminants from water, such as pesticides, phenols and chlorophenols.29-32 Magnetic composites of activated carbon/iron oxide were prepared with several weight ratios of 2:1, 1.5:1 and 1:1 and used for the adsorption of volatile organic compounds (VOCs) such as chloroform, phenol, chlorobenzene and dyes from aqueous solution.29,30 The composites showed that the presence of the magnetic iron oxide did not affect the adsorption capacity of the activated carbon.

Natural clays are low-cost and readily available materials functioning as excellent cation exchangers, which have often been used to adsorb metallic contaminants. The adsorption capacity of clays results from a relatively high surface area and a net negative charge on their structure, which attracts and holds cations such as heavy metals. Bentonite-iron oxide magnetic composites have been produced by simple co-precipitation method and showed high adsorption capacities for the Ni2+, Cu2+, Cd2+ and Zn2+ in aqueous solution in the range 40-75 mmol of M2+ g-1 of composite.33

Expanded or exfoliated vermiculite clay is an extremely interesting material with low cost a highly developed porous structure. This exfoliated mineral has been reported in some studies as effective to remove spilled oil from the water surface due to the strong capillary action of the slit shaped pores.34,35 Magnetic composites based on expanded vermiculite and iron were combined to prepare floating materials on water, being used to remove spilled oil contaminants.36 These magnetic materials have been coated/hydrophobized with polymers such as epoxy resin and polystyrene improving their oil removal capacity (Figure 9).


These composites showed several advantages over the simply exfoliated vermiculite: (i) they are magnetic and can be removed from the application medium by a simple magnetic separation procedure, (ii) the hydrophobization produced a strong increase in the oil adsorption/absorption capacity, (iii) the hydrophobization strongly increased the chemical resistance of the composites towards very acidic medium, and (iv) the hydrophobization strongly improved the mechanical resistance of the vermiculite, avoiding the delamination process and resulting in a completely floatable composite.

Magnetic nanostructured composites based on carbon coated iron phases

Iron magnetic particles can be coated with a protective layer of different materials to improve their stability and to introduce new surface properties and functionalities. Carbon is a versatile coating material due to its chemical stability, biocompatibility, possibility of surface modification and pore creation. In general, carbon coating processes are relatively complex, demanding special precursors and producing relatively low yields.37,38

Our group has been investigating the production of carbon coating by a combined reduction/CVD (chemical vapor deposition) process in which iron is first reduced to form magnetic particles followed by carbon deposition. Different carbon sources such as CH4, C2H4 and CO have been investigated.39 The combined reduction/CVD process using methane and hematite is a versatile, technically simple and low cost method to produce carbon coated Fe3O4 particles.40,41 In this process, methane reduces Fe2O3 with very good selectivity to Fe3O4 magnetic nuclei and leads to an amorphous carbon deposition by a CVD reaction (Figure 10).


This technically simple method can use as precursor different iron containing materials, such as synthetic (Fe2O3, Fe3O4, FeOOH, etc.) and naturally occurring iron oxides or even iron containing wastes (e.g., red mud and mining waste).42

If ethanol is used as the reducing agent and carbon source, hematite is reduced to Fe metal and carbide and large amounts of carbon nanotubes (CNTs) are formed (Figure 11). These magnetic coated particles were used as adsorbent of organic compounds, e.g., methylene blue and chlorobenzene, and for the production of a magnetic recyclable supported Pd catalyst, as hydrogenation reactions (Figure 12).40-43



An innovative approach to produce magnetic nanoparticles based on iron cores encapsulated by a high surface area carbon was produced using Fe3+ ions and sucrose as a carbon source and reducing agent. In this process, first Fe3+ ions are solubilized in aqueous sucrose and upon thermal decomposition the iron is reduced to form magnetic particles surrounded by a nanometric layer of more organized graphitic carbon entrapped in an amorphous carbonaceous matrix (Figure 13).44 Studies of these materials as Pd catalysts support in hydrogenation reactions showed promising results with the full conversion of the substrate 1,5-COD (1,5-cyclooctadiene).


4. Use of Iron to Produce Amphiphilic Magnetic Nanostructured Particles

Amphiphilic synthesis

An important and innovative application of iron compounds developed in our group is on the production of amphiphilic composites.45-48 These amphiphilic materials are composed of a ceramic matrix (providing the hydrophilic surface) containing carbon nanostructures (responsible for the hydrophobic properties) and magnetic iron cores coated with carbon to produce the magnetic properties of the composite (Figure 14).


For the synthesis of these composites, a matrix containing Fe catalyst was submitted to CVD to grow carbon nanostructures, mainly nanofibers (NF) and nanotubes (NT).49,50

The control of the type and amount of carbon formed is important for the different envisaged applications of the composites. Our group has reported works using different ceramic matrices, such as alumina,51,52 vermiculite46,47,53,54 and chrysotile minerals46,48 magnesia55 and peroviskites.39,52

Microparticles of magnetic amphiphilic composites were produced from the clay vermiculite. The lamellar clay mineral was first fragmented to form microsheet fragments. The microsheets were then impregnated with iron nitrate and subjected to a CVD process to grow the carbon nanostructures46,47,53,54 (Figure 15).


Similar approach was used to prepare magnetic amphiphilic composites with the fibrous mineral chrysotile.46,48Figure 16 shows SEM images of a crysotile/carbon nanostructure/iron core composite.


Emsulsifier and demulfier

A very promising application for the amphiphilic materials is the formation and breaking of emulsions (Figure 17) with several potential uses in different industries, such as petrochemistry, biodiesel, vegetable oils and wastewater treatment.56-58 Due to the amphiphilic character of these materials, they act in the interface of the droplets. Figure 17 shows an optic microscopy image of an oil-water emulsion stabilized by amphiphilic magnetic material.


Our group has reported the utilization of magnetic amphiphilic composites in different steps of biodiesel production.46 For example, in the transesterification reaction to produce biodiesel, oils do not mix with the alkali/methanol phase and a vigorous stirring to promote a good interface is necessary for the reaction to take place.59 When the amphiphilic composites were added to these biphasic systems, an emulsion was formed and due to the excellent interface, an efficient transesterification took place.46

After transesterification, the biodiesel is emulsified with a more polar phase reaction formed by water, glycerol and the excess methanol. Due to the magnetic properties of the amphiphilic composites, they can be dragged towards an external applied magnetic field.

This magnetic process destabilizes the emulsion leading to a rapid phase separation schematically represented in Figure 18. Furthermore, amphiphilic materials have also proved effective to break the emulsion formed during washing and the wastewater from the production of biodiesel.48


Adsorption of hazardous large hydrophobic contaminant molecules

Amphiphilic materials can be used as a highly efficient adsorbent for hazardous organic contaminant molecules in wastewaters such as endocrinous disruptor. The carbon nanostructures (nanotubes and nanofibers (CNF)) of the amphiphilic materials supported on the inorganic surface are very efficient for the adsorption of these hydrophobic organic molecules. Our group showed that the composite formed by the inorganic support vermiculite, carbon nanostructures and magnetic iron particles were effective for the adsorption of the hormone ethinylestradiol in water.47 Due to the presence of the inorganic support, the composite disperses very well in water while keeping the CNT and CNF separated (avoiding agglomeration). This exposed carbon surface area is very efficient for the adsorption of the hormone (Figure 19). Furthermore, the presence of magnetic iron phases allows a facile magnetic separation of the composite from the medium after adsorption.


5. Catalytic Applications of Iron Based Materials

Iron phases can be used as catalysts for different reactions, especially oxidations of contaminants such as CO,60β-pinene61 and toluene.62,63 Magnetite showed a high activity for the oxidation of carbon monoxide at lower temperatures, being related to the presence of surface Fe2+ species capable of activating gas phase O2 to form more reactive species.64,65

Magnetite doped with Mn or Co, Fe3-xMxO4 (M = Mn, Co; x = 0-0.75) was also used as catalyst to high selective oxidation of β-pinene, a renewable monoterpene, under solvent free conditions. The pinene is oxidized with O2 with high selectivity to special products for the perfume and flavor industries.61

The introduction of Fe in the LaMnO3 structure produced oxidation catalysts with improved properties. The presence of small amounts of Fe in the perovskite structure led to an increase of the catalytic activity for the oxidation of VOCs such as methane and toluene. The improvement of the catalytic activity was discussed in terms of the effect of Fe on the creation of surface and structural defects which can increase the perovskite reactivity towards oxygen.63,65

Iron was also used as catalyst associated with materials such as clays. The pillared clay montmorillonite containing highly dispersed iron oxide showed very good activity and stability for the oxidation of toluene.62

6. Fuel Storage

Hydrogen is considered the most promising fuel to replace fossil energy sources.66 However, the large-scale use of H2 faces two main challenges: the production and storage.67 The main production methods that have been studied are electrolysis,68 thermolysis,69 water photolysis,70 biological process71 and reforming of methane or alcohols.72 The use of ethanol for the production of hydrogen has been considered an interesting route since ethanol is a renewable fuel, easy to transport with low toxicity.73 Our group has developed a new concept based on a redox cycle for H2 production and storage using ethanol and iron compounds. This process occurs in two steps. First, ethanol reduces the iron ion phases to iron metal. Second, H2 is produced by the oxidation of the iron metal with water. An advantage of this process is the indirect storage of hydrogen. The iron metal obtained in the first part of the cycle can be stored and transported to produce H2 wherever it is necessary by a reaction with H2O (Figure 20).


Different iron compounds were studied, e.g., NixFe3-xO4 ferrites,74 goethite, hematite and magnetite,75 and Fe2O3 supported in SiO2 or Al2O3.76 All iron based system showed promising results for H2 storage.

7. Use of Iron Containing Wastes for Environmental Applications

Several industries produce large amounts of Fe rich wastes such red mud (RM, produced in the Bayer process), foundry sand, kaolin mining and blast furnace dust waste from the steel industry.75 The Fe present in these wastes in relatively high concentrations can be used for several environmental applications as described in some of the work carried out in our group (Figure 21).


RM is an iron rich waste of the Al2O3 extraction by the Bayer process. It is mainly composed of Fe2O3 (ca. 20-30 wt.%), Al2O3, CaO, SiO2 and TiO2.76 Red mud can be reduced by H2 to produce different iron phases from Fe3O4, Fe3O4/Feº to pure Feº. The other oxides present in RM, such as Al2O3 and SiO2, are thermally stable and act as support to disperse the iron phases improving their reactivity. The obtained materials showed very good results for the oxidation of organic contaminants in water using H2O2 in a Fenton like reaction.77 These composites also showed good activity for Cr(VI) reduction.77 Red mud can also be used for the upgrading of bio-oil which involves mainly deoxygenation reactions promoted by reduced iron species.78

Waste foundry sand (WFS) contains silica sand, clay binder, carbon and iron mainly present as oxide and metal. The texture and granulometry of WFS make it a suitable candidate to produce reactive permeable barriers.79

WFS and blast furnace dust are not active for environmental processes. However, after a simple thermal treatment, these wastes strongly increased the activity for different reactions, such as Fenton oxidation and Cr(VI) reduction.80

These results were discussed in terms of reactions of the carbon present in the waste to reduce the different iron species to form active reducing iron phases (equation 3).

Kaolin is a material extensively used in the paper industry. The kaolin mining produces large amounts of a waste composed of TiO2 phases, Fe oxides/oxyhydroxides and quartz. The controlled reduction of the kaolin waste with H2 at 400 ºC produced efficient systems for the oxidation of different contaminants with aqueous H2O2 and also for the Cr(VI) reduction.81

RM can also be used as catalyst for the CVD synthesis of the carbon nanostructures from ethanol as carbon source. Figure 22 shows carbon nanostructures and iron cores obtained after CVD synthesis with RM.


The obtained magnetic composites showed very good results as adsorbent for dyes in aqueous medium and as support to produce greener recyclable magnetic Pd catalyst using the model reaction of 1,5-cyclooctadiene hydrogenation.

8. Conclusions

Iron is very versatile element. It can be reversibly transformed in different phases with remarkable physicochemical properties and many potential technological applications. Figure 23 shows some possible applications of iron phases. The controlled reduction of different Fe sources, Fe2+, Fe3+, iron oxides and hydroxides and iron rich wastes and natural sources produces Fe3O4, Feº and Feº/Fe3O4 composites (Figure 23). The inverse spinel Fe3O4 is magnetic and can be combined with different materials to produce magnetic adsorbents. It can also be used as catalyst, especially when Fe is replaced in the structure by other metals such as Co, Mn and Cr. The composites Feº/Fe3O4 showed remarkable activity as electron transfer systems which can be used in many environmental applications such as the Fenton reaction and Cr(VI) reduction. Fe metal can be used for H2 and fossil fuel storage carbon nanotubes and nanofiber growth to produce magnetic composites with application as adsorbent, catalyst support and amphiphilic materials for emulsions.


Acknowledgements

The authors thank Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq), Fundação de Amparo à Pesquisa do estado de Minas Gerais (FAPEMIG), Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES), PRPq-UFMG and Centro de Microscopia (UFMG).

Submitted: August 22, 2012

Published online: September 21, 2012

Ana Paula de Carvalho Teixeira is graduated in Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) and obtained her MSc degree at Centro de Desenvolvimento da Tecnologia Nuclear (Minas Gerais State, Brazil). She obtained her PhD at UFMG working on the preparation of amphiphilic magnetic composites and carbon nanotubes for application in synthesis, catalysis and environmental processes.

Juliana Cristina Tristão is graduated and obtained her PhD in Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil). She is currently a professor at Universidade Federal de Viçosa (UFV Minas Gerais State, Brazil) developing research on the synthesis and application of magnetic particles based on iron and carbon nanostructures for application in environmental processes and heterogeneous catalysis.

Maria Helena Araujo obtained her MSc under the supervision of Prof Maria D. Vargas at Universidade de Campinas (UNICAMP, São Paulo State, Brazil) in 1990 and the PhD in 1995 at UNICAMP and Sussex University (United Kingdon) under the supervision of Prof Maria D. Vargas and John F. Nixon. This was followed by a research fellow position at Sussex University from 1996-1997 and a Postdoctoral position at UNICAMP from 1998-1999, working always with organometallic chemistry. Since 2000 she is working at Department of Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) on environmental chemistry and catalysis. She is currently working with magnetic nanoparticles covered with carbon and ionic liquids for catalysis.

Luiz Carlos A. Oliveira has graduated in Chemistry, BSc (1997), Master in Physical Chemistry (2000) and PhD in Inorganic Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) and Post doctorate at University of California (USA, 2009). He is currently an adjunct professor at UFMG and member of the Advisory Board of the CEX-Fapemig. He operates in environmental chemistry, on the following subjects: activated charcoal, iron oxide, catalysis, adsorption and contaminants. He was a fellow of Productivity and Technological Development Innovative Extension.

Flávia Cristina Camilo Moura has graduated and obtained her PhD in Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) In 2005 she spent one year at University of Montreal (Canada) under the supervision of Prof Richard Martel working with carbon nanotubes. Since 2009 she works at Department of Chemistry (UFMG) developing research on heterogeneous catalysis and adsorbents with environmental applications.

José Domingos Ardisson has graduated in Physics at Universidade Federal do Espírito Santo (Espírito Santo State, Brazil) in 1982 and MSc and PhD in Physics at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) (1995). Since 1998 he is a researcher at the Applied Physics Laboratory, Nuclear Technology Development Center (CDTN/CNEN Minas Gerais State, Brazil).

Camila Costa de Amorim graduated in Environmental Engineering at Universidade Federal de Viçosa (UFV, Minas Gerais State, Brazil) has PhD in Sanitation, Environment and Water Resources at Universidade Federal de Minas Gerais (Minas Gerais State). She is currently Adjunct Professor in the Department of Sanitary and Environmental Engineering in UFMG, developing research on wastewater treatment technologies and industrial waste reuse, with emphasis in advanced oxidative process and developing of the iron oxides catalysts for environmental applications.

Rochel Montero Lago is graduated at Universidade de Campinas (UNICAMP, São Paulo State, Brazil) with MSc under the supervision of Prof Ulf Schuchardt. In 1992, he spent one year at Gifu University (Japan) followed by a PhD at Oxford University (United Kingdom) under the supervision of Prof M. L. H. Green and a Pos-Doc with Prof J. L. G Fierro at Institute of Catalysis and Petrochemistry (Madrid, Spain) working always in the area of catalysis. In 2005, he went to University of Montreal (Canada) as a Visiting Researcher at the laboratories of Prof Richard Martel to work with carbon nanotubes and a Pos-Doc at the business school HEC (Heutes Etudes Commerciales, Canada) with Prof L. J. Filion on the theme technological entrepreneurship. He works at Department of Chemistry at Universidade Federal de Minas Gerais (UFMG, Minas Gerais State, Brazil) since 1997.

  • 1. Cornell R. W.; Schwertmann, U.; The Iron Oxides, 1st; Wiley-VCH: New York, 1996.
  • 2. Lemley, A. T.; Wang, Q.; Saltmiras, D. A. In Pesticide Decontamination and Detoxification, ACS Symposium Series, No. 863; Gan, J. J.; Zhu, P. C.; Aust, S. D.; Lemley, A. T., eds.; Oxford University Press: USA, 2003, p. 65-83.
  • 3. Moura, F. C. C.; Oliveira, G. C.; Araujo, M. H.; Ardisson, J. D.; Macedo, W. A. A.; Lago, R. M.; Appl. Catal., A 2006,307,195.
  • 4. Huang, H. H.; Lu, M.C.; Chen, J. N.; Water Res. 2001,35,2291.
  • 5. Centi, G.; Perathoner, S.; Torre, T.; Verduna, M. G.; Catal. Today 2000,55,61.
  • 6. Kwan, W. P.; Voelker, B. M.; Environ. Sci. Technol 2003,37,1150.
  • 7. Kwan, W. P.; Voelker, B. M.; Environ. Sci. Technol. 2002,36,1467.
  • 8. Chou, S.; Huang, C.; Chemosphere 1999,38,2719.
  • 9. Feng, J.; Hu, X.; Yue, H. Y.; Zhu, Y.; Lu, G. Q.; Water Res. 2003,37,3776.
  • 10. Friák, M.; Schindlmayr, A.; Scheffler, M.; New J. Phys. 2007,9,5.
  • 11. Costa, R. C. C.; Lelis, M. F. F.; Oliveira, L. C. A.; Fabris, J. D.; Ardisson, J. D.; Rios, R. R. V. A.; Silva, C. N.; Lago, R. M.; Catal. Commun. 2003,4,525.
  • 12. Costa, R. C. C.; Lelis, M. F. F.; Oliveira, L. C. A.; Fabris, J. D.; Ardisson, J. D.; Rios, R. R. V. A.; Silva, C. N.; Lago, R. M.; J. Hazard. Mater. 2006,B129,171.
  • 13. Costa, R. C. C.; Moura, F. C. C.; Ardisson, J. D.; Fabris, J. D.; Lago, R. M.; Appl. Catal., B Environ. 2008,83,131.
  • 14. Coelho, F.; Ardison, J. D.; Moura, F. C. C.; Lago, R. M.; Murad, E.; Fabris, J. D.; Chemosphere 2008,71,90.
  • 15. Moura, F. C. C.; Araujo, M. H.; Costa, R. C. C.; Fabris, J. D.; Ardisson, J. D.; Macedo, W. A. A.; Lago, R. M.; Chemosphere 2005,60,1118.
  • 16. Moura, F. C. C.; Araujo, M. H.; Dalmázio, I.; Alves, T. M. A.; Santos, L. S.; Eberlin, M. N.; Augusti, Rodinei ; Lago, R. M.; Rapid Commun. Mass Spectrom. 2006,20,1859.
  • 17. Magalhães, F.; Moura, F. C. C.; Ardisson, J. D.; Lago, R. M.; Mater. Res. 2008,11,307.
  • 18. Moura, F. C. C.; Araújo, M. H.; Ardisson, J. D.; Macedo, W. A. A.; Albuquerque, A. S.; Lago, R. M.; J. Braz. Chem. Soc. 2007,18,322.
  • 19. Callao, M. P.; Gómes, V.; TrAC, Trends Anal. Chem 2006,25,1006.
  • 20. Park, J. M.; Park, D.; Yun, Y. S.; J. Colloid Interface Sci. 2008,317,54.
  • 21. Fendorf, S.; Ginder-Vogel, M.; Borch, T.; Mayes, M. A.; Jardine, P. M.; Environ. Sci. Technol. 2005,39,7833.
  • 22. Lee, D. Y.; Yu, P. F.; Juang, K. W.; Plant Soil 2004,258,333.
  • 23. Pereira, M. C.; Coelho, F. S.; Nascentes, C. C.; Fabris, J. D.; Araújo, M. H.; Sapag, K.; Oliveira, L. C. A.; Lago, R. M.; Chemosphere 2010,81,7.
  • 24. Magalhães, F.; Pereira, M. C.; Fabris, J. D.; Bottrel, S. E. C.; Sansiviero, M. T. C.; Amaya, A.; Tancredi, N.; Lago, R. M.; J. Hazard. Mater. 2009,165,1016.
  • 25. Booker, N. A.; Keir, D.; Priestley, A.; Rithchie, C. D.; Sudarmana, D. L.; Woods, M. A.; Water Sci. Technol. 1991,23,1703.
  • 26. Safarik, I.; Safarikova, M.; Buricova, V.; Collect. Czech. Chem. Commun. 1995,60,1448.
  • 27. Orbell, J. D.; Godhino, L.; Bigger, S. W.; Nguyen, T. M.; Ngeh, L. N.; J. Chem. Educ. 1997,74,1446.
  • 28. Shim, J. W.; Park, S. J.; Ryu, S. K.; Carbon 2001,39,1635.
  • 29. Oliveira, L. C. A.; Rios, R. V. R. A.; Fabris, J. D.; Garg, V.; Sapag, K.; Lago, R. M.; Carbon 2002,40,2177.
  • 30. Oliveira, L. C. A.; Rios, R. V. R. A.; Fabris, J. D.; Lago, R. M.; Sapag, K.; J. Chem. Educ. 2004,81,248.
  • 31. Pignon, H.; Brasquet, C.; La Cloirec, P.; Water Sci. Technol. 2000,42,355.
  • 32. Lua, A. C.; Guo, J.; J. Environ. Eng. 2001,127,889.
  • 33. Oliveira, L. C. A.; Rios, R. V. R. A.; Fabris, J. D.; Sapag, K.; Garg, V. K.; Lago, R. M.; Appl. Clay Sci. 2003,22,169.
  • 34. Martins, J.; Br 39004025, 1990
  • 35. Machado, L. C. R.; Torchia, C. B.; Lago, R. M.; Catal. Comum. 2006,7,538.
  • 36. Machado, L. C. R.; Lima, F. W. J.; Paniago, R.; Ardison, J. D.; Sapag, K.; Lago, R. M.; Appl. Clay Sci. 2006,31,207.
  • 37. Zhao, X. L.; Shi, Y. L.; Wang, T.; Cai, Y. Q.; Jiang, G. B.; J. Chromatogr., A 2008,1188,140.
  • 38. Lee, J.; Lee, Y.; Youn, J. K.; Bin Na, H.; Yu, T.; Kim, H.; Lee, S. M.; Koo, Y. M.; Kwak, J. H.; Park, H. G.; Chang, H. N.; Hwang, M.; Park, J. G.; Kim, J.; Hyeon, T.; Small 2008,4,143.
  • 39. Moura, F. C. C.; Tristão, J. C.; Lago, R. M.; Martel, R.; Catal. Today 2008,133,846.
  • 40. Tristão, J. C.; Oliveira, A. A. S.; Ardisson, J. D.; Dias, A.; Lago, R. M.; Mater. Res. Bull. 2011,46,748.
  • 41. Tristão, J. C.; Silva, A. A.; Ardisson, J. D.; Lago, R. M.; Hyperfine Interact. 2010,195,21.
  • 42. Oliveira, A. A. S.; Tristão, J. C.; Ardisson, J. D.; Dias, A.; Lago, R. M.; Appl. Catal., B 2011,105,163.
  • 43. Tristão, J. C.; Ardisson, J. D.; Sansiviero, M. T. C.; Lago, R. M.; Hyperfine Interact. 2010,195,15.
  • 44. Mendonça, F. G.; Ardisson, J. D.; Rosmaninho, M. G.; Lago, R. M.; Tristão, J. C.; Hyperfine Interact. 2011,202,123.
  • 45. Oliveira, A. S.; Teixeira, F. T.; Ribeiro, L. P.; Tristão, J. C.; Dias, A. D.; Lago, R. M.; J. Braz. Chem. Soc 2010,21,2184.
  • 46. Teixeira, A. P. C.; Purceno, A. D.; Barros, A. S.; Lemos, B. R. S.; Ardisson, J. D.; Macedo, W. A. A.; Nassor, E. C. O.; Amorim, C. C.; Moura, F. C. C.; Hernández-Terrones, M. G.; Portela, F. M.; Lago, R. M.; Catal. Today 2012,190,133.
  • 47. Purceno, A. D.; Teixeira, A, P. C.; de Souza, N. J.; Fernandez-Outon, L. E.; Ardisson, J. D.; Lago, R. M.; J. Colloid Interface Sci 2012,379,84.
  • 48. Lemos, B. R. S.; Teixeira, A. P. C.; Ardisson, J. D.; Macedo, W. A. A.; Fernandez-Outon, L. E.; Amorim, C. C.; Moura, F. C. C.; Lago, R. M.; Appl. Sci. 2012,2,513.
  • 49. Oncel, C.; Yurum, Y.; Fullerenes, Nanotubes, Carbon Nanostruct 2006,14,17.
  • 50. Dupuis, A. C.; Prog. Mater. Sci 2005,50,929.
  • 51. Oliveira, P. F.; Ribeiro, L. P.; Rosmaninho, M. G.; Ardisson, J. D.; Dias, A.; Lago, R. M.; Hyperfine Interact 2011,203,67.
  • 52. Tristão, J. C.; Moura, F. C. C.; Lago, R. M.; Sapag, K.; Quim. Nova 2010,33,1379.
  • 53. Moura, F. C. C.; Lago, R. M.; Appl. Catal., B 2009,90,436.
  • 54. Purceno, A. D.; Barrioni, B. R.; Dias, A.; Costa, G. M.; Lago, R. M.; Moura, F. C. C.; Appl. Clay Sci 2011,54,15.
  • 55. Teixeira, A. P. C.; Lemos, B. R. S.; Magalhães, L. A.; Ardisson, J. D.; Lago, R. M.; Furtado, C. A.; Santos, A. P.; J. Nanosci. Nanotechnol 2012,12,2661.
  • 56. Barros, F. F. C.; Quadros, C. P.; Maróstica Jr., M. R.; Pastore, G. M.; Quim. Nova 2007,30,409.
  • 57. Al-Sabagh, A. M.; Maysour, N. E.; NoorEl-Din, M. R.; J. Dispersion Sci. Technol. 2007,28,547.
  • 58. Oliveira, A. G.; Scarpa, M. V.; Correa, M. A.; Cera, L. F. R.; Formariz, T. P.; Quim. Nova 2004,27,131.
  • 59. Sharma, Y. C.; Singh, B.; Korstad, J.; Fuel 2011,90,1309.
  • 60. Oliveira, L. C. A.; Fabris, J. D.; Rios, R. R. V. A.; Mussel, W. N.; Lago, R. M.; Appl. Catal., A 2004,259,253.
  • 61. Menini, L.; da Silva, M. C.; Lelis, M. F. F.; Fabris, J. D.; Lago, R. M.; Gusevskaya, E. V.; Appl. Catal., A 2004,269,117.
  • 62. Nogueira, F. G. E.; Lopes, J. H.; Silva, A. C.; Lago, R. M.; Fabris, J. D.; Oliveira, L. C. A.; Appl. Clay Sci 2011,51,385.
  • 63. Tristão, J. C.; Ardisson, J. D.; Macedo, W. A. A.; Lago, R. M.; Moura, F. C. C.; J. Braz. Chem. Soc. 2007,18,1524.
  • 64. Lelis, M. F. F.; Rios, R. V. R. A.; Lago, R. M.; Fabris, J. D.; Mussel, W. N.; Macedo, W. A. A.; Martins, M. D.; Hyperfine Interact 2002,5,345.
  • 65. Rosmaninho, M. G.; Tristão, J. C.; Moura, F. C. C.; Lago, R. M.; Araujo, M. H.; Anal. Bioanal. Chem. 2010,396,2785.
  • 66. Navarro, R. M.; Alvarez-Galvan, M. C.; Villoria, J. A.; Al-Zahrani, S. M.; Fierro, J. L. G.; Energy Environ. Sci. 2010,3,1865.
  • 67. Wendt, W.; Götz, M.; Linardi, M.; Quim. Nova 2000,23,538.
  • 68. Sigurvinsson, J.; Mansilla, C.; Lovera, P.; Werkoff, F.; Int. J. Hydrogen Energy 2007,32,1174.
  • 69. Steinfeld, A.; Sol. Energy 2005,78,603.
  • 70. Yan, J. H.; Zhu, Y. R.; Tang, Y. G.; Zheng, S. Q.; J. Alloys Compd. 2009,472,429.
  • 71. Levin, D. B.; Chahine, R.; Int. J. Hydrogen Energy 2010,35,4962.
  • 72. Armos, J. N.; Catal. Lett. 2005,101,131.
  • 73. Hotza, D.; da Costa, J. C. D.; Int. J. Hydrogen. Energy 2008,33,4915.
  • 74. Rosmaninho, M. G.; Herreras, S.; Lago, R. M.; Araujo, M. H.; Navarro, R. M.; Fierro, J. L. G.; Nanosci. Nanotechnol. Lett. 2011,3,705.
  • 75. Rosmaninho, M. G.; Moura, F. C. C.; Souza, L. R.; Nogueira, R. K.; Gomes, G. M.; Nascimento, J. S.; Pereira, M. C.; Fabris, J. D.; Ardisson, J. D.; Nazarro, M. S.; Sapag, K.; Araujo, M. H.; Lago, R. M.; Appl. Catal., B 2012,115,45.
  • 76. Rosmaninho, M. G.; Souza, L. R.; Gomes, G. M.; Zica, R. F.; Nascimento, J. S.; Pereira, M. C.; Fabris, J. D.; Ardisson, J. D.; Moura, F. C. C.; Lago, R. M.; Araujo, M. H.; Hyperfine Interact 2010,195,49.
  • 75. Dungan, R.; Dees, N.; Water Air Soil Pollut 2007,183,213.
  • 76. Power, G.; Grafe, M.; Klauber, C.; Hydrometallurgy 2011,108,33.
  • 77. Costa, R. C. C.; Moura, F. C. C.; Oliveira, P. E. F.; Magalhaes, F.; Ardisson, J. D.; Lago, R. M.; Chemosphere 2010,78,1116.
  • 78. Karimi, E.; Teixeira, I. F.; Ribeiro, L. P.; Gomez, A.; Lago, R. M.; Penner, G.; Kycia, S. W.; Schlaf, M.; Catal. Today 2012,190,73.
  • 79. Oliveira, P. E. F.; Oliveira, L. D.; Ardisson, J. D.; Lago, R. M.; J. Hazard. Mater. 2011,194,393.
  • 80. Amorim, C. C.; Dutra, P. R.; Pereira, M. C.; Fabris, J. D.; Lago, R. M.; Chem. Eng. J. 2012,in press, DOI: 2012.08.023.
  • 81. Pereira, M. C.; Tavares, C. M.; Fabris, J. D.; Lago, R. M.; Murad, E.; Criscuolo, P. S.; Clay Miner 2007,42,299.
  • *
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  • Publication Dates

    • Publication in this collection
      02 Oct 2012
    • Date of issue
      Sept 2012

    History

    • Received
      22 Aug 2012
    • Accepted
      21 Sept 2012
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