<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">JSEMAT</journal-id><journal-title-group><journal-title>Journal of Surface Engineered Materials and Advanced Technology</journal-title></journal-title-group><issn pub-type="epub">2161-4881</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jsemat.2018.81001</article-id><article-id pub-id-type="publisher-id">JSEMAT-80759</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Chemistry&amp;Materials Science</subject><subject> Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  The Role of Metal-Doped into Magnetite Catalysts for the Photo-Fenton Degradation of Organic Pollutants
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Xuan</surname><given-names>Sang Nguyen</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Kim</surname><given-names>Dinh Ngo</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Environmental Institute, Vietnam Maritime University, Hai Phong, Vietnam</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>sangnx.vmt@vimaru.edu.vn(XSN)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>30</day><month>11</month><year>2017</year></pub-date><volume>08</volume><issue>01</issue><fpage>1</fpage><lpage>14</lpage><history><date date-type="received"><day>19,</day>	<month>October</month>	<year>2017</year></date><date date-type="rev-recd"><day>27,</day>	<month>November</month>	<year>2017</year>	</date><date date-type="accepted"><day>30,</day>	<month>November</month>	<year>2017</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  Recently, the incorporation of transition metals into magnetite increasing the heterogeneous Fenton catalytic activity of magnetite with high efficiency and interesting magnetic properties applied for degradation of organic pollutants in water purification and wastewater treatment have attracted more and more researchers. In this review, using of one or some metal doped magnetite based systems in heterogeneous Fenton, or photo-Fenton processes are discussed. Then, the role of metal doped species for the enhanced efficiency of degradation process is presented. Finally, possible reaction mechanism for the photo-Fenton degradation pollutants in the present of metal doped magnetite is also given.
 
</p></abstract><kwd-group><kwd>Transition Doped Metal</kwd><kwd> Metal Doped Magnetite</kwd><kwd> Photo-Fenton</kwd><kwd> Role of Doped Metal</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>The rapid global economic growth has resulted in clean water crisis and environmental pollution since industrial revolution. Literature indicates an increasing trend in generation of wastewaters with recalcitrant characteristics from the many activities of industrial societies [<xref ref-type="bibr" rid="scirp.80759-ref1">1</xref>] . A large number of these pollutants are toxic in nature even at micro quantities [<xref ref-type="bibr" rid="scirp.80759-ref2">2</xref>] . Wastewaters containing these compounds are known to be high in chemical oxygen demand (COD) and low in biological oxygen demand (BOD). These non-biodegradable molecules enter the environment predominantly from mainly industrial activities [<xref ref-type="bibr" rid="scirp.80759-ref3">3</xref>] .</p><p>Currently, there are various of methods to deal with these issues such as: bio-method, chemical-physical method and so on. However, traditional biological methods can effectively treat wastewaters with high biodegradability ratio (BOD<sub>5</sub>/COD ≥ 0.4). In many industries, conventional treatment technologies cannot even produce effluents that meet water quality criteria and effluent limitation guidelines for recalcitrant pollutants [<xref ref-type="bibr" rid="scirp.80759-ref4">4</xref>] . In addition, traditional treatment techniques only succeed in contaminants transfer from liquid phase to solid phase which can cause second pollution. To effectively treat recalcitrant effluent, the scope should encompass degradation as well as mineralization of organic contaminants. That is conversion of probe molecule to its highest stable oxidation state: water, carbon dioxide, and the oxidized inorganic anions of any heteroatoms present, mainly to inorganic acids; or to more easily degradable molecules, that can be easily removed biologically.</p><p>Accordingly, advanced oxidation processes (AOPs) are considered as powerful methods for degradation of these pollutants due to their ability for removing almost any organic contaminant [<xref ref-type="bibr" rid="scirp.80759-ref5">5</xref>] . AOPs are considered as water treatment processes at near ambient temperature and pressure that produce very active radicals for degradation of pollutants [<xref ref-type="bibr" rid="scirp.80759-ref6">6</xref>] . In water/wastewater treatment, AOPs generally refer to a group of processes that cover O<sub>3</sub> and H<sub>2</sub>O<sub>2</sub> as oxidants with assistance of light, catalyst (e.g. Fe<sup>2+</sup>, Fe<sup>3+</sup> and TiO<sub>2</sub>), ultrasonic insertion and/or thermal input and there are several combinations such as Fenton (H<sub>2</sub>O<sub>2</sub>/Fe<sup>2+</sup>), photo-Fenton (H<sub>2</sub>O<sub>2</sub>/UV/Fe<sup>2+</sup>), peroxidation combined with Ultraviolet light (H<sub>2</sub>O<sub>2</sub>/UV), Peroxone (O<sub>3</sub>/H<sub>2</sub>O<sub>2</sub>). These oxidation processes are cost effective technologies and give rise to non-selective active species that oxidize a wide variety of non-biodegradable compounds [<xref ref-type="bibr" rid="scirp.80759-ref7">7</xref>] . AOPs have been used at various scales for overall organic content (COD) reduction, specific pollutant destruction, sludge treatment, increase of bioavailability of recalcitrant organics, destruction of micropollutants and color and odour removal [<xref ref-type="bibr" rid="scirp.80759-ref8">8</xref>] [<xref ref-type="bibr" rid="scirp.80759-ref9">9</xref>] . However, there are some disadvantages for the application of the traditional homogeneous Fenton and photo-Fenton process, including the requirement of low pH, a significant amount of ferric hydroxide sludge formed in the course of homogeneous Fenton treatment, high leaching ion iron in solution and difficult to separate catalyst after reaction [<xref ref-type="bibr" rid="scirp.80759-ref10">10</xref>] . The heterogeneous photo-Fenton reaction can solve the problem of eliminating and reusing e from the reaction system at the end of the process, but the separation of the solid phase is still a remaining issue [<xref ref-type="bibr" rid="scirp.80759-ref11">11</xref>] . The separation problem is even more important in the case of oxide nanoparticles, which are potentially more reactive because of the favorable surface-to-volume ratio. From this point of view, the fact that magnetite undergoes very easy magnetic separation from aqueous systems makes it a very interesting material to be tested for photo-Fenton reactivity. Recent studies demonstrate that magnetite is the most effective heterogeneous Fenton, photo-Fenton catalyst as compared to other iron oxides, possibly because it is the only one that has Fe<sup>2+</sup> in its structure to enhance the production rate of OH radical [<xref ref-type="bibr" rid="scirp.80759-ref12">12</xref>] . Moreover, its interesting magnetism leads it easy to be separated from the reaction system [<xref ref-type="bibr" rid="scirp.80759-ref13">13</xref>] . More recently, it is reported that the introduction of Mn, Zn, Ni [<xref ref-type="bibr" rid="scirp.80759-ref14">14</xref>] , Cr [<xref ref-type="bibr" rid="scirp.80759-ref15">15</xref>] , Ti [<xref ref-type="bibr" rid="scirp.80759-ref16">16</xref>] into magnetite structure may strongly promote the Fenton, photo-Fenton degradation of organic contaminants due to a significant promotion of H<sub>2</sub>O<sub>2</sub> decomposition.</p><p>In this work, we give a mini review about using of some currently metal doped magnetite based systems in heterogeneous Fenton, or photo-Fenton processes for degradation of pollutants. Then, the role of metal doped species for the enhanced efficiency of degradation process is discussed. Finally, possible reaction mechanism for the photo-Fenton degradation pollutants in the present of metal doped magnetite is also given.</p></sec><sec id="s2"><title>2. Fenton Process</title><p>In 1894, French scientist J. H. Fenton found that the oxidation ability of H<sub>2</sub>O<sub>2 </sub>has been greatly increased when Fe<sup>2+</sup> catalyse H<sub>2</sub>O<sub>2</sub> given the acid conditions (pH: 2 - 5). It is called Fenton reaction and the acid solution is called Fenton reagent [<xref ref-type="bibr" rid="scirp.80759-ref17">17</xref>] . It is clear nowadays that the hydroxyl radical (•OH) which has strong oxidation ability is caused by the compound of Fe<sup>2+</sup> and H<sub>2</sub>O<sub>2</sub> [<xref ref-type="bibr" rid="scirp.80759-ref18">18</xref>] . The oxidation potential of hydroxyl radical (•OH) is well known with 2.80V which is merely lower than that of F<sub>2</sub>. The hydroxyl radical (•OH) can destroy structure of organic synthesis because of strong oxidation. The fact make it possible that environmental pollutants can be degradated which can’t often be done by other general methods. The mechanisms of generating •OH in Fenton reaction are as follows [<xref ref-type="bibr" rid="scirp.80759-ref12">12</xref>] :</p><p>Fe ( II ) + H 2 O 2 → Fe ( III ) +   &#183; OH + OH − (1)</p><p>Fe ( III ) + H 2 O 2 → Fe ( HO 2 ) 2 + + H + (2)</p><p>Fe ( HO 2 ) 2 + → Fe ( II ) + HO 2 (3)</p><p>O 2 − + Fe ( III ) → Fe ( II ) + O 2 (4)</p><p>&#183; OH + H 2 O 2 → HO 2 + H 2 O (5)</p><p>Thus •OH is formed from hydrogen peroxide when either Fe(II) or Fe(III) is present. The existence of •OH radicals in Fenton reaction has been proven by monitoring the fluorescence intensity changes [<xref ref-type="bibr" rid="scirp.80759-ref19">19</xref>] .</p></sec><sec id="s3"><title>3. Photo-Fenton Process</title><p>Heterogeneous photo-Fenton process is combination of Fenton reagents (H<sub>2</sub>O<sub>2</sub> and Fe<sup>2+</sup>) and UV-Vis radiation (λ &lt; 600 nm) that gives rise to extra •OH radicals by two additional reactions. One is the photoreduction of Fe<sup>3+</sup> to Fe<sup>2+</sup> ions as shown and another is the peroxide photolysis via shorter wavelengths as the following equations [<xref ref-type="bibr" rid="scirp.80759-ref20">20</xref>] :</p><p>Fe 3 + + H 2 O 2 + h υ → Fe 3 + OOH + H + (6)</p><p>Fe 3 + OOH → Fe 2 + + OOH (7)</p><p>Fe 2 + + H 2 O 2 → Fe 3 + +   &#183; OH + OH − (8)</p><p>Fe ( OH ) 2 + + h υ → Fe 2 + +   &#183; OH (9)</p><p>H 2 O 2 + h υ → 2 &#183; OH (10)</p><p>The photo-Fenton process was reported as more efficient than Fenton treatment. In some cases, use of sunlight instead of UV irradiation reduced the costs [<xref ref-type="bibr" rid="scirp.80759-ref21">21</xref>] . However, this offers a lower degradation rate of pollutants. Acidic conditions (about pH 3) were also reported to be favorable and this may be mainly due to the conversion of carbonate and bicarbonate species into carbonic acid, which has a low reactivity with hydroxyl radicals [<xref ref-type="bibr" rid="scirp.80759-ref22">22</xref>] .</p><p>In the case of conductor catalyst, the reaction mechanism can be proposed as following:</p><p>Catalyst + h υ → Catalyst ( e cb − , h vb + ) (11)</p><p>e − + H 2 O 2 →   &#183; OH + OH − (12)</p><p>e − + Fe 3 + → Fe 2 + (13)</p><p>Fe 2 + + H 2 O 2 → Fe 3 + +   &#183; OH + OH − (14)</p><p>Regenerated Fe<sup>3+</sup> will take place the reaction to form Fenton reagents leading to<sup> </sup>more •OH can be produced [<xref ref-type="bibr" rid="scirp.80759-ref23">23</xref>] <sup> </sup>as showed in <xref ref-type="fig" rid="fig1">Figure 1</xref>.</p></sec><sec id="s4"><title>4. Metal Doped Fe<sub>3</sub>O<sub>4</sub> Based Catalysts</title><p>It is recently reported that Fe<sub>3</sub>O<sub>4</sub> is the effective heterogeneous Fenton, photo Fenton catalyst for removal contaminants in wastewater treatment [<xref ref-type="bibr" rid="scirp.80759-ref24">24</xref>] . The magnetite ability to promote photo-Fenton reactions even under circum neutral pH conditions, the limited iron leaching and its easy magnetic separation makes magnetite a promising catalyst in wastewater treatment applications. In addition, magnetite can be synthesized in the laboratory by various biotic and abiotic</p><p>pathways. Abiotic procedures to form magnetite include co-precipitation of soluble Fe (II) and Fe (III) species, oxidation of hydroxylated Fe (II) species and ferric oxides trans-formation. The morphology, crystallography and specific surface area of natural or synthetic magnetite can be controllable synthesized with vary widely route. There are many ways for fabrication of magnetite nanoparticles, such as the hydrothermal route [<xref ref-type="bibr" rid="scirp.80759-ref25">25</xref>] , ball mill method [<xref ref-type="bibr" rid="scirp.80759-ref26">26</xref>] , polydiallyldimethylamonium chloride method [<xref ref-type="bibr" rid="scirp.80759-ref27">27</xref>] , co-precipitation, emulsion method [<xref ref-type="bibr" rid="scirp.80759-ref28">28</xref>] , solvothermal [<xref ref-type="bibr" rid="scirp.80759-ref29">29</xref>] , etc. For example, iron oxide nanoparticles, with size ranging from 50 to 100 nm, were synthesized by a solvothermal method [<xref ref-type="bibr" rid="scirp.80759-ref11">11</xref>] . The samples with magnetic properties consisting of magnetite (Fe<sub>3</sub>O<sub>4</sub>), or by a mixture of magnetite and maghemite (γ-Fe<sub>2</sub>O<sub>3</sub>), and samples with no magnetism consisting of hematite (α-Fe<sub>2</sub>O<sub>3</sub>) can be obtained by a simple route of adjusting precursor materials. The catalytic activity of the materials was studied for the degradation of diphenhydramine using the photo-Fenton process. The results showed that complete degradation of diphenhydramine with 78% of mineralization was achieved at relatively low leaching of iron species from the catalyst to the aqueous solution (1.9 mg・L<sup>−</sup><sup>1</sup>) with magnetite catalysts (<xref ref-type="fig" rid="fig2">Figure 2</xref>).</p><p>However, using magnetite in the Fenton, photo-Fenton processes are still limited due to its drawbacks such as a low relative magneticity, poor dispersibility, limited adsorption properties, and low catalytic activity [<xref ref-type="bibr" rid="scirp.80759-ref30">30</xref>] [<xref ref-type="bibr" rid="scirp.80759-ref31">31</xref>] . To come out some of disadvantages of pure magnetite, amount of routes has studied extremely as synthesis with controllable size, morphology, shaped or composite with other materials or non-metal or metal doping. In these routes, metal element doping is reported to be a promising approach due to interesting properties of products.</p><sec id="s4_1"><title>4.1. Metal Doped Fe<sub>3</sub>O<sub>4</sub> Based Catalysts for Fenton, Photo-Fenton Degradation</title><p>Recently, studying on metal doped magnetite based catalyst has paid more and</p><p>more attention of researchers. Based on the previous reports in this filed, it is can be seen that the introduction of Co, Cr [<xref ref-type="bibr" rid="scirp.80759-ref32">32</xref>] , Ti, Zn and Mn into magnetite structure may strongly promote the Fenton, photo-Fenton degradation of organic contaminants due to a significant promotion of H<sub>2</sub>O<sub>2</sub> decomposition. Our previous report showed Zn doped magnetite has higher capacity in the photo-Fenton degradation of cephalexin and rhodamine B compared to pure magnetite. Hongping Hea et al. have prepared substituted magnetite with chromium via a simple precipitation-oxidation method. The applicability of series of substituted magnetite as Fenton catalyst in the degradation of cationic (MB) and anionic (acid orange II) model dyes was investigated [<xref ref-type="bibr" rid="scirp.80759-ref33">33</xref>] . Cr incorporation significantly improved the catalytic activity of magnetite in heterogeneous Fenton reaction. After 200 min of degradation, the MB removal rate was 59.3%, 71.3%, 87.0% and 95.2% in the presence of Fe<sub>2.82</sub>Cr<sub>0.18</sub>O<sub>4</sub>, Fe<sub>2.67</sub>Cr<sub>0.33</sub>O<sub>4</sub>, Fe<sub>2.53</sub>Cr<sub>0.47</sub>O<sub>4</sub> and Fe<sub>2.33</sub>Cr<sub>0.67</sub>O<sub>4</sub>, respectively (as shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>). A series of Mn doped magnetite was showed the enhanced efficiency in photo-Fenton degradation of MB compared to non-doped magnetite (<xref ref-type="fig" rid="fig4">Figure 4</xref>). It is noted that magnetite doping 1% Mn has higher catalytic capability than that of 10% [<xref ref-type="bibr" rid="scirp.80759-ref34">34</xref>] .</p><p>From the fact that in most natural cases, more than two kinds of metals are simultaneously introduced into magnetites in geological processes so studies on the influence of co-substituting metals on the structure and properties of magnetite, especially the surface reactivity and catalytic activity have been conducted widely [<xref ref-type="bibr" rid="scirp.80759-ref35">35</xref>] . The application of V-Ti co-doped magnetite in heterogeneous Fenton reaction showed that the incorporation of Ti<sup>4+</sup> and V<sup>3+</sup> can greatly enhance UV-Fenton catalytic activity of magnetite during the MB decolorizaition [<xref ref-type="bibr" rid="scirp.80759-ref36">36</xref>] . <xref ref-type="fig" rid="fig5">Figure 5</xref> revealed that Ti or V doped magnetite exhibited the higher catalyst in</p><p>the Fenton-degradation of MB. Through a series of experiments about the degradation and mineralization of two dyes (MO and MB) in heterogeneous Fenton using modified magnetite nanoparticles (Fe<sub>3−x−y</sub>Nb<sub>x</sub>Mo<sub>y</sub>O<sub>4</sub>), Shima Rahim Pouran et al. found out that co-doped Nb-Mo-magnetite nanoparticles showed highest activity in comparison to single Nb- and Mo-substituted magnetite samples [<xref ref-type="bibr" rid="scirp.80759-ref37">37</xref>] .</p><p>The results from previous reports have indicated that metal doping with magnetite can be a promising approach for improving the efficient degradation of contaminants in the Fenton and photo-Fenton due to high degradation efficiency around neutral pH, easy recycle of catalyst in practical wastewater purification. It is also because that metal doping magnetite can be easy to controllable synthesis. The obtained products have many interesting catalytic and magnetic properties. The different characterization of these obtained products depends tightly on not only the prepared route but also the metal doping.</p></sec><sec id="s4_2"><title>4.2. Role of Metal Doped Species and Compare Enhanced Efficiency of Degradation Process</title><p>So far, several single-metal cations, such as Ti<sup>4+</sup>, V<sup>3+</sup>, Mn<sup>2+</sup>, Co<sup>2+</sup>, Cr<sup>3+</sup>, Zn<sup>2+</sup>, and co-substituting metals have been reported as active components to increase the Fenton, photo-Fenton catalytic activity of magnetite. It has been widely acknowledged that the catalytic activity of magnetite is greatly dependent on the species, valence and occupancy of substituting metals. Substituting metals exhibiting thermo-dynamically favorable redox pairs can improve the catalytic activity of magnetite by accelerating the electronic transfer to produce the active species Fe<sup>2+</sup> for the Fenton reaction [<xref ref-type="bibr" rid="scirp.80759-ref33">33</xref>] . Effect of metal doped that exhibiting thermo-dynamically favorable redox pairs has proved via experiments reported by Rochel M. Lago et al. [<xref ref-type="bibr" rid="scirp.80759-ref39">39</xref>] . The experiments results showed that a low activity for methylene blue or chlorobenzen oxidation in the presence of Fe<sub>2:46</sub>Ni<sub>0:54</sub>O<sub>4</sub>, with only 10% color reduction after 50 min but Mn and Co substituted magnetites showed very high oxidation activity with complete discoloration of the solution in 5 and 10 min, respectively. This constraint efficiency can be explained by the different role of substituted metal. For nickel it can be considered that only the Ni<sup>2+</sup> species is stable and for this reason cannot initiate the reaction like Fe<sup>2+</sup> and Mn<sup>2+</sup>. Another reason for low efficiency of Ni doped magnetite is that Ni<sup>2+</sup> can replace mainly Fe<sup>2+</sup> in the magnetite structure leading to the reaction inhibited since Fe<sup>2+</sup> is responsible for the initial step. On the other hand, cobalt and manganese exhibit the redox pairs Co<sup>2+</sup>/Co<sup>3+</sup> and Mn<sup>2+</sup>/Mn<sup>3+</sup>, which could also produce radicals according to the reactions:</p><p>Co surf 2 + + H 2 O 2 → Co surf 3 + + OH − +   &#183; OH (15)</p><p>Mn surf 2 + + H 2 O 2 → Mn surf 3 + + OH − +   &#183; OH (16)</p><p>The strong effect of Co and Mn substitution it could also be considered a thermodynamically favorable electron transfer during the reaction shown by the following equations:</p><p>Fe 2 + + Co 3 + → Fe 3 + + Co 2 + (17)</p><p>Fe 2 + + Mn 3 + → Fe 3 + + Mn 2 + (18)</p><p>The efficient regeneration of the surface Co<sup>2+</sup> or Mn<sup>2+</sup> species by this process would be responsible for the remarkable increase an activity of H<sub>2</sub>O<sub>2</sub> decomposition and organic oxidation observed for these materials. Radicalar mechanism proposal for the activation of H<sub>2</sub>O<sub>2</sub> by Fe<sup>2+</sup> or meal doping of magnetite can be shown in <xref ref-type="fig" rid="fig6">Figure 6</xref>.</p><p>Magnetite is a semiconductor with a narrow band gap (0.1 eV) and shows a very high conductivity with almost metallic character which is important for</p><p>electron transport. Metal doping in magnetite is also expected as reactor for controllable synthesis of magnetite which the metal doped present can be change chemical and physical properties of initial magnetic leading to enhance catalytic activity. Our previous showed that diffusion of Zn into crystal Fe<sub>3</sub>O<sub>4</sub> can form new magnetite exposing interesting properties as optical absorption spectra, area surface and unique structure, resulting in higher capacity of photo-Fenton degradation of pollutants [<xref ref-type="bibr" rid="scirp.80759-ref40">40</xref>] . Recently, Hongping He reported that Cr substitution greatly increases the catalytic activity of magnetite in the heterogeneous Fenton reaction, but its enhancement extent depends on the chromium substitution level [<xref ref-type="bibr" rid="scirp.80759-ref33">33</xref>] . The catalytic activity relies on the octahedral cations rather than the tetrahedral ones, as the octahedral sites are almost exclusively exposed at the surface of the spinel structure (as <xref ref-type="fig" rid="fig7">Figure 7</xref>).</p><p>The obtained novel insights on role of metal doped species are of high importance for the designed synthesis as well as the utilization of substituted magnetite in the field of wastewater treatment.</p></sec></sec><sec id="s5"><title>5. Reaction Mechanism</title><p>From recent reports in literature on the transition metal oxide promoted H<sub>2</sub>O<sub>2</sub> decomposition in the absent of light, a possible reaction mechanism can be proposed. The H<sub>2</sub>O<sub>2</sub> decomposition in participate of doped metal is take place by two possible reaction pathways [<xref ref-type="bibr" rid="scirp.80759-ref41">41</xref>] : 1) the surface oxygen vacancies (Va<sub>surf</sub>) mechanism and 2) the radicalar mechanism. In the first route, a H<sub>2</sub>O<sub>2</sub> molecule will be actived by oxygen vacancy on the oxide surface participates to form O<sub>2</sub> (Equations (19) and (20)):</p><p>Va surf + H 2 O 2 → Va   −   O surf + H 2 O (19)</p><p>Va   −   O surf + H 2 O 2 → Va surf + H 2 O + O 2 (20)</p><p>The radical mechanism will be initiated by a reaction of H<sub>2</sub>O<sub>2</sub> with a partially</p><p>reduced surface pieces according to a Fenton like reaction or conduct reduce-oxidation reactions between redox pairs:</p><p>M surf 2 + + H 2 O 2 → M surf 3 + + OH − +   &#183; OH (21)</p><p>Fe 2 + + M 3 + → Fe 3 + + M 2 + (22)</p><p>In the radical route, O<sub>2</sub> can be form and the formation of O<sub>2</sub> can be proposed simply via the hydroperoxide radical:</p><p>H 2 O 2 +   &#183; OH → H 2 O +   &#183; OOH (23)</p><p>Fe surf 3 + +   &#183; OOH → Fe surf 2 + + H + + O 2 (24)</p><p>Due to magnetite, Fe<sub>3</sub>O<sub>4</sub>, is a semiconductor with a narrow band gap (0.1 eV) so in the present of light (UV/visible light), a following reaction mechanism suggested for understanding photo-Fenton reaction in the present of Zn doped Fe<sub>3</sub>O<sub>4</sub> HSMSs catalyst [<xref ref-type="bibr" rid="scirp.80759-ref42">42</xref>] . Under visible light irradiation, electron/hole pairs can be photogenerated in the catalyst. Then, photogenerated electrons can be trapped by H<sub>2</sub>O<sub>2</sub> leading to •OH. Simultaneously, they can be trapped by Fe<sup>3+</sup> on surface of catalyst forming Fe<sup>2+</sup>. Then more •OH can be produced that resulting in reaction between formed Fe<sup>2+</sup> with H<sub>2</sub>O<sub>2</sub>.</p><p>Catalyst + h υ → Catalyst ( e cb − , h vb + ) (25)</p><p>e − + H 2 O 2 →   &#183; OH + OH − (26)</p><p>e − + Fe 3 + → Fe 2 + (27)</p><p>Fe 2 + + H 2 O 2 → Fe 3 + +   &#183; OH + OH − (28)</p></sec><sec id="s6"><title>6. Conclusion</title><p>Based on the reports on magnetite increasing intensity in the literature recently, it can be seen that the introduction of Co, Cr, Ti, Zn and Mn into magnetite structure may strongly promote the Fenton, photo-Fenton degradation of organic contaminants due to a significant promotion of H<sub>2</sub>O<sub>2</sub> decomposition. Moreover, role of metal doping in the most case have been proposed. A possible reaction mechanism suggested for understanding photo-Fenton reaction in the present of metal doped magnetite have discussed in this work. However, reaction mechanism with participation of transition metal doping need make clearer by more studies. In particular, how to synthesis metal doped magnetite based materials to meet designed requirements plays a very important role in this field. These new insights are important direction for the controllable synthesis and the environmental application of metal substituted magnetites in the purification of organic contaminant textile wastewater.</p></sec><sec id="s7"><title>Cite this paper</title><p>Nguyen, X.S. and Ngo, K.D. (2018) The Role of Metal-Doped into Magnetite Catalysts for the Photo-Fenton Degradation of Organic Pollutants. 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