<?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">MSA</journal-id><journal-title-group><journal-title>Materials Sciences and Applications</journal-title></journal-title-group><issn pub-type="epub">2153-117X</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/msa.2020.116026</article-id><article-id pub-id-type="publisher-id">MSA-101159</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></subj-group></article-categories><title-group><article-title>
 
 
  Preparation and Characterization of Magnetic Banana Peels Biochar for Fenton Degradation of Methylene Blue
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Eric</surname><given-names>Sakué Ngankam</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Lemankreo</surname><given-names>Dai-Yang</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Baissassou</surname><given-names>Debina</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Abdellaziz</surname><given-names>Baçaoui</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Abdelrani</surname><given-names>Yaacoubi</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Abdoul</surname><given-names>Ntieche Rahman</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff3"><addr-line>Department of Chemistry, Higher Teachers’ Training College of Bertoua, University of Ngaoundéré, Ngaoundéré, Cameroon</addr-line></aff><aff id="aff1"><addr-line>Department of Chemistry, Faculty of Science, University of Maroua, Maroua, Cameroon</addr-line></aff><aff id="aff2"><addr-line>Department of Chemistry, Faculty of Science Semlalia, University of Cady Ayyad, Marrakech, Morocco</addr-line></aff><pub-date pub-type="epub"><day>02</day><month>06</month><year>2020</year></pub-date><volume>11</volume><issue>06</issue><fpage>382</fpage><lpage>400</lpage><history><date date-type="received"><day>25,</day>	<month>October</month>	<year>2019</year></date><date date-type="rev-recd"><day>26,</day>	<month>June</month>	<year>2020</year>	</date><date date-type="accepted"><day>29,</day>	<month>June</month>	<year>2020</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>
 
 
  Co-precipitation method was used for the synthesis of biochar/Fe
  <sub>3</sub>O
  <sub>4</sub> to heterogeneously degrade methylene blue (MB) in an aqueous medium. This catalyst was characterized by different techniques such as Fourier Transform Infrared (FTIR) Spectroscopy, X-ray diffraction (XRD), Scanning Electron Microscopy (SEM), Energy Dispersive X-ray Spectroscopy (EDX) and Raman Microscopy. The analysis highlighted the presence of iron oxides on the surface of the biochar in the form of magnetite (Fe
  <sub>3</sub>O
  <sub>4</sub>). Catalytic tests performed on this composite showed significant degradation and simple magnetic separation in the solution for reuse. Maximum degradation was carried out after stirring it for 90 minutes in an MB aqueous solution at different concentrations. The percentages of degradation were 99% and 98.6% 93.3% and 91% for concentrations of MB 40 mg/L and 60 mg/L, 80 mg/L and 120 mg/L respectively. The reactions followed a second-order kinetics with correlation coefficients r
  <sup>2</sup> = 0.9598, 0.9247, 0.9548 and 0.9614 for the same concentrations of MB at pH = 2, 0.2 mL/L H
  <sub>2</sub>O
  <sub>2</sub> and 15 mg of biochar/Fe
  <sub>3</sub>O
  <sub>4</sub>. This work provides a simple and an effective method for the preparation of biochar/Fe
  <sub>3</sub>O
  <sub>4</sub> and its use for the oxidation of MB by means of heterogeneous Fenton.
 
</p></abstract><kwd-group><kwd>Co-Precipitation</kwd><kwd> Magnetic Separation</kwd><kwd> Composite</kwd><kwd> Heterogeneous Fenton</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Water pollution by dyes has become a concern for the world’s population for decades. These dyes are listed in more than 100,000 types with an annual pollution of 7 &#215; 10<sup>5</sup> tons. The textile industries are considered as major consumers with around 36,000 tons per year. The World Bank estimates that around 20% of dye pollution comes from dyeing and textile processing [<xref ref-type="bibr" rid="scirp.101159-ref1">1</xref>]. According to studies 50 L to 100 L of water are consumed to tint 1 kg of cotton [<xref ref-type="bibr" rid="scirp.101159-ref2">2</xref>]. Insufficient treatment of textile effluents can lead to their accumulation in the water cycle, which can affect people living either through direct consumption of polluted water or through the food chain.</p><p>Physical techniques including adsorption are used for the treatment of industrial wastewater, but they are limited to a simple transfer of the pollutant from the effluent to the adsorbent, without any degradation occurs. The Advanced Oxidation process (AOP) is the burgeoning method of the chemical treatment of organic contaminants, considered to be bio-recalcitrant and/or for the disinfection of emerging pathogens [<xref ref-type="bibr" rid="scirp.101159-ref3">3</xref>]. It is based on the formation of highly reactive oxidative species (free radicals ˚OH) that can be induced by catalytic, sonochemical, biological, electrochemical and/or photochemical activations [<xref ref-type="bibr" rid="scirp.101159-ref4">4</xref>]. The high reactivity of the hydroxide radical with an oxidation potential of +2.80 V (ESH), has the power to oxidize many organic and inorganic molecules leading to their mineralization [<xref ref-type="bibr" rid="scirp.101159-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref6">6</xref>]. The mechanism of generation of ˚OH by the Fenton reactions has been taken up by Xuang and Kim (2018) according to the following equations:</p><p>Fe ( II ) + H 2 O 2 → Fe ( III ) + &#176; OH + OH − (1)</p><p>Fe ( III ) + H 2 O 2 → Fe ( HO 2 ) 2 + + H + (2)</p><disp-formula id="scirp.101159-formula7"><label>(3)</label><graphic position="anchor" xlink:href="//html.scirp.org/file/4-7702494x4.png"  xlink:type="simple"/></disp-formula><p>O 2 − + Fe ( III ) → Fe ( II ) + O 2 (4)</p><p>&#176; OH + H 2 O 2 → HO 2 + H 2 O (5)</p><p>Unlike the homogeneous Fenton method using iron ion and hydrogen peroxide, the heterogeneous Fe<sub>3</sub>O<sub>4</sub> method is increasingly used because it is easy to recover in a solvent using a magnetic field and can be regenerated for multiple uses [<xref ref-type="bibr" rid="scirp.101159-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref8">8</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref9">9</xref>].</p><p>To increase the catalytic activity of Fe<sub>3</sub>O<sub>4</sub>, it is more and more immobilized in porous supports. Biochar [<xref ref-type="bibr" rid="scirp.101159-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref10">10</xref>]; clay [<xref ref-type="bibr" rid="scirp.101159-ref11">11</xref>]; activated carbon [<xref ref-type="bibr" rid="scirp.101159-ref12">12</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref14">14</xref>], carbon microspheres [<xref ref-type="bibr" rid="scirp.101159-ref5">5</xref>], graphenes [<xref ref-type="bibr" rid="scirp.101159-ref15">15</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref16">16</xref>], multi-walled carbon nanotube [<xref ref-type="bibr" rid="scirp.101159-ref17">17</xref>] are the most used because of their small sizes, the hydrophilic groups on their surfaces, their thermal stability as well as their ease in being dispersed in water. Biochar is used as an excellent platform to support various catalytic nanoparticles due to its unique surface properties, easily adjustable functional groups, chemical stability and electrical conductivity [<xref ref-type="bibr" rid="scirp.101159-ref18">18</xref>]. It is considered a reservoir of electrons, and the quinone groups on the surface facilitate electronic exchanges during catalysis [<xref ref-type="bibr" rid="scirp.101159-ref19">19</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref20">20</xref>]. Banana peel is used for the preparation of biochar by its abundance. In 2016, Cameroon was considered the first banana producer in Africa. Therefore, it has been proved banana peels equivalent to 40% of the total weight of fresh banana, are generated as a wasted product in industries producing banana products [<xref ref-type="bibr" rid="scirp.101159-ref21">21</xref>]. These peels are not being used for any other purposes and or mostly dumped as solid waste at large expense; hence the need to transform it into biochar and use it as a catalytic support. We now count several methods of immobilization of Fe<sub>3</sub>O<sub>4</sub> of magnetism on a biochar support, namely the co-precipitation technique, the hydrothermal method, ball mill method; the sol gel method [<xref ref-type="bibr" rid="scirp.101159-ref22">22</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref23">23</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref24">24</xref>]. The co-precipitation method is the one most used because it is easy to implement that and it takes place at low temperature. The coprecipitation method has the advantage of directly obtaining homogeneous nanomaterials with small size and size distribution through various chemical reactions in the solution. The main advantage is that a large quantity of nanoparticles material can be produced. The coprecipitation technique is probably the simplest and most convenient chemical pathway to synthesize magnetic nanoparticles [<xref ref-type="bibr" rid="scirp.101159-ref25">25</xref>].</p><p>In this work, the biochar from the dry banana peels was prepared by simple pyrolysis under nitrogen atmosphere and the co-precipitation method was used for the immobilization of magnetite used as precursors FeCl<sub>2</sub>&#183;4H<sub>2</sub>O and FeCl<sub>3</sub>&#183;6H<sub>2</sub>O. The catalyst prepared was characterized by Fourier transform infrared (FTIR), Raman spectroscopy, X-ray diffraction (XRD), Scanning electron microscopy (SEM), energy dispersive X-ray spectroscopy (EDX). The ability of the particles to facilitate the Fenton oxidation of methylene blue (MB) has been studied under conditions of pH, pollutant concentration, agitation time, catalyst mass and very precise H<sub>2</sub>O<sub>2</sub> concentration.</p></sec><sec id="s2"><title>2. Experimental Section</title><sec id="s2_1"><title>2.1. Reagents and Materials</title><p>The “Musa” banana peels, collected in municipal garbage cans were washed, dried and used as precursors of char. Iron III chloride hexahydrate (FeCl<sub>3</sub>&#183;6H<sub>2</sub>O, 99% purity) and iron II chloride tetrahydrate (FeCl<sub>2</sub>&#183;4H<sub>2</sub>O 99% purity) was supplied by LaboChemie. Sodium Hydroxide (NaOH, ≥99% purity) purchased from Sigma Aldrich. Hydrochloric acid (HCl 37%) from CarloERBA. Ethanol (CH<sub>3</sub>CH<sub>2</sub>OH, ≥99%) purchased from Sigma Aldrich. Hydrogen peroxide (H<sub>2</sub>O<sub>2</sub>, 30.1%) from PROLABO. Methylene blue (MB, 98%) of formula C<sub>16</sub>H<sub>18</sub>ClN<sub>3</sub>S from Reactive RAL. All chemicals are analytical grade and were used without further purification.</p></sec><sec id="s2_2"><title>2.2. Preparation of Biochar/Fe<sub>3</sub>O<sub>4</sub></title><p>Raw materials (ripe banana peels), collected in municipal garbage cans were washed, dried in the sun for 8 hours and then at 80˚C in an oven for 24 hours. Later on, the samples were scrambled into small particles followed by the introduction of 15 g of obtained samples into the carbolite brand turbolace and their carbonization at 500˚C under nitrogen N<sub>2</sub> atmosphere (0.15 mL/min) with a temperature change of 10˚C/min and a residence time of 2 h. The oven was allowed to cool down to room temperature. The biochar was then recovered, dried in an oven during 24 hours and then stored.</p><p>The biochar/Fe<sub>3</sub>O<sub>4</sub> was prepared by co-precipitation method as described by Monica et al. [<xref ref-type="bibr" rid="scirp.101159-ref13">13</xref>]: 2 g of biochar previously prepared were introduced in 200 mL of an aqueous solution containing 7.32 g of FeCl<sub>3</sub>&#183;6H<sub>2</sub>O (27 mM) and 2, 67 g of FeCl<sub>2</sub>&#183;4H<sub>2</sub>O (13.5 mM) (Fer III/Fer II ratio 2: 1) under magnetic stirring at 80˚C; 50 mL of NaOH solution (5M) was added while maintaining the temperature 80˚C, pH (10 - 12). The suspension was stirred for about 1 hour until the color changed from the brown to black color. The whole left at room temperature was filtered and the precipitate was washed several times with distilled water and ethanol to neutral pH. The obtained sample was dried at 80˚C and stored for physico-chemical characterizations. Pure magnetite was prepared by the same procedure in the absence of biochar.</p></sec><sec id="s2_3"><title>2.3. Characterization of the Catalyst</title><p>The pH of zero charge was determined as follows: 50 mL of an aqueous solution of NaCl (0.01M) were introduced into six pH bottles; the pH was adjusted to 2, 4, 6, 8 and 10. These different bottles were bubbled with nitrogen to stabilize the pH. 0.15 g of Biochar/Fe<sub>3</sub>O<sub>4</sub> was introduced into these different flasks. The mixtures, stirred during 48 hours were filtered and the final pH of the filtrate was measured using a pH meter (HI 2209 pH meter). The encounter with the first bisector of the pH curve (final) = f (initial pH) indicates the pH of charge zero charge [<xref ref-type="bibr" rid="scirp.101159-ref26">26</xref>]. Similarly, the pH of the material was carried out using 0.15 g Biochar/Fe<sub>3</sub>O<sub>4</sub> in 50 mL of distilled water, stirred for 48 h and measuring the pH.</p><p>The functional groups present in Biochar/Fe<sub>3</sub>O<sub>4</sub> were ascertained by Fourier transform Infrared spectroscopy (FTIR, Vertex 70 de BRUKER) over the region 400 - 4000 cm<sup>−1</sup> in pellet form the powder samples of 1 mg mixed with spectroscopic grade KBr (Merck) of 9 mg with a resolution of 4 cm<sup>−1</sup> (32 scans). Spectra X-ray diffraction on XRD powder (RigakuGeigerflex, Cu Kα, λ = 1.5406A) produced at 30 kV and 25 mA scanned the diffraction angles (2θ) between 10˚ and 80˚ with the step size of 0.002˚ 2θ per second. Elemental EDX analysis performed using EDAX TEAM, 125.9 ev of resolution, to know the composition of the elements present in the material as well as SEM (VEGA3 TESCAN) to know the surface morphology. Raman spectroscopy to determine the structural and electronic properties of materials performed with a Nano brand SP (Confotec MR-SOL instrument) with the 570 nm wavelength laser. All these analyzes were carried out at the “Centre d’Analyseet de Caract&#233;risation” Semlalia-Marrakech Faculty of Sciences of Cadi Ayyad University (Morocco).</p></sec><sec id="s2_4"><title>2.4. Experimental Procedure</title><p>To evaluate the catalytic activity of the material, an aqueous solution of methylene blue at the concentrations of 40 mg/L and 60 mg/L, 80 and 120 mg/L were used. 15 mg of the catalyst was added to 50 mL of the MB solution, pH = 2. 0.2 mL/L of hydrogen peroxide (H<sub>2</sub>O<sub>2</sub>) was added to the MB solution. The whole solution was stirred for 90 min and after the solid phase was separated from liquid one by magnetization (<xref ref-type="fig" rid="fig1">Figure 1</xref>). The residual concentration of MB was measured by means of SECOMAN brand UV-Vis spectrometer.</p><p>The MB degradation percentage was calculated using the following formula</p><p>% R = ( C o − C e ) ⋅ 100 C o</p><p>C<sub>o</sub> is the initial concentration of MB (mg/L); C<sub>e</sub> is the concentration at any time (mg/L) and %R is the percentage of elimination of MB (%). Kinetic studies were performed and the equations corresponding to the different orders are given by the formulas [<xref ref-type="bibr" rid="scirp.101159-ref27">27</xref>]:</p><p>The kinetics of the zero order, is given by Equation (6)</p><p>[ M B ] i − [ M B ] t = k o t (6)</p><p>The first order is given by Equation (7)</p><p>− ln ( [ M B ] t [ M B ] i ) = K 2 t (7)</p><p>with [MB]<sub>i</sub> and [MB]<sub>t</sub> the concentrations t = 0 and t = t respectively, k is the speed constant (min<sup>−1</sup>) and t the time (min).</p><p>The second order is given by Equation (8)</p><p>1 [ M B ] t − 1 [ M B ] i = K 2 t (8)</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Characterization</title><p>Fourier transform infrared spectrum (FTIR) is done to determine the structural characterization of the dry banana peels, biochar and biochar/Fe<sub>3</sub>O<sub>4</sub>. <xref ref-type="fig" rid="fig2">Figure 2</xref> shows the FTIR spectra of the banana peels, biochar and biochar/Fe<sub>3</sub>O<sub>4</sub> in wave number range of 4000 - 400 cm<sup>−1</sup>.</p><p>Some characteristic bands from dry banana peels disappeared for the benefit of others bands. The wide band around 3500 - 3250 cm<sup>−1</sup> attributable to the −OH stretching vibrations. This band reappears intensely when magnetite is introduced; due to the fact that the impregnation reaction is carried out in an aqueous medium (co-precipitation). The bands around 1583.4 - 1635 cm<sup>−1</sup> attributed to the elongation vibrations of C=O, C=C functions remained unchanged and having almost the same intensities on the dried banana peel as on the calcined and magnetized peel. Just a decrease in the intensity of the peaks (on banana peel calcined at 500˚C) due to pyrolysis. The presence of O-H deformation bond is observed at 1300 cm<sup>−1</sup>. We observe the C-O stretching vibration band at 1053 cm<sup>−1</sup> with a higher intensity on the black curve. Two bands, one very intense (650 - 567 cm<sup>−1</sup>) and the other less intense (444 cm<sup>−1</sup>) are observed and respectively corresponded to iron oxides (Fe-O) and oxides iron and silica (Fe-O-Si) [<xref ref-type="bibr" rid="scirp.101159-ref28">28</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref29">29</xref>] revealed that the band between 450 - 740 cm<sup>−1</sup> belonged to the Fe-O vibrations of the nanoparticles of iron oxides. We have in this case the chemical shifts towards the high wavelengths (hypochromic effect) of the probably biochar which thanks to its surface rich in electrons, has the capacity to reduce the gap energy of the semiconductors thus causing an increase its chemical shift [<xref ref-type="bibr" rid="scirp.101159-ref30">30</xref>].</p><p>Raman spectroscopy is a non-destructive method used to characterize the structural and electronic properties of materials. <xref ref-type="fig" rid="fig3">Figure 3</xref> is the Raman analysis curves for our biochar and biochar/Fe<sub>3</sub>O<sub>4</sub> samples.</p><p>The Raman spectra of the biochar from the banana peels (<xref ref-type="fig" rid="fig3">Figure 3</xref>(a)) have several bands, three of which are larger and have corresponding chemical shifts. The band at 1567 cm<sup>−1</sup> corresponding to the band G (G = graphite) of the E<sub>2</sub>g mode of hexagonal graphite. It is related to the vibration involving sp<sup>2</sup> of hybrid carbon atoms that includes graphene sheet [<xref ref-type="bibr" rid="scirp.101159-ref31">31</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref32">32</xref>]. This position of the peak G indicates the degree of charge transfer. Due to the stiffness of G-peak related links, the phonon mode energy increases [<xref ref-type="bibr" rid="scirp.101159-ref33">33</xref>]. On the other hand, when we mix the biochar with the iron oxides, the Raman spectrum (<xref ref-type="fig" rid="fig3">Figure 3</xref>(b)) indicates the very weak G band (I<sub>D</sub>/I<sub>G</sub> = 2.4). This low intensity as well as the I<sub>D</sub>/I<sub>G</sub> ratio shows that iron oxides create a lot of disorder in the biochar structure.</p><p>Band D (D = disorder) at about 1372.2 cm<sup>−1</sup> (<xref ref-type="fig" rid="fig3">Figure 3</xref>(a)) is known as the disorder or defect band and represents a carbon ring breathing pattern sp2, although to be active the ring must be adjacent to a graphene edge or defect. Its intensity is much greater in our material (<xref ref-type="fig" rid="fig3">Figure 3</xref>(a)) and the ratio I<sub>D</sub>/I<sub>G</sub> = 0.98 thus confirms the defect in the carbon structure. The presence of defects improves the performance of carbon materials because of the strong anisotropy, mechanical strength, or electrical conductivity between the plane and out-of-plane direction [<xref ref-type="bibr" rid="scirp.101159-ref34">34</xref>]. On the spectrum in <xref ref-type="fig" rid="fig3">Figure 3</xref>(b) we observe a weak intensity as well as a Raman shift towards the low wavelengths (1291.3 cm<sup>−1</sup>). This decrease is accompanied by the absence of band G.In the end the strongest and most intense band covers an area between 2400 cm<sup>−1</sup> and 3300 cm<sup>−1</sup>at is the 2D band. This band has no defect and is still used to determine the thickness of the graphene layer. This is one of the characteristic bands of grapheme.</p><p>Some bands absent on the spectrum <xref ref-type="fig" rid="fig3">Figure 3</xref>(a) are present in <xref ref-type="fig" rid="fig3">Figure 3</xref>(b) between 200 cm<sup>−1</sup> and 1050 cm<sup>−1</sup>. These bands are 209.8 cm<sup>−1</sup> respectively; 278.5 cm<sup>−1</sup>; 391.75 cm<sup>−1</sup>; 481.5 cm<sup>−1</sup> and 603 cm<sup>−1</sup>. The band observed at 603 cm<sup>−1</sup> is assigned to the A<sub>1</sub>g mode which provides the stretching vibration of the oxygen atoms along the Fe-O bonds [<xref ref-type="bibr" rid="scirp.101159-ref35">35</xref>]. This expected band around 590 cm<sup>−1</sup> moves towards the strong wavelengths of the biochar. The bands around 209.8 cm<sup>−1</sup>; 278.5 cm<sup>−1</sup>; 481.5 cm<sup>−1</sup> corresponds to T<sub>2g</sub> (1) asymmetric Fe-O bonding mode; E<sub>g</sub> symmetrical Fe-O and T<sub>2g</sub> (2) symmetrical Fe-O stretch band of magnetite. We have at the end a 1090 cm<sup>−1</sup> band that could be a harmonic band of maghemite melted into magnetite [<xref ref-type="bibr" rid="scirp.101159-ref36">36</xref>].</p><p>The SEM/EDX analyze of the carbonized material and the magnetized materials are represented by <xref ref-type="fig" rid="fig4">Figure 4</xref>.</p><p>The SEM image of biochar <xref ref-type="fig" rid="fig4">Figure 4</xref>(a) showed a porous surface due to the carbonization process which favored the development of the porosity of materials. The SEM image of the magnetized banana peels <xref ref-type="fig" rid="fig4">Figure 4</xref>(c) showed a surface filled with cavity resulting from the pyrolysis of the banana peels at 500˚C. However, it is covered with iron oxides which obstruct these cavities. The presence of pores in the form of a cavity on the surface of a material is favorable to the adsorption of iron particles during the synthesis process as shown in <xref ref-type="fig" rid="fig4">Figure 4</xref>(c) [<xref ref-type="bibr" rid="scirp.101159-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref14">14</xref>].</p><p>The elemental and semi-quantitative composition of the biochar and the catalyst (Biochar/Fe<sub>3</sub>O<sub>4</sub>) are represented on the EDX spectra in <xref ref-type="fig" rid="fig4">Figure 4</xref>(b) and <xref ref-type="fig" rid="fig4">Figure 4</xref>(d) and the summary is shown in <xref ref-type="table" rid="table1">Table 1</xref>. We observe on the EDX spectrum, the variation of the percentage (C, O, Al, Si, P, Cl), the disappearance of elements (K, Mg) and the appearance of the new elements (Fe, N) after impregnation of magnetite. The presence of various elements even after impregnation of magnetite, informe us about the impure nature of Biochar/Fe<sub>3</sub>O<sub>4</sub>.</p><p>X-Ray Diffraction is an indispensable technique for identifying the crystalline phases of a compound. It is based on the observation of constructive interferences starting from a monochromatic radiation of wavelength λ using Bragg’s law:</p><p>2 d sin θ = n λ .</p><p>where: θ is the diffraction angle and the area under the peak is proportional to the diffracted intensity; d: distance between the crystalline plane; n: diffraction order.</p><p>The position of the peaks in the diagram corresponds to the angle 2θ.</p><p>The X-ray diffraction spectra of our two materials are shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>.</p><p>The biochar curve powder diffractogram (black) showed several peaks, one of which is stronger and the others are not excessively good. This makes us understand that more than 80% of the carbon structure is amorphous. This tells us that pyrolysis at 500˚C of banana peel is not complete and that amorphous carbon still exists. According to the position of the peaks, the banana peel would be thermally decomposed Fullerene and chaolite. Peaks 2θ = 11.4˚ and 31.7˚ are those of fullerenes and those at 2θ = 23.06˚; 28.34˚; 30.7˚; 31.62˚; 37.92˚ and 40.58˚ are attributed to chaolite [<xref ref-type="bibr" rid="scirp.101159-ref37">37</xref>]. On the other hand, according to Li et al. (2007), the more intense peak at 2θ = 28.34 could be the turbostratic structure of graphite carbon.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Elemental composition of biochar and biochar/Fe<sub>3</sub>O<sub>4</sub> catalysts</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Material</th><th align="center" valign="middle" >Element</th><th align="center" valign="middle" >Weight (%)</th><th align="center" valign="middle" >Atomic (%)</th><th align="center" valign="middle" >Material</th><th align="center" valign="middle" >Element</th><th align="center" valign="middle" >Weight (%)</th><th align="center" valign="middle" >Atomic (%)</th></tr></thead><tr><td align="center" valign="middle"  rowspan="10"  >Biochar</td><td align="center" valign="middle" >C</td><td align="center" valign="middle" >31.26</td><td align="center" valign="middle" >52.37</td><td align="center" valign="middle"  rowspan="10"  >Biochar/Fe<sub>3</sub>O<sub>4</sub></td><td align="center" valign="middle" >C</td><td align="center" valign="middle" >52.61</td><td align="center" valign="middle" >66.58</td></tr><tr><td align="center" valign="middle" >O</td><td align="center" valign="middle" >15.19</td><td align="center" valign="middle" >19.10</td><td align="center" valign="middle" >O</td><td align="center" valign="middle" >27.75</td><td align="center" valign="middle" >26.36</td></tr><tr><td align="center" valign="middle" >Mg</td><td align="center" valign="middle" >0.44</td><td align="center" valign="middle" >0.36</td><td align="center" valign="middle" >Fe</td><td align="center" valign="middle" >13.02</td><td align="center" valign="middle" >3.54</td></tr><tr><td align="center" valign="middle" >Al</td><td align="center" valign="middle" >0.48</td><td align="center" valign="middle" >0.36</td><td align="center" valign="middle" >Al</td><td align="center" valign="middle" >0.17</td><td align="center" valign="middle" >0.09</td></tr><tr><td align="center" valign="middle" >Si</td><td align="center" valign="middle" >1.16</td><td align="center" valign="middle" >0.83</td><td align="center" valign="middle" >Si</td><td align="center" valign="middle" >0.39</td><td align="center" valign="middle" >0.21</td></tr><tr><td align="center" valign="middle" >P</td><td align="center" valign="middle" >1.44</td><td align="center" valign="middle" >0.94</td><td align="center" valign="middle" >P</td><td align="center" valign="middle" >0.47</td><td align="center" valign="middle" >0.23</td></tr><tr><td align="center" valign="middle" >Cl</td><td align="center" valign="middle" >5.62</td><td align="center" valign="middle" >3.19</td><td align="center" valign="middle" >Cl</td><td align="center" valign="middle" >1.02</td><td align="center" valign="middle" >0.44</td></tr><tr><td align="center" valign="middle" >K</td><td align="center" valign="middle" >44.41</td><td align="center" valign="middle" >22.85</td><td align="center" valign="middle" >Ca</td><td align="center" valign="middle" >1.70</td><td align="center" valign="middle" >0.64</td></tr><tr><td align="center" valign="middle" >N</td><td align="center" valign="middle" >0</td><td align="center" valign="middle" >0</td><td align="center" valign="middle" >N</td><td align="center" valign="middle" >2.88</td><td align="center" valign="middle" >1.90</td></tr><tr><td align="center" valign="middle" >Total</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >Total</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >100</td></tr></tbody></table></table-wrap><p>On the spectrum of biochar/Fe<sub>3</sub>O<sub>4</sub> (red), the diffraction peaks are present at 2θ = 30.2˚, 35.7˚, 43.3˚, 53.7˚, 57.2˚, 62.9˚ correspond to the indices (220) (221) (400) (422) (511) (440) which are the inverse spinel group (Fd-3m) of magnetite according to the literature [<xref ref-type="bibr" rid="scirp.101159-ref37">37</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref38">38</xref>]. A peak at 2θ = 26.8˚ would belong to quartz grain crystals (SiO<sub>2</sub>) according to He et al. [<xref ref-type="bibr" rid="scirp.101159-ref10">10</xref>].</p></sec><sec id="s3_2"><title>3.2. Catalytic Activities</title><p>The degradation of MB was studied by various processes namely homogeneous Fenton (Fe<sub>3</sub>O<sub>4</sub>/H<sub>2</sub>O<sub>2</sub>), adsorption (Biochar, Fe<sub>3</sub>O<sub>4</sub> and Biochar/Fe<sub>3</sub>O<sub>4</sub>), and finally heterogeneous Fenton (Biochar/Fe<sub>3</sub>O<sub>4</sub>/H<sub>2</sub>O<sub>2</sub>) in a solution of 80 mg/L (MB) at pH = 2 (<xref ref-type="fig" rid="fig6">Figure 6</xref>), 90 minutes stirring and 0.2 ml/L H<sub>2</sub>O<sub>2</sub>. The results indicated no degradation effect when Fe<sub>3</sub>O<sub>4</sub> is used, low retention of (5%) when introducing Biochar/Fe<sub>3</sub>O<sub>4</sub> and 15% for biochar alone. This weak adsorption (5%) might be due to the occupation of the sites of adsorption of biochar by magnetite during synthesis on the one hand. On the other hand, the MB being a cationic pollutant, the adsorption in an acid medium is not favorable because of the electrostatic repulsions between the MB cation and the biochar surface (pHzc &gt; pH of the medium) possessing the same positive charge. When we introduce H<sub>2</sub>O<sub>2</sub> alone there is no effect. Whereas, when we use Fe<sub>3</sub>O<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> in the methylene blue solution, we observe a degradation of 65.8% under the same conditions. This degradation is due to the generation of hydroxide radicals which leads to the oxidation of MB. The degradation reached its maximum at 93.3% (for 80 mg/L MB) when passing to heterogeneous Fenton using Biochar/Fe<sub>3</sub>O<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> as catalyst. This is due to the electron-rich biochar surface of quinone groups that facilitates electronic exchanges during catalysis [<xref ref-type="bibr" rid="scirp.101159-ref19">19</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref20">20</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref39">39</xref>].</p><p>The kinetic studies made on Biochar/Fe<sub>3</sub>O<sub>4</sub>/H<sub>2</sub>O<sub>2</sub> for the different concentrations of MB at 90 min, pH = 2, 0.2 mL/L H<sub>2</sub>O<sub>2</sub>, 15 mg of the catalyst indicated that they are all first-order with correlation coefficients r<sup>2</sup> = 0.9598; 0.9247; 0.9548 and 0.9614 for the concentrations of 40 mg/L, 60 mg/L and 80 mg/L and 120 mg/L MB respectively (<xref ref-type="table" rid="table2">Table 2</xref>).</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> MB elimination rate as a function of initial concentration at 90 min and parameters of kinetic models</title></caption><table><tbody><thead><tr><th align="center" valign="middle" ></th><th align="center" valign="middle" ></th><th align="center" valign="middle"  colspan="2"  >Zero-order model</th><th align="center" valign="middle"  colspan="2"  >First-ordermodel</th><th align="center" valign="middle"  colspan="2"  >Second-order model</th></tr></thead><tr><td align="center" valign="middle" >Concentration (mg/L)</td><td align="center" valign="middle" >Degradation (%)</td><td align="center" valign="middle" >K<sub>0</sub>(min<sup>−1</sup>)</td><td align="center" valign="middle" >R<sup>2</sup></td><td align="center" valign="middle" >K<sub>1</sub>(min<sup>1</sup>)</td><td align="center" valign="middle" >R<sup>2</sup></td><td align="center" valign="middle" >K<sub>2</sub>(min<sup>−1</sup>)</td><td align="center" valign="middle" >R<sup>2</sup></td></tr><tr><td align="center" valign="middle" >40</td><td align="center" valign="middle" >99</td><td align="center" valign="middle" >0.4414</td><td align="center" valign="middle" >0.78</td><td align="center" valign="middle" >0.0546</td><td align="center" valign="middle" >0.96</td><td align="center" valign="middle" >0.0339</td><td align="center" valign="middle" >0.54</td></tr><tr><td align="center" valign="middle" >60</td><td align="center" valign="middle" >98.6</td><td align="center" valign="middle" >0.678</td><td align="center" valign="middle" >0.77</td><td align="center" valign="middle" >0.0587</td><td align="center" valign="middle" >0.92</td><td align="center" valign="middle" >0.0198</td><td align="center" valign="middle" >0.82</td></tr><tr><td align="center" valign="middle" >80</td><td align="center" valign="middle" >93.3</td><td align="center" valign="middle" >0.8704</td><td align="center" valign="middle" >0.79</td><td align="center" valign="middle" >0.0433</td><td align="center" valign="middle" >0.95</td><td align="center" valign="middle" >0.0064</td><td align="center" valign="middle" >0.65</td></tr><tr><td align="center" valign="middle" >120</td><td align="center" valign="middle" >91.4</td><td align="center" valign="middle" >1.1561</td><td align="center" valign="middle" >0.71</td><td align="center" valign="middle" >0.0461</td><td align="center" valign="middle" >0.96</td><td align="center" valign="middle" >0.0084</td><td align="center" valign="middle" >0.51</td></tr></tbody></table></table-wrap></sec><sec id="s3_3"><title>3.3. pH Effects</title><p>Studies on the pH of the medium showed a slight degradation of MB at pH 4 (<xref ref-type="fig" rid="fig7">Figure 7</xref>). This is due to the precipitation of Biochar/Fe<sub>3</sub>O<sub>4</sub> in the MB solution. At pH = 2 the degradation is maximal for 15 mg of the catalyst, 0.2 mL/L H<sub>2</sub>O<sub>2</sub>, 90 min. The increase in the oxidizing power of the MB at low pH (generally between 2 and 4) is attributed to the increase of the oxidizing potential of hydroxide radicals (HO˚) and to a strong dissolution of iron in solution in MB [<xref ref-type="bibr" rid="scirp.101159-ref40">40</xref>]. The strongly acidic medium is favorable for the stabilization of the hydrogen peroxides which favors the generation of HO˚ as well as the formation of the metal oxides leading to mineralization of the MB according to the Equations (1, 2, 3, 4 and 5). Beyond pH = 2 - 4, iron ions (Fe<sup>3+</sup> and Fe<sup>2+</sup>) are likely precipitated as solid [Fe(OH)<sub>2</sub>] iron hydroxide and [FeO(OH)] solid. These precipitations reducing the number of ferrous ions used to catalyze the Fenton reaction and thus induce low catalytic activity [<xref ref-type="bibr" rid="scirp.101159-ref41">41</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref42">42</xref>] [<xref ref-type="bibr" rid="scirp.101159-ref43">43</xref>]. This same phenomenon has been observed on our material which recorded degradation beyond pH 2, from 93.3% to 88.5% at pH 3. At pH 4, we observe a drop in degradation (34.54%) characterized by an increase in the precipitation of iron hydroxides.</p></sec><sec id="s3_4"><title>3.4. Effects of the Masses</title><p>The mass effect of the catalyst has a very important influence on the degradation of the MB. Indeed the masses of 5 mg, 10 mg and 15 mg were used in a solution of MB (40, 60, 80 and 120 mg/L) at pH 2, 0.2 ml/L H<sub>2</sub>O<sub>2</sub> for a maximum contact time of 90 min (<xref ref-type="fig" rid="fig8">Figure 8</xref>). The results obtained indicated an increase in the percentage of degradation with the increase of the catalyst mass (Biochar/Fe<sub>3</sub>O<sub>4</sub>). That is a degradation ranging from 70% to 99% for masses 5 mg to 15 mg of the catalyst. This is explained by the increase of active sites on the surface of the catalyst which is accompanied by the generation of a large amount of iron particles with production of OH˚ radicals.</p></sec><sec id="s3_5"><title>3.5. Concentration Effect of the Pollutant</title><p>The degradation of MB was also studied according to its concentration. We studied here the concentrations 40 mg/L, 60 mg/L and 80 mg/L and 120 mg/L. The results of <xref ref-type="fig" rid="fig9">Figure 9</xref>, shows a decrease in the degraded amount of MB when increasing the concentration of the pollutant. The maximum elimination is observed at 90 min with a mass of 15 mg of the catalyst leading to a degradation of 99%; 98.6%; 93.3% and 91.4% for MB concentrations 40 mg/L, 60 m/L, 80 mg/L and 120 mg/L. This slight decrease in degradation as a function of concentration is probably due to an increase in the number of MB molecules in the solution for the same amount of hydroxyl radicals formed (responsible for the Fenton reaction). Nevertheless, more than 60% of elimination is observed for the highest concentration of 120 mg/L after 90 min for a small mass of 5 mg of biochar/Fe<sub>3</sub>O<sub>4</sub>. What is encouraging because the concentrations found in textile wastewater is between 10 mg/L and 250 mg/L [<xref ref-type="bibr" rid="scirp.101159-ref14">14</xref>]. Regarding <xref ref-type="fig" rid="fig9">Figure 9</xref>, the highest degradation percentage was obtained with the highest mass.</p></sec><sec id="s3_6"><title>3.6. Effect of Stirring Time</title><p>The influence of contact time has been studied for different catalyst masses (5 mg, 10 mg and 15 mg) of 15 to 90 min (Figure10). The results of Figureshow an increase in degradation as a function of mass and stirring time and a decrease when increasing the concentration of MB. Indeed the reaction is slow during the first 15 minutes with degradation less than 20%, and becomes fast as from 30 min. It reaches the maximum at 90 min with a degradation percentage greater than 75% depending on the masses and the concentration of the dye. This is due to the permanent production of the electrons by the biochar as well as the radicals HO˚ by the hydrogen peroxide (H<sub>2</sub>O<sub>2</sub>) in the medium as a function of the time, which increases the rate of the reaction of catalysis. The longer the stirring time, the more electrons and radicals HO˚ are produced and the greater the degradation.</p></sec><sec id="s3_7"><title>3.7. Uv-Vis Spectra of Degradation of Methylene Blue as a Function of Time</title><p>The recording of the Uv-vis spectrum in the region 200 - 800 nm, of 80 mg/L methylene blue (<xref ref-type="fig" rid="fig1">Figure 1</xref>1), indicates a progressive decrease of the wavelength peaks 293 nm and 661 nm as a function of the contact time. The disappearance of the bands is obtained at a maximum time of 90 min in 15 mg/L of the catalyst, and 0.2 ml/L of H<sub>2</sub>O<sub>2</sub>. The decline in peaks around 293 nm is evidence of the destruction of the aromatic ring and heteropolyaromatic linkages of MB. Similarly, the decrease in the intensity of the band around 661 nm is due to the destruction of the thiazine group responsible for the blue coloring of MB [<xref ref-type="bibr" rid="scirp.101159-ref42">42</xref>]. Thus the degradation of methylene blue by homogeneous Fenton using magnetic biochar is evidenced.</p></sec><sec id="s3_8"><title>3.8. Stability and Reusability of the Catalyst</title><p>The stability and reusability of the material is an important factor in catalysis. Thus we repeated four times the degradation of methylene blue by the same catalyst. After use, the catalyst was recovered by simple magnetic filtration, washed with distilled water and reused for three cycles (<xref ref-type="fig" rid="fig1">Figure 1</xref>2). This reuse of biochar/Fe<sub>3</sub>O<sub>4</sub> (15 mg) was carried out in a solution of 80 mg/L (MB), pH = 2, 0.2 ml/L H<sub>2</sub>O<sub>2</sub> and at 90 min of stirring. We see the same degradation of methylene blue with no loss of the catalyst activity during the first two cycles and a slight loss of activity in the third cycle and four. This gives us information on the stability of our material (biochar/Fe<sub>3</sub>O<sub>4</sub>) for two cycles.</p></sec></sec><sec id="s4"><title>4. Conclusion</title><p>Biochar/Fe<sub>3</sub>O<sub>4</sub> was prepared by a simple method (Co-precipitation) using a biochar based on banana peel and iron chlorides as precursors. The analysis made on these materials showed a better dispersion of the magnetite particles on the surface of the biochar with a yield of 3.54% iron. Biochar/Fe<sub>3</sub>O<sub>4</sub> was found to be very useful for the degradation of methylene blue in aqueous media by heterogeneous Fenton. The use of H<sub>2</sub>O<sub>2</sub> (0.2 ml/L) as an oxidizing agent greatly favored the process, from a degradation of less than 5% (without H<sub>2</sub>O<sub>2</sub>) to more than 90% (in the presence of H<sub>2</sub>O<sub>2</sub>) during 90 min of stirring, 15 mg of the catalyst and at pH 2. The recovery of the catalyst by magnetization allowed the reusability without prior treatment in the Fenton process.</p></sec><sec id="s5"><title>Acknowledgements</title><p>Authors gratefully acknowledge the technical support of the Laboratory of Applied Organic Chemistry, Analysis and Environmental Unit, Faculty of Science Semlalia, University Caddy Ayyad of Marrakech in Morocco.</p></sec><sec id="s6"><title>Conflicts of Interest</title><p>The authors declare no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s7"><title>Cite this paper</title><p>Ngankam, E.S., Dai-Yang, L., Debina, B., Ba&#231;aoui, A., Yaacoubi, A. and Rahman, A.N. (2020) Preparation and Characterization of Magnetic Banana Peels Biochar for Fenton Degradation of Methylene Blue. Materials Sciences and Applications, 11, 382-400. https://doi.org/10.4236/msa.2020.116026</p></sec></body><back><ref-list><title>References</title><ref id="scirp.101159-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Reza, K.M., Kurny, A. and Gulshan, F. (2016) Photocatalytic Degradation of Methylene Blue by Magnetite+H2O2+UV Process. International Journal of Environmental Science and Development, 7, 325-329. https://doi.org/10.7763/IJESD.2016.V7.793</mixed-citation></ref><ref id="scirp.101159-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Kpinsoton, G.M.R. (2019) Elaboration de catalyseurs à base de charbon actifs et de latérites pour la dégradatin du bleu de méthylène par procédé fenton hétérogène. 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