<?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">GEP</journal-id><journal-title-group><journal-title>Journal of Geoscience and Environment Protection</journal-title></journal-title-group><issn pub-type="epub">2327-4336</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/gep.2020.89012</article-id><article-id pub-id-type="publisher-id">GEP-103290</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Earth&amp;Environmental Sciences</subject></subj-group></article-categories><title-group><article-title>
 
 
  Study of Coagulation Process with Lime in Treatment of Landfill Leachate from Fkih Ben Salah City (Morocco)
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Merzouki</surname><given-names>Hasna</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Hnini</surname><given-names>Rachid</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Brhich</surname><given-names>Amina</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Ellaite</surname><given-names>Mohammed</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Hanine</surname><given-names>Hafida</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>Lekhlif</surname><given-names>Brahim</given-names></name><xref ref-type="aff" rid="aff4"><sup>4</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Mandi</surname><given-names>Laila</given-names></name><xref ref-type="aff" rid="aff5"><sup>5</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Bahi</surname><given-names>Lahoucine</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Merzouki</surname><given-names>Mohammed</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib></contrib-group><aff id="aff4"><addr-line>Research Team Hydrogeology/Treatment and Treatment of Waters and Climate Change, Laboratory of Environmental 
Engineering, Hassania School of Public Works, Casablanca, Morocco</addr-line></aff><aff id="aff1"><addr-line>1</addr-line></aff><aff id="aff2"><addr-line>Laboratory of Bioprocess and Biointerface, Faculty of Science and Technology, University of Sultan Moulay Slimane, Beni Mellal, Morocco</addr-line></aff><aff id="aff3"><addr-line>Laboratory of Biological Engineering, Faculty of Science and Technology, University Sultan Moulay Slimane, Beni Mellal, Morocco</addr-line></aff><aff id="aff5"><addr-line>National Center for Studies and Research on Water and Energy (CNEREE), University Cadi Ayyad, Marrakech, Morocco</addr-line></aff><pub-date pub-type="epub"><day>08</day><month>09</month><year>2020</year></pub-date><volume>08</volume><issue>09</issue><fpage>197</fpage><lpage>211</lpage><history><date date-type="received"><day>17,</day>	<month>July</month>	<year>2020</year></date><date date-type="rev-recd"><day>27,</day>	<month>September</month>	<year>2020</year>	</date><date date-type="accepted"><day>30,</day>	<month>September</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>
 
 
  The leachates are the seat of complex processes which give them a heterogeneous character. Their compositions vary according to several factors: nature of the waste, conditions of their deposition, climatic conditions, their durations of stay, etc. They contain important quantities of organic, mineral matters even of bacteria, which require their treatment in order to safeguard the environment. To do this, several methods are used, such as membrane techniques (reverse osmosis, nanofiltration, etc.), biological techniques (activated sludge, SBR, etc.) and physicochemical techniques (Coagulation-flocculation, adsorption on activated carbon, etc.). Among these techniques, the leachate treatment by coagulation process with the lime showed interesting reduction of the various pollutants: 92.95% of turbidity, 88.23% of suspended matter, 89.89% of COD, 90.83% of BOD5, 78.39% of Fe, 77.78% of Mo, 38.29% of Cd, 48.75% of Al, 50.24% of S
  <sup>2-</sup>, 20.57% of K
  <sup>+</sup>, 27.24% of phosphorus and 19.53% of Cl
  <sup>-</sup>. Based on these results, the coagulation with the lime reveals interesting because it allows to reduce at a lesser cost the pollutants present in leachates.
 
</p></abstract><kwd-group><kwd>Leachate Treatment</kwd><kwd> Pollutants</kwd><kwd> Biological Techniques</kwd><kwd> Physicochemical Techniques</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>The Fkih Ben Salah landfill generates leachates with a high polluting load (COD = 74,530 mg O<sub>2</sub>/L and Conductivity = 24.90 ms/cm). They are a source of contamination for groundwater and superficial water, Idlahcen, Souabi, Taleb et al. (2014) and Chtioui, Khalil, Souabi et al. (2008). They must be imperatively treated before being rejected in the natural environment, Renou, Poulain, Givaudan et al. (2009), by using simple and little expensive technologies, Berradi, Chabab, Arroub et al. (2014).</p><p>The main objective of this work is to study the coagulation with the lime of young leachates. It aims to determining the optimal conditions of this treatment for a significant reduction of TSS, the organic and mineral load, Merzouki, Hanine, Lekhlif et al. (2016). The use of the lime is opportune, because it plays the coagulant role (Ca<sup>2+</sup>), and at the same time it allows the neutralization of the leachate (acid pH of the young leachate) thanks to its ions OH<sup>−</sup>. Its effectiveness compared with other coagulants (Fe<sup>3+</sup>, Al<sup>3+</sup>) has been shown by several authors, Merzouki, Hanine, Lekhlif et al. (2016), Hamidi, Salina, Mohd Nordin et al. (2007), Benradi, El Yahyaoui, Bouhlassa et al. (2013), El Bada, Assobhei, Kebbabi et al. (2010), and Khalil, Bouaouine, Chtioui et al. (2015).</p><p>In this study, we present the results of the coagulation tests using the following parameters: pH, turbidity, COD, BOD5, conductivity, quantity of the generated sludge, mineral and metallic elements (Al, Fe, Cd, Mg, Ca, Cl, Mo, P, K, Si, S), as well as abatement rates of present pollutants in the leachate.</p></sec><sec id="s2"><title>2. Materials and Methods</title><sec id="s2_1"><title>2.1. Sampling Zone</title><p>The landfill of Fkih Ben Salah city covers an area of 20 ha. It is located in 12 km north of the city on the R11 national road (<xref ref-type="fig" rid="fig1">Figure 1</xref>). It receives more than 85.51 tons per day of waste and generates 2730.72 L/day of leachate, Merzouki, Hanine, Lekhlif et al. (2016), corresponding to rate of 3.49% liter of leachate by ton of waste.</p><p>The leachate samples were collected directly at the level of collection trucks bringing household waste to the landfill. Volumes of leachate (5 L) were collected and mixed to form a homogeneous sample. The pH, the electrical conductivity and the temperature were measured in situ. In order to determine the other parameters, the samples were kept at a temperature below 4˚C and transmitted to 4˚C and transmitted to the laboratory within 24 hours.</p></sec><sec id="s2_2"><title>2.2. Preparation of Coagulant</title><p>For coagulation, a stock solution of coagulant was prepared by adding in one liter of distilled water 60 g of the hydrated lime in powder form of Ca(OH)<sub>2</sub>. From this solution, increasing volumes are taken and added to six beakers, each containing a volume of 500 ml of leachate. The concentration of Ca(OH)<sub>2</sub> obtained ranges from 2 to 12 g/L.</p></sec><sec id="s2_3"><title>2.3. Procedure Jar Test</title><p>The coagulation tests were accomplished in a Jar test apparatus (<xref ref-type="fig" rid="fig2">Figure 2</xref>). The mixture was agitated quickly at a speed of 250 rpm for 5 minutes and then to a speed of 25 rpm for 20 minutes. After 120 min of decantation, supernatant fraction samples are then recovered to analyze the following parameters: pH, DCO, total suspended solids (TSS), quantity of sludge and concentrations of mineral and metallic elements.</p></sec><sec id="s2_4"><title>2.4. Measurement of Biological and Physicochemical Parameters</title><p>The potential of Hydrogen (pH), the electrical conductivity (CE), the temperature (T ˚C), TSS and the salinity were measured using a multi-parameter probe type Consort C933. The suspended solids (MS) are determined by filtration on membranes at 0.45 μm in diameter (AFNOR T 90-105). The biological oxygen demand (BOD5) is determined according to the respirometric method in an enclosure thermostat at 20˚C (AFNOR, T 90-103). Chemical oxygen demand (COD) was determined using the standard method. The turbidity is measured by a turbidity</p><p>meter of the Palintest 7000 type. Calcium and magnesium were determined by complexometric titration with EDTA. Mineral and metallic elements (Fe, Cd, Cl, Mo, Si, S, K ...) were measured by a portable analyzer of the florescence Ray-X.</p><p>The estimation of the sludge produced after treatment by the lime coagulation technique was realized by measuring its volume and weight after decantation, filtration and drying in an oven at 105˚C until constant weight.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Characterization of the Studied Leachate</title><p>The leachates studied have a brownish color and a fecal odor. Their contents are presented in <xref ref-type="table" rid="table1">Table 1</xref>.</p><p>The physicochemical analyzes of the raw leachate have shown that it has an acidic character (pH = 4.05), an electric conductivity of 24.90 ms/cm and contains a concentration in SM of 3400 mg/L and a turbidity of 8018.33 NTU. The acid character is due to the fact that the leachate is young. This observation is noted by several authors, Jirou, Harrouni, Arroud et al. (2014), Benyoucef, EL Ghmari, &amp; Ouatmane (2015).</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Processes with special significance during SEA treatment</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Parameters</th><th align="center" valign="middle" >Minimum</th><th align="center" valign="middle" >Maximum</th><th align="center" valign="middle" >Average</th><th align="center" valign="middle" >Standard deviation</th><th align="center" valign="middle" >*GVRD</th><th align="center" valign="middle" >Unit</th></tr></thead><tr><td align="center" valign="middle" >Ph</td><td align="center" valign="middle" >3.99</td><td align="center" valign="middle" >4.02</td><td align="center" valign="middle" >4.05</td><td align="center" valign="middle" >0.08</td><td align="center" valign="middle" >5.5 - 9.5</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >T</td><td align="center" valign="middle" >28.16</td><td align="center" valign="middle" >33.15</td><td align="center" valign="middle" >30.65</td><td align="center" valign="middle" >0.12</td><td align="center" valign="middle" >30</td><td align="center" valign="middle" >˚C</td></tr><tr><td align="center" valign="middle" >Turbidity</td><td align="center" valign="middle" >7895.00</td><td align="center" valign="middle" >8180.00</td><td align="center" valign="middle" >8018.33</td><td align="center" valign="middle" >146.32</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >NTU</td></tr><tr><td align="center" valign="middle" >Salinity</td><td align="center" valign="middle" >13.02</td><td align="center" valign="middle" >14.23</td><td align="center" valign="middle" >13.45</td><td align="center" valign="middle" >0.68</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >PSU</td></tr><tr><td align="center" valign="middle" >CE</td><td align="center" valign="middle" >24.71</td><td align="center" valign="middle" >25.02</td><td align="center" valign="middle" >24.90</td><td align="center" valign="middle" >0.16</td><td align="center" valign="middle" >2.7</td><td align="center" valign="middle" >ms/cm</td></tr><tr><td align="center" valign="middle" >TSS</td><td align="center" valign="middle" >3090.00</td><td align="center" valign="middle" >4150.00</td><td align="center" valign="middle" >3613.33</td><td align="center" valign="middle" >53.01</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >COD</td><td align="center" valign="middle" >72150.00</td><td align="center" valign="middle" >76124.68</td><td align="center" valign="middle" >74530.00</td><td align="center" valign="middle" >209.96</td><td align="center" valign="middle" >500</td><td align="center" valign="middle" >mg O<sub>2</sub>/L</td></tr><tr><td align="center" valign="middle" >BOD5</td><td align="center" valign="middle" >37690.00</td><td align="center" valign="middle" >39420.00</td><td align="center" valign="middle" >38313.33</td><td align="center" valign="middle" >96.10</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >mg O<sub>2</sub>/L</td></tr><tr><td align="center" valign="middle" >SM**</td><td align="center" valign="middle" >2703.20</td><td align="center" valign="middle" >3906.00</td><td align="center" valign="middle" >3400.40</td><td align="center" valign="middle" >62.39</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Cl</td><td align="center" valign="middle" >33.25</td><td align="center" valign="middle" >34.26</td><td align="center" valign="middle" >33.81</td><td align="center" valign="middle" >0.5</td><td align="center" valign="middle" >0.2</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Ca</td><td align="center" valign="middle" >2075.00</td><td align="center" valign="middle" >2275.00</td><td align="center" valign="middle" >2175.00</td><td align="center" valign="middle" >100.00</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Mg</td><td align="center" valign="middle" >198.16</td><td align="center" valign="middle" >215.38</td><td align="center" valign="middle" >204.85</td><td align="center" valign="middle" >9.23</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Al</td><td align="center" valign="middle" >2.49</td><td align="center" valign="middle" >3.04</td><td align="center" valign="middle" >2.78</td><td align="center" valign="middle" >0.27</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >P</td><td align="center" valign="middle" >799.21</td><td align="center" valign="middle" >883.25</td><td align="center" valign="middle" >853.93</td><td align="center" valign="middle" >47.43</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >K</td><td align="center" valign="middle" >813.57</td><td align="center" valign="middle" >865</td><td align="center" valign="middle" >844.96</td><td align="center" valign="middle" >27.53</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Cd</td><td align="center" valign="middle" >23.43</td><td align="center" valign="middle" >24.98</td><td align="center" valign="middle" >24.00</td><td align="center" valign="middle" >0.85</td><td align="center" valign="middle" >0,25</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Mo</td><td align="center" valign="middle" >9.06</td><td align="center" valign="middle" >10.12</td><td align="center" valign="middle" >9.47</td><td align="center" valign="middle" >0.57</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Iron</td><td align="center" valign="middle" >213.62</td><td align="center" valign="middle" >268.32</td><td align="center" valign="middle" >241.087</td><td align="center" valign="middle" >27.35</td><td align="center" valign="middle" >5</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >Si</td><td align="center" valign="middle" >3.168</td><td align="center" valign="middle" >4.86</td><td align="center" valign="middle" >3.74</td><td align="center" valign="middle" >3.74</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr><tr><td align="center" valign="middle" >S</td><td align="center" valign="middle" >498.32</td><td align="center" valign="middle" >585.12</td><td align="center" valign="middle" >553.243</td><td align="center" valign="middle" >47.769</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >mg/L</td></tr></tbody></table></table-wrap><p>*General limit values of rejection of discharge; **SM: Suspended Matter.</p><p>Concerning the electrical conductivity and the concentration in SM, they are very high in comparison to the limit values, Jirou, Harrouni, Arroud et al. (2014) (CE = 2.7 ms/cm and SM = 100 mg/L). Nevertheless, they are in the range of values usually encountered for leachate, Jirou, Harrouni, Arroud et al. (2014), and Bouaouine, Khalil, Chtioui et al. (2015). The turbidity presents, as for it, a relatively high value, compared with those found by other authors: 2053 NTU, Khalil, Bouaouine, Chtioui et al. (2015), 1360 NTU, Toklo, Josse, Topanou et al. (2015), and 840 NTU, Benradi, El Yahyaoui, Bouhlassa et al. (2016).</p><p>The COD and the BOD5 are equal respectively to 74,530 mg/O<sub>2</sub>/L and 38313.33 mg/O<sub>2</sub>/L. They exceed the discharge standards (DCO = 500 mg/O<sub>2</sub>/L, BOD5 = 100 mg/O<sub>2</sub>/L), Jirou, Harrouni, Arroud et al. (2014). They are indicative of a strong organic load; they are comparable with those of landfill leachate of Agadir city (Morocco): COD = 72,000 mg O<sub>2</sub>/L, BOD5 = 44,000 mg O<sub>2</sub>/L, Jirou, Harrouni, Arroud et al. (2014), and superior to those obtained in Fez (Morocco): COD = 5400 mg O<sub>2</sub>/L, BOD5 = 1700 mg O<sub>2</sub>/L 5, Bouaouine, Khalil, Chtioui et al. (2015).</p><p>Concerning the mineral and metallic pollution, there is a high load of Ca (2175 mg/L), Al (2.78 mg/L), Mg (204.85 mg/L), P (853 mg/L), K (844.96 mg/L); Cd (24 mg/L), and Fe (241.087 mg/L). These values exceed the standards, Jirou, Harrouni, Arroud et al. (2014). They are greater than the values found in the Fez landfill (Morocco) (Fe = 33.72 mg/L, Cd = 4.36 mg/L), Benyoucef, EL Ghmari, &amp; Ouatmane (2015), and lower than those of the Oran landfill (Algeria) (Ca = 5216 mg/L, Mg = 4800 mg/L), Bennama, Younsi, Zoubir et al. (2010) and Larache Landfill (Morocco) (Fe = 650 mg/L), Er-raioui, Bouzid, Khannous et al. (2011). These results indicate pollution by several types of industrial solid waste rich in mineral and metallic elements. The concentrations of the various pollutants found at the Fkih Ben Salah landfill are generally different from those of other landfills. This is due to the nature of the waste, the age of the landfill and the climatic conditions, Bikash, Khet, &amp; Sanjay (2014), and Kurniawan, Lo, &amp; Chan (2006).</p></sec><sec id="s3_2"><title>3.2. Results of the Leachate Coagulation</title><sec id="s3_2_1"><title>3.2.1. Visual Observations</title><p>During coagulation, it is observed that the sludge separates progressively depending on the coagulant dose. During decantation, the leachate color changes. It gradually changes from brown to light brown (<xref ref-type="fig" rid="fig3">Figure 3</xref>). This change of color by coagulation has also been observed by several authors, El Bada, Assobhei, Kebbabi et al. (2010), and Shabiimam &amp; Anil (2011).</p></sec><sec id="s3_2_2"><title>3.2.2. Evolution of the pH</title><p>The pH of the young leachate is acid character (4.05). This denotes the installation of the anaerobic process, in particular in its acidogenesis phase producing the AGV. When the lime concentration increases, the supernatant pH value increases (<xref ref-type="fig" rid="fig4">Figure 4</xref>). This can be explained by the release of the OH<sup>−</sup> ions in solution.</p><p>This evolution has also been observed by other authors, Renou, Poulain, Givaudan et al. (2009), and Shabiimam &amp; Anil (2011).</p></sec><sec id="s3_2_3"><title>3.2.3. Evolution of the Quantity of Sludge Generated by Coagulation</title><p>As shown in <xref ref-type="fig" rid="fig5">Figure 5</xref> and <xref ref-type="fig" rid="fig6">Figure 6</xref>, the volume of sludge increases with the lime concentration. It varies from 30.33 ml/L to 27,967 ml/L (<xref ref-type="fig" rid="fig5">Figure 5</xref>). These volumes of sludge correspond to the quantities of dry matter ranging from 0 to 47.60 g/L (<xref ref-type="fig" rid="fig6">Figure 6</xref>).</p><p>The quantity of sludge obtained in these tests is lower compared to other studies, such as the one carried out, Khalil, Bouaouine, Chtioui et al. (2015), which found 647 ml/L of sludge after introduction 12 g/L of the lime on a leachate, agitated at a rotation speed of 200 rpm for 10 min and then at a slow speed of 60 rpm for 30 min. Merzouki, Hanine, Lekhlif et al. (2016), found almost identical results under the same coagulation conditions (302 ml/L of sludge). That can be due to the nature of the leachate, the rheology of the sludge and the retention of water within the solid matrix.</p></sec><sec id="s3_2_4"><title>3.2.4. Evolution of Electrical Conductivity</title><p>According to the figure (<xref ref-type="fig" rid="fig7">Figure 7</xref>), we note a slight decrease of the electrical conductivity, it passes from 24.08 mS/cm to 21.91 mS/cm to 6 g/L of Ca(OH)<sub>2</sub>, then an increase to 24.16 mS/cm from 10 g/L. At the beginning, the added lime eliminates the ions and molecules, contributing to the conductivity of leachate,</p><p>by coagulation up to pH = 6, which probably explains the decrease in the conductivity. Its increase then could be attributed to the concentration of added Ca<sup>2+</sup> and OH<sup>−</sup> ions, Renou, Poulain, Givaudan et al. (2009). Renou, Poulain, Givaudan et al. (2009), and El Bada, Assobhei, Kebbabi et al. (2010) have observed the same conductivity behavior. On the other hand, Renou, Poulain, Givaudan et al. (2009) have noted that the lime doses corresponding to the conductivity minimum increase when its initial value in the leachate increases.</p></sec><sec id="s3_2_5"><title>3.2.5. Evolution of Turbidity and Suspended Matter</title><p>The results of turbidity (<xref ref-type="fig" rid="fig8">Figure 8</xref>) show a decrease in the addition of lime. It passes from 8031.67 NTU to 566.27 NTU in a concentration of 10 g/L, which corresponds to a removal efficiency of about 92%. This value is similar to that found by Renou, Poulain, Givaudan et al. (2009) for an initial turbidity of 5190 NTU and by Slater, Uchrin, &amp; Ahlert (1983), and it is very high than that found by El Bada, Assobhei, Kebbabi et al. (2010) who carried out tests on an initial leachate turbidity of 130 NTU during methanation (65%). As for Shabiimam &amp; Anil (2011), having studied a leachate presenting an initial turbidity of 317 NTU, they were able to obtain a 99.9% removal of the turbidity at pH = 8 with a coagulant dose of 25 g/L.</p><p>According to <xref ref-type="fig" rid="fig9">Figure 9</xref>, the suspended matter abatement rate reaches 88.23% at 10 g/L of lime. This rate is in the range of values found by numerous authors, Melike &amp; Kadir (2007). Merzouki, Hanine, Lekhlif et al. (2016) have found successively a reduction of 82% and 71.6% of the suspended matter on the raw leachate.</p></sec><sec id="s3_2_6"><title>3.2.6. Evolution of the Organic Matte</title><p>The addition of the lime has reduced the COD of the leachate (<xref ref-type="fig" rid="fig1">Figure 1</xref>0). The abatement rate is 89.76%. It is comparable to that obtained by Merzouki, Hanine, Lekhlif et al. (2016) in the same conditions (90.27%) and Shabiimam &amp; Anil (2011) (86%), after adding 25 g/L of the lime on an initial COD of 2451 mg/L, and higher compared to those obtained by other authors. Tatsi, Zouboulis, Matis et al., (2003) found COD removal rates ranging from 30% to 45% when adding lime at a concentration of 7 g/L in fresh and partially stabilized leachate samples with an initial COD of 5350 mg/L, El Bada, Assobhei, Kebbabi et al. (2010) found a yield of 31% at a concentration of 10 g/L of lime for an initial COD of 138.76 mg/L, as for Shabiimam &amp; Anil (2011), they found a yield of 69% after addition of 25 g/L of lime for an initial COD leachate of 2451 mg/L.</p><p>The addition of the lime allowed to reducing also the BOD5 of the leachate (<xref ref-type="fig" rid="fig1">Figure 1</xref>1). The removal is 83.48%.</p><p>The elimination of COD and BOD5 of the leachate is due to the coagulation by the lime. It is also probably due to the adsorption on metal precipitates, including those of Ca<sup>2+</sup>, which are formed in the basic pH range, such as hydroxides, phosphates, carbonates, etc., or by entrainment during the coagulation of</p><p>the suspended matter. They can be further adsorbed by the positive charge of the Ca<sup>2+</sup> cations, which could constitute a bridge in the image of clay-humic complexes occurring clay coagulation.</p><p>COD and BOD5 decrease with lime increase simultaneously, giving a biodegradability ratio ranging between 1.21 and 3.27 with an average of 2.17 (<xref ref-type="table" rid="table2">Table 2</xref>), which denoting the biodegradability of the studied leachate, Kouassia, Ahoussik, Koffiy et al. (2014). We note that at the first addition of 2 g/L of lime, the ratio COD/DBO5 increases and then decreases (<xref ref-type="table" rid="table2">Table 2</xref>, <xref ref-type="fig" rid="fig1">Figure 1</xref>2). The increase is probably due to hydrolysis reactions or reactions leading to the release of entities more or less biodegradable. The decrease afterwards can be explained by the coagulation, precipitation and adsorption reactions which may occur as a result of the increase in the lime quantity; the mineral and refractory fractions tend to decrease also.</p></sec><sec id="s3_2_7"><title>3.2.7. Evolution of Mineral and Metallic Elements</title><p>The concentration of the main heavy metals presents in the leachate decreases. The elimination rates are 77.14% for the iron (<xref ref-type="fig" rid="fig1">Figure 1</xref>3), 77.78% for molybdenum (<xref ref-type="fig" rid="fig1">Figure 1</xref>4), and 41.67% for cadmium (<xref ref-type="fig" rid="fig1">Figure 1</xref>5). They are eliminated either by precipitation when the solubility product is reached or by simple adsorption on the various precipitates or on the coagulated suspension material, forming in solution. For the majority of them (Fe, Zn, Ba, Cr, Ni, Mn…), precipitation occurs when the pH increases, however their optimal pH do not coincide, Salem &amp; Allia (2011). They precipitate in the form of hydroxides, carbonates, phosphates, etc.</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Ratio COD/BOD5 according to doses of the lime</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Dose of lime (g)</th><th align="center" valign="middle" >0</th><th align="center" valign="middle" >2</th><th align="center" valign="middle" >4</th><th align="center" valign="middle" >6</th><th align="center" valign="middle" >8</th><th align="center" valign="middle" >10</th><th align="center" valign="middle" >12</th></tr></thead><tr><td align="center" valign="middle" >COD (gO<sub>2</sub>/L)</td><td align="center" valign="middle" >74.5</td><td align="center" valign="middle" >44.8</td><td align="center" valign="middle" >31.8</td><td align="center" valign="middle" >28.8</td><td align="center" valign="middle" >19.2</td><td align="center" valign="middle" >7.63</td><td align="center" valign="middle" >7.5</td></tr><tr><td align="center" valign="middle" >BOD5 (gO<sub>2</sub>/L)</td><td align="center" valign="middle" >38.3</td><td align="center" valign="middle" >13.7</td><td align="center" valign="middle" >12.7</td><td align="center" valign="middle" >12.3</td><td align="center" valign="middle" >10.3</td><td align="center" valign="middle" >6.33</td><td align="center" valign="middle" >3.6</td></tr><tr><td align="center" valign="middle" >COD/BOD5</td><td align="center" valign="middle" >1.95</td><td align="center" valign="middle" >3.27</td><td align="center" valign="middle" >2.50</td><td align="center" valign="middle" >2.34</td><td align="center" valign="middle" >1.86</td><td align="center" valign="middle" >1.21</td><td align="center" valign="middle" >2.08</td></tr></tbody></table></table-wrap><p>Many researchers having realized the tests of coagulation have found results more or less similar by coagulation with the lime, El Bada, Assobhei, Kebbabi et al. (2010), and Khalil, Bouaouine, Chtioui et al. (2015). According to Steeve, (1998), the treatment with the lime allows almost complete precipitation of numerous metals: Fe<sup>3+</sup>, AI<sup>3+</sup>, Fe<sup>2</sup><sup>+</sup> at pH 7.4 - 7.5. Dean, Bosqui, &amp; Lanouette (1972), showed that the lime allows the removal of many metals such as copper, zinc, iron, manganese, nickel and cobalt.</p><p>Figures 16-18 show the evolution of phosphorus, P, K<sup>+</sup> and S. The abatement rates are respectively 15.60% (Phosphorus), 20.57% (K<sup>+</sup>) and 20.77% (S). They are probably eliminated by adsorption. Phosphorus and S may also be removed by precipitation as phosphate or metal sulphide.</p></sec></sec></sec><sec id="s4"><title>4. Conclusion</title><p>The physicochemical study of the leachate characterization of the public landfill of Fkih Ben Salah city showed strong levels of pollution which widely exceed the legal limit values. According to this study, the leachate treatment by coagulation process with the lime showed interesting reduction of the various pollutants: turbidity, organic matter, mineral matter, etc. That is due to the coagulation by Ca<sup>2+</sup>, the precipitation of heavy metals in form of hydroxides, phosphates, carbonates, etc. when the pH increases, and their adsorption rates. The yields obtained were: 92.95% of turbidity, 88.23% of suspended matter, 89.89% of COD, 90.83% of BOD5, 78.39% of Fe, 77.78% of Mo, 38.29% of Cd, 48.75% of Al, 50.24% of S<sup>2−</sup>, 20.57% of K<sup>+</sup>, 27.24% of Phosphorus and 19.53% of Cl<sup>−</sup>. On the other hand, the biodegradability ratio COD/BOD5 presents an average value of 2.17, indicating the biodegradability of the leachate, which is similarly obtained with the pretreated leachate. Thus, a complementary biological treatment can be envisaged to further reduce the polluting load.</p></sec><sec id="s5"><title>Acknowledgements</title><p>My thanks and esteem go first of all to Professor Hafida Hanine who supervised this work, within the Laboratory of Bioprocesse and Biointerface, Faculty of Science and Technology, University of Sultan Moulay Slimane Beni Mellal, and that in collaboration with Professor Brahim Lekhlif who is part of the Hydrogeology, Water Treatment and Treatment and Climate Change research team, Environmental Engineering Laboratory, Hassania School of Public Works, Casablanca, I warmly thank him for his help and guidance .</p><p>A large part of the analyzes of this work was carried out within the National Center for Studies and Research on Water and Energy (CNEREE), at the Cadi Ayyad University, headed by Professor Laila Mandi. In this regard, I express my warm thanks to him for welcoming me to the CNEREE laboratories.</p><p>I would also like to express my gratitude to the researchers at the Laboratory of Biological Engineering, Sultan Moulay Slimane University Faculty of Science and Technology Beni Mellal; Professor Mohammed Merzouki, PhD student Mrs Brhich Amina, and Professor Ellaite Mohammed, for their contribution in this work.</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>Hasna, M., Rachid, H., Amina, B., Mohammed, E., Hafida, H., Brahim, L., Laila, M., Lahoucine, B., &amp; Mohammed, M. (2020). Study of Coagulation Process with Lime in Treatment of Landfill Leachate from Fkih Ben Salah City (Morocco). Journal of Geoscience and Environment Protection, 8, 197-211. https://doi.org/10.4236/gep.2020.89012</p></sec></body><back><ref-list><title>References</title><ref id="scirp.103290-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Bennama, T., Younsi, A., Zoubir, D., &amp; Debab, A. (2010). Caractérisation et traitement physico-chimique des lixiviats de la décharge publique d’El-Kerma (Algérie) par adsorption en discontinu sur de la sciure de bois naturelle et activée chimiquement. Water Quality Research Journal of Canada, 45, 81-90. https://doi.org/10.2166/wqrj.2010.009</mixed-citation></ref><ref id="scirp.103290-ref2"><label>2</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Benradi</surname><given-names> F.</given-names></name>,<name name-style="western"><surname> El Yahyaoui</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Bouhlassa</surname><given-names> S.</given-names></name>,<name name-style="western"><surname> Nounah</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Cherkaoui</surname><given-names> E.</given-names></name>,<name name-style="western"><surname> &amp; Ghrissi</surname><given-names> F. </given-names></name>,<etal>et al</etal>. (<year>2013</year>)<article-title>. Epaississement des concentrats d’osmose inverse</article-title><source> Journal of Materials and Environmental Science</source><volume> 4</volume>,<fpage> 832</fpage>-<lpage>839</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref3"><label>3</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Benradi</surname><given-names> F.</given-names></name>,<name name-style="western"><surname> El Yahyaoui</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Bouhlassa</surname><given-names> S.</given-names></name>,<name name-style="western"><surname> Nounah</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Khamar</surname><given-names> M.</given-names></name>,<name name-style="western"><surname> &amp; Ghrissi</surname><given-names> F. </given-names></name>,<etal>et al</etal>. (<year>2016</year>)<article-title>. Effect of pH and Time on the Leachate Treatment by Coagulation</article-title><source> Journal of Materials and Environmental Science</source><volume> 7</volume>,<fpage> 1001</fpage>-<lpage>1007</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref4"><label>4</label><mixed-citation publication-type="other" xlink:type="simple">Benyoucef, F., EL Ghmari, A., &amp; Ouatmane, A. (2015). Essai de traitement des lixiviats par UASB: Cas de la ville de Kasba Tadla. Déchets Sciences et Techniques, 70, 3-10. https://doi.org/10.4267/dechets-sciences-techniques.3272</mixed-citation></ref><ref id="scirp.103290-ref5"><label>5</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Berradi</surname><given-names> M.</given-names></name>,<name name-style="western"><surname> Chabab</surname><given-names> Z.</given-names></name>,<name name-style="western"><surname> Arroub</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> Nounah</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> &amp; El Harfi</surname><given-names> A. </given-names></name>,<etal>et al</etal>. (<year>2014</year>)<article-title>. Optimization of the Coagulation/Floculation Process for the Treatment of Industrial Wastewater from the Hot Dip Galvanizing of Steel</article-title><source> Journal of Materials and Environmental Science</source><volume> 5</volume>,<fpage> 360</fpage>-<lpage>365</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref6"><label>6</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Bikash</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Khet</surname><given-names> R. D.</given-names></name>,<name name-style="western"><surname> &amp; Sanjay</surname><given-names> N. </given-names></name>,<etal>et al</etal>. (<year>2014</year>)<article-title>. A Review of Factors Affecting the Composition of Municipal Solid Waste Landfill Leachat</article-title><source> International Journal of Engineering Science and Innovative Technology</source><volume> 3</volume>,<fpage> 273</fpage>-<lpage>281</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref7"><label>7</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Bouaouine</surname><given-names> O.</given-names></name>,<name name-style="western"><surname> Khalil</surname><given-names> F.</given-names></name>,<name name-style="western"><surname> Chtioui</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> Zaitan</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> &amp; Harrach</surname><given-names> A. </given-names></name>,<etal>et al</etal>. (<year>2015</year>)<article-title>. Traitement par électrocoagulation des lixiviats de la décharge publique contr&amp;#244lée de la ville de Fès (MAROC)</article-title><source> Larhyss Journal</source><volume> 23</volume>,<fpage> 53</fpage>-<lpage>67</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref8"><label>8</label><mixed-citation publication-type="other" xlink:type="simple">Chtioui, H., Khalil, F., Souabi, S., &amp; Aboulhassan, M. A. (2008). Evaluation de la pollution générée par les lixiviats de la décharge publique de la ville de Fès, Déchets. Sci Tech, 49, 25-28. https://doi.org/10.4267/dechets-sciences-techniques.1435</mixed-citation></ref><ref id="scirp.103290-ref9"><label>9</label><mixed-citation publication-type="other" xlink:type="simple">Dean, J. G., Bosqui, F. L., &amp; Lanouette, K. H. (1972). Removing Heavy Metals from Waste Water. Environmental Science &amp; Technology, 6, 518-522. https://doi.org/10.1021/es60065a006</mixed-citation></ref><ref id="scirp.103290-ref10"><label>10</label><mixed-citation publication-type="other" xlink:type="simple">El Bada, N., Assobhei, O., Kebbabi, A., Mhamdi, R., &amp; Mountadar, M. (2010). Caractérisation et prétraitement du lixiviat de la décharge de la ville d’azemmour, Déchets. Sciences et techniques revue francophone d’écologie industrielle n&amp;#730 58 2eme trimestre. https://doi.org/10.4267/dechets-sciences-techniques.3016</mixed-citation></ref><ref id="scirp.103290-ref11"><label>11</label><mixed-citation publication-type="other" xlink:type="simple">Er-raioui, H., Bouzid, S., Khannous, S., &amp; Zouag, M. A. (2011). Contamination des eaux souterraines par le lixiviat des décharges publiques: Cas de la nappe phréatique R’Mel (Province de Larache-Maroc Nord-Occidental). International Journal of Biological and Chemical Sciences, 5, 1118-1134. https://doi.org/10.4314/ijbcs.v5i3.72237</mixed-citation></ref><ref id="scirp.103290-ref12"><label>12</label><mixed-citation publication-type="other" xlink:type="simple">Hamidi, A., Salina, A., Mohd Nordin, A., Faridah, A., Asaari, H., &amp; Mohd Shahrir, Z. (2007). Colour Removal from Landfill Leachate by Coagulation and Flocculation Processes. Bioresource Technology, 98, 218-220. https://doi.org/10.1016/j.biortech.2005.11.013</mixed-citation></ref><ref id="scirp.103290-ref13"><label>13</label><mixed-citation publication-type="other" xlink:type="simple">Idlahcen, A., Souabi, S., Taleb, A., Zahidi, K., &amp; Bouezmarni, M. (2014). évaluation de la pollution générée par les lixiviats de la décharge publique de la ville de Mohammedia et son impact sur la qualité des eaux souterraines. Scientific Study &amp; Research: Chemistry &amp; Chemical Engineering, Biotechnology, Food Industry, 15, 35-50.</mixed-citation></ref><ref id="scirp.103290-ref14"><label>14</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Jirou</surname><given-names> Y.</given-names></name>,<name name-style="western"><surname> Harrouni</surname><given-names> Ch.</given-names></name>,<name name-style="western"><surname> Arroud</surname><given-names> A.</given-names></name>,<name name-style="western"><surname> Daoud</surname><given-names> S.</given-names></name>,<name name-style="western"><surname> Fox</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> &amp; Fatmi</surname><given-names> M. </given-names></name>,<etal>et al</etal>. (<year>2014</year>)<article-title>. Characterization of Urban Waste Leachate for Better Management of the Greater Agadir Controlled Landfill, Southern Morocco</article-title><source> Journal of Materials and Environmental Science</source><volume> 5</volume>,<fpage> 1816</fpage>-<lpage>1824</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref15"><label>15</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Khalil</surname><given-names> F.</given-names></name>,<name name-style="western"><surname> Bouaouine</surname><given-names> O.</given-names></name>,<name name-style="western"><surname> Chtioui</surname><given-names> H.</given-names></name>,<name name-style="western"><surname> Souabi</surname><given-names> S.</given-names></name>,<name name-style="western"><surname> Aboulhassan</surname><given-names> M. A.</given-names></name>,<name name-style="western"><surname> &amp; Ouammou</surname><given-names> A. </given-names></name>,<etal>et al</etal>. (<year>2015</year>)<article-title>. Traitement des lixiviats de décharge par coagulation-floculation</article-title><source> Journal of Materials and Environmental Science</source><volume> 6</volume>,<fpage> 337</fpage>-<lpage>1342</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref16"><label>16</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Kouassia</surname><given-names> E.</given-names></name>,<name name-style="western"><surname> Ahoussik</surname><given-names> E.</given-names></name>,<name name-style="western"><surname> Koffiy</surname><given-names> B.</given-names></name>,<name name-style="western"><surname> Kouamei</surname><given-names> K.</given-names></name>,<name name-style="western"><surname> Soro</surname><given-names> N.</given-names></name>,<name name-style="western"><surname> &amp; Biemi</surname><given-names> J. </given-names></name>,<etal>et al</etal>. (<year>2014</year>)<article-title>. Caracterisation physico-chimique du lixiviat d’une decharge de l’afrique de l’ouest: Cas de la decharge d’akouedo (abidjan-c&amp;#244te d’ivoire)</article-title><source> Larhyss Journal</source><volume> 19</volume>,<fpage> 63</fpage>-<lpage>74</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref17"><label>17</label><mixed-citation publication-type="other" xlink:type="simple">Kurniawan, T. A., Lo, W., &amp; Chan, G. Y. S. (2006). Physico-Chemical Treatments for Removal of Recalcitrant Contaminants from Landfill Leachate. Journal of Hazardous Materials, B129, 80-100. https://doi.org/10.1016/j.jhazmat.2005.08.010</mixed-citation></ref><ref id="scirp.103290-ref18"><label>18</label><mixed-citation publication-type="journal" xlink:type="simple"><name name-style="western"><surname>Melike</surname><given-names> Y.</given-names></name>,<name name-style="western"><surname> &amp; Kadir</surname><given-names> K. </given-names></name>,<etal>et al</etal>. (<year>2007</year>)<article-title>. TanerYonar</article-title><source> Journal of Biodiversity and Environmental Sciences</source><volume> 1</volume>,<fpage> 3</fpage>-<lpage>43</lpage>.<pub-id pub-id-type="doi"></pub-id></mixed-citation></ref><ref id="scirp.103290-ref19"><label>19</label><mixed-citation publication-type="other" xlink:type="simple">Merzouki, H., Hanine, H., Lekhlif, B., Mandi, L., &amp; Merzouki, M. (2016). Physico-Chemical Traitement of Leachates Case of the Landfill of Fkih Ben Salah, Morocco. IOSR Journal of Environmental Science, Toxicology and Food Technology, 10, 41-50.</mixed-citation></ref><ref id="scirp.103290-ref20"><label>20</label><mixed-citation publication-type="other" xlink:type="simple">Renou, S., Poulain, S., Givaudan, J. G., &amp; Moulin, P. (2009). Treatment Process Adapted to Stabilized Leachates: Lime Precipitation-Prefiltration-Reverse Osmosis. Journal of Membrane Science, 313, 9-22. https://doi.org/10.1016/j.memsci.2007.11.023</mixed-citation></ref><ref id="scirp.103290-ref21"><label>21</label><mixed-citation publication-type="other" xlink:type="simple">Salem, Z., &amp; Allia, K. (2011). Landfill Leachate Evaluation and Combined Treatment Process. In Proceedings of the 12th International Conference on Environmental Science and Technology (Vol. 2, p. 1600). Rhodes: Curran Associates, Inc.</mixed-citation></ref><ref id="scirp.103290-ref22"><label>22</label><mixed-citation publication-type="other" xlink:type="simple">Shabiimam, M. A., &amp; Anil, K. D. (2011). Treatment of Landfill Leachate Using Coagulation. In 2011 2nd International Conference on Environmental Science and Technology (Vol. 6, pp. 119-122). Singapore: IACSIT Press.</mixed-citation></ref><ref id="scirp.103290-ref23"><label>23</label><mixed-citation publication-type="other" xlink:type="simple">Slater, C. S., Uchrin, C. G., &amp; Ahlert, R. C. (1983). Physiochemical Pretreatment of Landfill Leachates Using Coagulation. Journal of Environmental Science &amp; Health Part A, 18, 125-134. https://doi.org/10.1080/10934528309375097</mixed-citation></ref><ref id="scirp.103290-ref24"><label>24</label><mixed-citation publication-type="other" xlink:type="simple">Steeve, D. (1998). Traitement des lixiviats concentrés en métaux lourds suite à la déco tamina non d’un sol par un procédé biologique et chimique. Mémoire présenté pour l’obtention du grade de Ma&amp;#238tre ès science (M.Sc). Université du Québec INRS-Eau.</mixed-citation></ref><ref id="scirp.103290-ref25"><label>25</label><mixed-citation publication-type="other" xlink:type="simple">Tatsi, A. A., Zouboulis, A. I., Matis, K. A., &amp; Samaras, P. (2003). Coagulation-Flocculation Pretreatment of Sanitary Landfill Leachates. Chemosphere, 53, 737-744. https://doi.org/10.1016/S0045-6535(03)00513-7</mixed-citation></ref><ref id="scirp.103290-ref26"><label>26</label><mixed-citation publication-type="other" xlink:type="simple">Toklo, R. M., Josse, R. G., Topanou, N., Togbe, A. F., Dossou-Yovo, P., &amp; Coulomb, B. (2015). Physico-Chemical Characterization of the Leachates of a Discharge: Case of Sanitary Burying Place of Ouèssè-Ouidah (South of Benin). International Journal of Innovation and Applied Studies, 13, 921.</mixed-citation></ref></ref-list></back></article>