<?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">JMMCE</journal-id><journal-title-group><journal-title>Journal of Minerals and Materials Characterization and Engineering</journal-title></journal-title-group><issn pub-type="epub">2327-4077</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jmmce.2021.94024</article-id><article-id pub-id-type="publisher-id">JMMCE-110611</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Chemistry&amp;Materials Science</subject><subject> Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Production of High-Purity Silica Sand from Ivorian Sedimentary Basin by Attrition without Acid Leaching Process for Windows Glass Making
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Péyokoh</surname><given-names>Roger Thio</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>Kouassi</surname><given-names>Bruno Koffi</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>Kouadio</surname><given-names>Denis Konan</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>Kouakou</surname><given-names>Alphonse Yao</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib></contrib-group><aff id="aff2"><addr-line>National Polytechnic Institute Félix Houphou&amp;amp;#235;t-Boigny (INPHB), Yamoussoukro, C&amp;amp;#244;te d’Ivoire</addr-line></aff><aff id="aff1"><addr-line>Mechanics and Materials Science Laboratory, Yamoussoukro, C&amp;amp;#244;te d’Ivoire</addr-line></aff><aff id="aff3"><addr-line>Civil Engineering, Geoscience and Geographic Sciences Laboratory, Yamoussoukro, C&amp;amp;#244;te d’Ivoire</addr-line></aff><pub-date pub-type="epub"><day>14</day><month>07</month><year>2021</year></pub-date><volume>09</volume><issue>04</issue><fpage>345</fpage><lpage>361</lpage><history><date date-type="received"><day>27,</day>	<month>April</month>	<year>2021</year></date><date date-type="rev-recd"><day>13,</day>	<month>July</month>	<year>2021</year>	</date><date date-type="accepted"><day>16,</day>	<month>July</month>	<year>2021</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>
 
 
  To produce high-purity silica sand usable for glass making, the present study was carried out. The objective of this work was to increase the silicon dioxide (SiO
  <sub>2</sub>) content to at least 99% using a simple process without chemical input. The raw sand samples were taken from the Ivorian sedimentary basin, from Maf&#233;r&#233; and Assinie areas, C
  &amp;#244;te d’Ivoire. Wet sieving and attrition technique were used for the purification process. The results from the energy dispersive spectrometer (EDS) analyses of the raw and treated samples show a significant increase of silica content and a significant reduction of impurities. The silica content (SiO
  <sub>2</sub>) of the sand of Maf&#233;r&#233; increases from 98.73% &#177; 0.15% to 99.92% &#177; 0.05%. And the sand of Assinie increased from 98.82% &#177; 0.67% in the raw samples to 99.44% &#177; 0.27% after treatment. The rate of iron oxide and alumina is reduced in these sands. Moreover, the sand of Maf&#233;r&#233; contains 53.2% of grains of size lower than 500 microns and that of Assinie contains 29.30%. Regarding the chemical composition of these purified sands, they meet the standard BS2975s, the American Ceramic Society and the National Bureau of Standards for window glass making.
 
</p></abstract><kwd-group><kwd>Silica Sand</kwd><kwd> Silicon Oxide</kwd><kwd> Attrition</kwd><kwd> Wet Sieving</kwd><kwd> Soda Lime Glass</kwd><kwd> Maf&#233;r&#233;</kwd><kwd> Assinie</kwd><kwd> C&#244;te d’Ivoire</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Window glass making requires the use of very pure silica sand without impurities [<xref ref-type="bibr" rid="scirp.110611-ref1">1</xref>]. Other domains such as photovoltaic cell production, silicon metal wafers, and optical glass are also dependent on good quality silica [<xref ref-type="bibr" rid="scirp.110611-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref3">3</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref4">4</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref6">6</xref>]. The BS2975 (British Standards International) specification published in 2008 specifies the silicon oxide (silica) content and the limits of iron, chromium, and titanium oxides in good quality silica sands. However, natural silica can be used if it meets the quality requirements of the standards [<xref ref-type="bibr" rid="scirp.110611-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref8">8</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref9">9</xref>]. According to this standard, there are three distinct grades of sand named A, B and C. Grade A contains a maximum of 0.008% Fe<sub>2</sub>O<sub>3</sub>, 0.030% TiO<sub>2</sub>, 2 ppm Cr<sub>2</sub>O<sub>3</sub> and a minimum of 99.5% silica, Grade B sand contains a minimum of 99.5% silicon oxide and a maximum of 0.013% Fe<sub>2</sub>O<sub>3</sub> and 2 ppm Cr<sub>2</sub>O<sub>3</sub>, while Grade C contains a minimum of 98.5% SiO<sub>2</sub>, a maximum of 0.035% Fe<sub>2</sub>O<sub>3</sub> and 6 ppm Cr<sub>2</sub>O<sub>3</sub> [<xref ref-type="bibr" rid="scirp.110611-ref9">9</xref>]. Grade A sand is used for the manufacture of optical glass, Grade B sand is used for the manufacture of household objects and colored glass. Grade C sand, suitable for the manufacture of color less containers etc., should have a maximum Fe<sub>2</sub>O<sub>3</sub> content of 0.030% and not more than 6 ppm Cr<sub>2</sub>O<sub>3</sub>. There is a proviso that the Fe<sub>2</sub>O<sub>3</sub> specification can be relaxed to 0.035% maximum if the sand contains less than 2 ppm Cr<sub>2</sub>O<sub>3</sub>. A minimum SiO<sub>2</sub> content of 98.5% is specified.</p><p>Previous work has led to the discovery of silica sand (S.S) with a high silica content in the Ivorian sedimentary basin [<xref ref-type="bibr" rid="scirp.110611-ref10">10</xref>]. The sands with a high proportion of silicon oxide (silica) are found east of Abidjan up to the border with Ghana. In the locality of Maf&#233;r&#233;, Aboisso region, C&#244;te d’Ivoire, siliceous sands are found with an average silica content of 97.41%. These sands are fine with 66.8% of the grains less than or equal to 500 microns in size. The quality of these sands is suitable to produce silica glass [<xref ref-type="bibr" rid="scirp.110611-ref10">10</xref>].</p><p>However, pure sand with a silica content of 98% or more is required to produce window glass. Highly pure silica sands with a silica content of more than 99.00% are required to produce optical glass and for the manufacture of photovoltaic cells. In this perspective, this study was carried out to propose a method of simple treatment, without the use of chemical products on the said sands. Thus, after the sampling phase, treatment of the samples was carried out in the laboratory using only wet sieving and attrition.</p></sec><sec id="s2"><title>2. Material and Methods</title><sec id="s2_1"><title>2.1. Collection and Conservation of Samples</title><p>The sampling phase was done according to the method described in our previous work [<xref ref-type="bibr" rid="scirp.110611-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref11">11</xref>]. Samples were taken with an auger at a depth of 50 centimeters. Composite sand samples (S.S)<sub>0</sub> of 1050 grams were collected in Maf&#233;r&#233; and Assinie, C&#244;te d’Ivoire. <xref ref-type="fig" rid="fig1">Figure 1</xref> illustrates the location of the sampling sites. The samples were transported to the laboratory in canvas bags free of any contamination at room temperature.</p></sec><sec id="s2_2"><title>2.2. Sample Preparation for the Analysis Phase</title><p>In the laboratory, a fraction of 750 grams of each sample (S.S)<sub>0</sub> was dried. The drying was done at 105 degrees Celsius to constant mass. After cooling in the desiccator, a weight of 50 gram of each raw sample was pulverized (to a 75 micrometers particle size) for chemical composition analysis by energy dispersive spectrometer (EDS). Thereafter, 500 grams of each dried sample was used for particle size analysis. Finally, 200 grams of the raw samples (S.S)<sub>0</sub> was utilized for the processing phase.</p></sec><sec id="s2_3"><title>2.3. Wet Sieving and Attrition Technique</title><p>The processing procedure begins with wet sieving of 200 g of the raw samples (S.S)<sub>0</sub> with distilled water using a one-millimeter mesh size for removal of coarse particles and debris. The passing at this mesh is sifted, still in wet way, to 80 microns for the elimination of the fine clayey fraction and limestones. Thereafter, with the refusal of the sieve to 80 microns the attrition is carried out using the device of <xref ref-type="fig" rid="fig2">Figure 2</xref>. The equipment consists of a plastic test tube and an electric agitator used to shake the contents of the test tubes.</p><p>Attrition is the most common enrichment method for sand enrichment [<xref ref-type="bibr" rid="scirp.110611-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref14">14</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref15">15</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref16">16</xref>]. In this study, we introduce the 80 microns refusals of each sample into test tubes. Then, 300 milliliters of distilled water were added, and the test tubes were closed tightly. Finally, the mixture of sand and distilled water was agitated by a stirring machine that performs an oscillatory movement (180 oscillations per minute), with an amplitude of 20 centimeters. This movement creates friction between the sand grains.</p><p>The attrition was carried out in two cycles for 15 minutes each [<xref ref-type="bibr" rid="scirp.110611-ref14">14</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref17">17</xref>]. At the end of each 15-minute attrition sequence, the contents of the attrition vessel are sieved to 80 microns with distilled water.</p><p>The nomenclature of sand samples adopted in this manuscript is as follows: (S.S)<sub>(</sub><sub>i</sub><sub>,j</sub><sub>)</sub> with, i = {MAF; ASS}: sampling sites and j ∈ 〚 0 ; 1 〛 : processing level. The <xref ref-type="table" rid="table1">Table 1</xref> is the summary of the sample nomenclature.</p><p>The product of the last sieving carried out is oven dried. The schematic of the processing protocol is shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>.</p><p>Finally, a 50-grams fraction of the treated and dried sands is ground for chemical composition analysis.</p></sec><sec id="s2_4"><title>2.4. Analysis of the Samples</title><p>Several analyses were carried out on the sand samples. First, the chemical composition of the raw and treated sands was analyzed using the energy dispersive spectrometer (EDS). Then, the granularity of the raw sands was determined. Finally, the micrography of the quartz grains is performed by Scanning Electron Microscope (SEM).</p><p>Energy Dispersive Spectrometer (EDS)</p><p>Energy dispersive spectroscopy (EDS) provides elemental and chemical analysis of samples [<xref ref-type="bibr" rid="scirp.110611-ref18">18</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref19">19</xref>]. We use the crushed material of each sample (raw and processed) for the determination of the chemical composition. The principle of this analysis is to first ionize the atoms of the samples. Then the instrument measures the intensity and energy of the X-rays emitted by the atoms. The results of this method are the chemical composition and emission spectra of each sample.</p><p>Granulometric analysis</p><p>A weight of 500 grams of each previously dried crude was used. A series of AFNOR sieves (80 μm, 100 μm, 125 μm, 160 μm, 200 μm, 250 μm, 315 μm, 400 μm, 500 μm, 630 μm, 800 &#181;m, 1 mm, 1 mm. 25 mm, 1.6 mm, 2 mm, 2.5 mm) are used. The column is placed on a vibrating sieve machine for 10 minutes. Each sieve reject is weighed for determination of the proportions of pass and reject [<xref ref-type="bibr" rid="scirp.110611-ref11">11</xref>].</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Nomenclature of raw and processed samples</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Designation</th><th align="center" valign="middle" >Raw samples</th><th align="center" valign="middle" >Processed samples</th></tr></thead><tr><td align="center" valign="middle" >MAF: Maf&#233;r&#233;</td><td align="center" valign="middle" >(S.S)<sub>MAF,0</sub></td><td align="center" valign="middle" >(S.S)<sub>MAF,1</sub></td></tr><tr><td align="center" valign="middle" >ASS: Assinie</td><td align="center" valign="middle" >(S.S)<sub>ASS,0</sub></td><td align="center" valign="middle" >(S.S)<sub>ASS,1</sub></td></tr></tbody></table></table-wrap><p>Data from the particle size analysis are used for sand characterization. We use the method of statistical moments and that of Folk and Ward. These methods are described in the article by Blott and Pye [<xref ref-type="bibr" rid="scirp.110611-ref20">20</xref>]. They proposed a macro running under Microsoft Excel<sup>&#169;</sup> (GRADISTATv9.1xlsm) for the characterization of samples based on the particle size analysis. The good grading of the sands is also evaluated using the indices from the method of moments and the Folk and Ward method. These are parameters such as: means, mode(s), standard deviation, skewness, kurtosis, and a range of values of cumulative percentiles (the grain size at which a specified percentage of the grains are coarser), namely D<sub>10</sub>, D<sub>50</sub>, D<sub>90</sub>.</p><p>The particle size scale used was proposed by Blott [<xref ref-type="bibr" rid="scirp.110611-ref11">11</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref20">20</xref>]. <xref ref-type="table" rid="table2">Table 2</xref> illustrates the nomenclature of grain size classes. Grain sizes are expressed in mm (x<sub>mm</sub><sub>)</sub> or μm (x<sub>μm</sub><sub>)</sub> but also in phi (ϕ). The relationship between these units’ systems is established by the following expression:</p><p>x<sub>ϕ</sub> = −log<sub>2</sub>(x<sub>mm</sub>).</p><p>Processing weight efficiency</p><p>Next, we evaluate the yield (η) of the processing method for raw sand samples.</p><p>The adopted calculation method is illustrated by the formulas in <xref ref-type="table" rid="table3">Table 3</xref> and in <xref ref-type="table" rid="table4">Table 4</xref>. We use the results of the spectrometric analysis to calculate the different yields.</p><p>These formulas, <xref ref-type="table" rid="table3">Table 3</xref>, and <xref ref-type="table" rid="table4">Table 4</xref> consider the objective of silica sand treatment, which is to increase the silica content to 100% by removing impurities [<xref ref-type="bibr" rid="scirp.110611-ref21">21</xref>]. Indeed, a treatment method would be efficient (ideal) if it allows the reduction of impurities to 0% and raises the silica content to 100%. Thus, we calculated the yield on the silica content by the ratio of the difference between the final proportion (example T<sub>(</sub><sub>silica)MAF,1</sub>) and the initial proportion (example T<sub>(silica)MAF,0</sub>) and the difference between 100% and the initial proportion (example T<sub>(silica)MAF,0</sub>). For the impurities, the calculation of the yield was using the difference between 0% and the initial proportion (example T<sub>(</sub><sub>silica)MAF,0</sub>) in the denominator.</p><p>Scanning Electron Microscope (SEM)</p><p>Exoscopy allows us to observe and interpret this surface condition by analyzing images taken by scanning electron microscopy (SEM), at magnifications typically between &#215;500 and &#215;20,000. Nearly 250 characters have been listed [<xref ref-type="bibr" rid="scirp.110611-ref22">22</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref23">23</xref>]. They allow to determine the depositional environment of a grain, its history and sometimes its geographical origin. It is strongly recommended that the 250 - 355 μm fraction be preferred [<xref ref-type="bibr" rid="scirp.110611-ref11">11</xref>].</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Size scale proposed by Blott</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  colspan="2"  >Grain size</th><th align="center" valign="middle"  colspan="2"   rowspan="2"  >Descriptive terminology</th></tr></thead><tr><td align="center" valign="middle" >phi</td><td align="center" valign="middle" >mm/&#181;m</td></tr><tr><td align="center" valign="middle" >−6 to −5</td><td align="center" valign="middle" >32mm - 64 mm</td><td align="center" valign="middle" >Very coarse</td><td align="center" valign="middle"  rowspan="5"  >Gravel</td></tr><tr><td align="center" valign="middle" >−5 to −4</td><td align="center" valign="middle" >16 - 32</td><td align="center" valign="middle" >coarse</td></tr><tr><td align="center" valign="middle" >−4 to −3</td><td align="center" valign="middle" >8 - 16</td><td align="center" valign="middle" >Medium</td></tr><tr><td align="center" valign="middle" >−3 to −2</td><td align="center" valign="middle" >4 - 8</td><td align="center" valign="middle" >Fine</td></tr><tr><td align="center" valign="middle" >−2 to −1</td><td align="center" valign="middle" >2 - 4</td><td align="center" valign="middle" >Very fine</td></tr><tr><td align="center" valign="middle" >−1 to 0</td><td align="center" valign="middle" >1 - 2</td><td align="center" valign="middle" >Very coarse</td><td align="center" valign="middle"  rowspan="5"  >Sand</td></tr><tr><td align="center" valign="middle" >0 - 1</td><td align="center" valign="middle" >500 &#181;m - 1 mm</td><td align="center" valign="middle" >Coarse</td></tr><tr><td align="center" valign="middle" >1 - 2</td><td align="center" valign="middle" >250 &#181;m - 500 &#181;m</td><td align="center" valign="middle" >Medium</td></tr><tr><td align="center" valign="middle" >2 - 3</td><td align="center" valign="middle" >125 - 250</td><td align="center" valign="middle" >Fine</td></tr><tr><td align="center" valign="middle" >3 - 4</td><td align="center" valign="middle" >63 - 125</td><td align="center" valign="middle" >Very fine</td></tr></tbody></table></table-wrap><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Calculation of the yield of the treatment performed for Sand sample of Maf&#233;r&#233;</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Compound</th><th align="center" valign="middle" >yield of the treatment performed (η)</th></tr></thead><tr><td align="center" valign="middle" >Sand sample of Maf&#233;r&#233;</td></tr><tr><td align="center" valign="middle" >Silica</td><td align="center" valign="middle" >η<sub>(silica)</sub> = [T<sub>(silica)MAF,1</sub> − T<sub>(silica)MAF,0</sub>]/[100 − T<sub>(silica)MAF,0)</sub>] &#215; 100</td></tr><tr><td align="center" valign="middle" >Iron oxide</td><td align="center" valign="middle" >η<sub>(iron)</sub> = [T<sub>(iron)MAF,1</sub> − T<sub>(iron)MAF,0</sub>]/[0 − T<sub>(iron)MAF,0</sub>] &#215; 100</td></tr><tr><td align="center" valign="middle" >Alumina</td><td align="center" valign="middle" >η<sub>(alumina)</sub> = [T<sub>(alumina)MAF,1</sub> − T<sub>(alumina)MAF,0</sub>]/[0 − T<sub>(alumina)MAF,0</sub>] &#215; 100</td></tr></tbody></table></table-wrap><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Calculation of the yield of the treatment performed for Sand sample of Assinie</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Compound</th><th align="center" valign="middle" >yield of the treatment performed (η)</th></tr></thead><tr><td align="center" valign="middle" >Sand sample of Maf&#233;r&#233;</td></tr><tr><td align="center" valign="middle" >Silica</td><td align="center" valign="middle" >η<sub>(silica)</sub> = [T<sub>(silica)ASS,1</sub> − T<sub>(silica)ASS,0</sub>]/[100 − T<sub>(silica)ASS,0)</sub>] &#215; 100</td></tr><tr><td align="center" valign="middle" >Iron oxide</td><td align="center" valign="middle" >η<sub>(iron)</sub> = [T<sub>(iron)ASS,1</sub> − T<sub>(iron)ASS,0</sub>]/[0 − T<sub>(iron)ASS,0</sub>] &#215; 100</td></tr><tr><td align="center" valign="middle" >Alumina</td><td align="center" valign="middle" >η<sub>(alumina)</sub> = [T<sub>(alumina)ASS,1</sub> − T<sub>(alumina)ASS,0</sub>]/[0 − T<sub>(alumina)ASS,0</sub>] &#215; 100</td></tr></tbody></table></table-wrap></sec></sec><sec id="s3"><title>3. Results and Discussion</title><p>At the end of the implementation and the different analyses carried out on the sand samples, some results were found.</p><sec id="s3_1"><title>3.1. Particle Size Analysis</title><p>Glass production requires sand with a fine grain size of about 200 microns to 500 microns [<xref ref-type="bibr" rid="scirp.110611-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref14">14</xref>]. <xref ref-type="fig" rid="fig4">Figure 4</xref> and <xref ref-type="fig" rid="fig5">Figure 5</xref> represent the graphical results of the particle size analysis of the sands of Maf&#233;r&#233; and Assinie respectively. These figures show the proportions of passing on the sieves of the AFNOR series (from 80 microns to 2.5 millimeters).</p><p>The grain size distribution of Maf&#233;r&#233; sand is bimodal with one modal value at 450 micrometers and the other at 715 micrometers (respectively ϕ = 0.494 and ϕ = 1.61) (see <xref ref-type="fig" rid="fig4">Figure 4</xref> and <xref ref-type="table" rid="table5">Table 5</xref>). Other position indices such as D<sub>10</sub> and D<sub>90</sub> are equal to 206 (ϕ = 0.403) micrometers and 756 micrometers (ϕ = 2.278) respectively.</p><p>Also, in the Sand-Clay-Silt diagram, the Maf&#233;r&#233; sample is a sand containing 53.2% of grains smaller than 500 microns (<xref ref-type="fig" rid="fig6">Figure 6</xref>). There are 26.6% of grains between 250 microns and 500 microns in this sand.</p><p>Furthermore, according to the indices calculated by the method of moments and by the method of Folk and Ward (see <xref ref-type="table" rid="table6">Table 6</xref>), the sand of Maf&#233;r&#233; is a medium sand, moderately sorted. The fine granularity of the sand up to 125 microns is suitable for glass production [<xref ref-type="bibr" rid="scirp.110611-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.110611-ref13">13</xref>].</p><table-wrap id="table5" ><label><xref ref-type="table" rid="table5">Table 5</xref></label><caption><title> Statistical parameters of position of Maf&#233;r&#233; sand and Assinie Sand</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Sample</th><th align="center" valign="middle" >D<sub>10</sub></th><th align="center" valign="middle" >Median (D5<sub>0</sub>)</th><th align="center" valign="middle" >Mode(s)</th><th align="center" valign="middle" >D<sub>90</sub></th></tr></thead><tr><td align="center" valign="middle" >(S.S)<sub>MAF,1</sub></td><td align="center" valign="middle" >206 &#181;m</td><td align="center" valign="middle" >474 &#181;m</td><td align="center" valign="middle" >450 &#181;m and 715 &#181;m</td><td align="center" valign="middle" >756 &#181;m</td></tr><tr><td align="center" valign="middle" >(S.S)<sub>ASS,1</sub></td><td align="center" valign="middle" >372 &#181;m</td><td align="center" valign="middle" >624 &#181;m</td><td align="center" valign="middle" >715 &#181;m</td><td align="center" valign="middle" >924 &#181;m</td></tr></tbody></table></table-wrap><table-wrap id="table6" ><label><xref ref-type="table" rid="table6">Table 6</xref></label><caption><title> Parameters of the method of moments and the method of Folk and Ward of Maf&#233;r&#233; sand</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Parameters</th><th align="center" valign="middle"  colspan="3"  >Method of moments</th><th align="center" valign="middle"  colspan="2"  >Folk and Ward’s method</th><th align="center" valign="middle"  rowspan="2"  >Description</th></tr></thead><tr><td align="center" valign="middle" >Arithmetic (&#181;m)</td><td align="center" valign="middle" >Geometric (&#181;m)</td><td align="center" valign="middle" >Logarithmic phi (ϕ)</td><td align="center" valign="middle" >Geometric (&#181;m)</td><td align="center" valign="middle" >Logarithmic phi (ϕ)</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >492.663</td><td align="center" valign="middle" >434.026</td><td align="center" valign="middle" >1.204</td><td align="center" valign="middle" >438.087</td><td align="center" valign="middle" >1.191</td><td align="center" valign="middle" >Medium Sand</td></tr><tr><td align="center" valign="middle" >Sorting</td><td align="center" valign="middle" >225.084</td><td align="center" valign="middle" >1.676</td><td align="center" valign="middle" >0.745</td><td align="center" valign="middle" >1.658</td><td align="center" valign="middle" >0.730</td><td align="center" valign="middle" >Moderately Sorted</td></tr><tr><td align="center" valign="middle" >Skewness</td><td align="center" valign="middle" >0.726</td><td align="center" valign="middle" >−0.645</td><td align="center" valign="middle" >0.645</td><td align="center" valign="middle" >−0.288</td><td align="center" valign="middle" >0.288</td><td align="center" valign="middle" >Fine Skewed</td></tr><tr><td align="center" valign="middle" >Kurtosis</td><td align="center" valign="middle" >6.062</td><td align="center" valign="middle" >2.845</td><td align="center" valign="middle" >2.845</td><td align="center" valign="middle" >0.817</td><td align="center" valign="middle" >0.817</td><td align="center" valign="middle" >Platykurtic</td></tr></tbody></table></table-wrap><p>In the case of the Assinie sample, its particle size distribution is unimodal. The modal value is 715 micrometers (respectively ϕ = 0.494) (see <xref ref-type="fig" rid="fig7">Figure 7</xref> and <xref ref-type="table" rid="table7">Table 7</xref>). Other positional indices such as D<sub>10</sub> and D<sub>90</sub> are equal to 372 (ϕ = 0.114) micrometers and 924 micrometers (ϕ = 1.425) respectively.</p><p>In the Sand-Clay-Silt diagram, the Assinie sample is a sand containing 29.3% of grains smaller than 500 microns. The proportion of fine phase is very low. There are 0.7% of grains between 250 microns and 500 microns in this sand (<xref ref-type="fig" rid="fig7">Figure 7</xref>).</p><p>Moreover, regarding the indices calculated by the method of moments and by the method of Folk and Ward, the sand of Assinie is well sorted around the average diameter. The characteristic curve of its histogram is of mesokurtic form. This sand is coarser than that of Maf&#233;r&#233; (see <xref ref-type="table" rid="table4">Table 4</xref>).</p><p>Thus, the sand from Maf&#233;r&#233; would be more useful for glass production than that from Assinie. In addition to the granularity of these sands, we are interested in the chemical composition of these sands.</p><table-wrap id="table7" ><label><xref ref-type="table" rid="table7">Table 7</xref></label><caption><title> Parameters of the method of moments and the method of Folk and Ward of Assinie sand</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Parameters</th><th align="center" valign="middle"  colspan="3"  >Method of moments</th><th align="center" valign="middle"  colspan="2"  >Folk and Ward’s method</th><th align="center" valign="middle"  rowspan="2"  >Description</th></tr></thead><tr><td align="center" valign="middle" >Arithmetic (&#181;m)</td><td align="center" valign="middle" >Geometric (&#181;m)</td><td align="center" valign="middle" >Logarithmic phi (ϕ)</td><td align="center" valign="middle" >Geometric (&#181;m)</td><td align="center" valign="middle" >Logarithmic phi (ϕ)</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >642.7</td><td align="center" valign="middle" >598.7</td><td align="center" valign="middle" >0.740</td><td align="center" valign="middle" >590.8</td><td align="center" valign="middle" >0.759</td><td align="center" valign="middle" >Coarse Sand</td></tr><tr><td align="center" valign="middle" >Sorting</td><td align="center" valign="middle" >235.5</td><td align="center" valign="middle" >1.415</td><td align="center" valign="middle" >0.501</td><td align="center" valign="middle" >1.408</td><td align="center" valign="middle" >0.494</td><td align="center" valign="middle" >Well Sorted</td></tr><tr><td align="center" valign="middle" >Skewness</td><td align="center" valign="middle" >1.524</td><td align="center" valign="middle" >−0.090</td><td align="center" valign="middle" >0.090</td><td align="center" valign="middle" >−0.164</td><td align="center" valign="middle" >0.164</td><td align="center" valign="middle" >Fine Skewed</td></tr><tr><td align="center" valign="middle" >Kurtosis</td><td align="center" valign="middle" >8.766</td><td align="center" valign="middle" >3.372</td><td align="center" valign="middle" >3.372</td><td align="center" valign="middle" >1.089</td><td align="center" valign="middle" >1.089</td><td align="center" valign="middle" >Mesokurtic</td></tr></tbody></table></table-wrap></sec><sec id="s3_2"><title>3.2. Chemical Composition of Sedimentary Basin Sand</title><p>The results of the chemical composition analysis of the samples are shown in <xref ref-type="table" rid="table8">Table 8</xref> and <xref ref-type="table" rid="table9">Table 9</xref>. Three analyses were performed for each sample.</p><table-wrap id="table8" ><label><xref ref-type="table" rid="table8">Table 8</xref></label><caption><title> Chemical composition of raw and treated sands from Maf&#233;r&#233;</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  colspan="4"  >(S.S)<sub>MAF,0 </sub></th></tr></thead><tr><td align="center" valign="middle"  rowspan="2"  >Parameters</td><td align="center" valign="middle"  colspan="3"  >Chemical compound</td></tr><tr><td align="center" valign="middle" >Al<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >FeO/Fe<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >SiO<sub>2</sub> (%)</td></tr><tr><td align="center" valign="middle" >sample 1</td><td align="center" valign="middle" >0.18</td><td align="center" valign="middle" >0.99</td><td align="center" valign="middle" >98.83</td></tr><tr><td align="center" valign="middle" >sample 2</td><td align="center" valign="middle" >0.24</td><td align="center" valign="middle" >0.97</td><td align="center" valign="middle" >98.79</td></tr><tr><td align="center" valign="middle" >sample 3</td><td align="center" valign="middle" >0.59</td><td align="center" valign="middle" >0.86</td><td align="center" valign="middle" >98.56</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >0.33</td><td align="center" valign="middle" >0.94</td><td align="center" valign="middle" >98.73</td></tr><tr><td align="center" valign="middle" >Std. deviation</td><td align="center" valign="middle" >0.22</td><td align="center" valign="middle" >0.07</td><td align="center" valign="middle" >0.15</td></tr><tr><td align="center" valign="middle"  colspan="4"  >(S.S)<sub>MAF,1</sub></td></tr><tr><td align="center" valign="middle" ></td><td align="center" valign="middle" >Al<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >FeO/Fe<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >SiO<sub>2</sub> (%)</td></tr><tr><td align="center" valign="middle" >Sample 1</td><td align="center" valign="middle" >0.09</td><td align="center" valign="middle" >0.03</td><td align="center" valign="middle" >99.88</td></tr><tr><td align="center" valign="middle" >sample 2</td><td align="center" valign="middle" >0.09</td><td align="center" valign="middle" >0.01</td><td align="center" valign="middle" >99.90</td></tr><tr><td align="center" valign="middle" >sample 3</td><td align="center" valign="middle" >0.00</td><td align="center" valign="middle" >0.03</td><td align="center" valign="middle" >99.97</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >0.06</td><td align="center" valign="middle" >0.03</td><td align="center" valign="middle" >99.92</td></tr><tr><td align="center" valign="middle" >Std. deviation</td><td align="center" valign="middle" >0.06</td><td align="center" valign="middle" >0.01</td><td align="center" valign="middle" >0.05</td></tr></tbody></table></table-wrap><table-wrap id="table9" ><label><xref ref-type="table" rid="table9">Table 9</xref></label><caption><title> Chemical composition of raw and treated sands from Assinie</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  colspan="4"  >(S.S)<sub>ASS,0</sub></th></tr></thead><tr><td align="center" valign="middle"  rowspan="2"  >Parameters</td><td align="center" valign="middle"  colspan="3"  >Chemical compound</td></tr><tr><td align="center" valign="middle" >Al<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >FeO/Fe<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >SiO<sub>2</sub> (%)</td></tr><tr><td align="center" valign="middle" >sample 1</td><td align="center" valign="middle" >1.40</td><td align="center" valign="middle" >0.19</td><td align="center" valign="middle" >98.41</td></tr><tr><td align="center" valign="middle" >sample 2</td><td align="center" valign="middle" >0.17</td><td align="center" valign="middle" >0.24</td><td align="center" valign="middle" >99.59</td></tr><tr><td align="center" valign="middle" >sample 3</td><td align="center" valign="middle" >1.28</td><td align="center" valign="middle" >0.26</td><td align="center" valign="middle" >98.46</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >0.95</td><td align="center" valign="middle" >0.23</td><td align="center" valign="middle" >98.82</td></tr><tr><td align="center" valign="middle" >Std. deviation</td><td align="center" valign="middle" >0.68</td><td align="center" valign="middle" >0.04</td><td align="center" valign="middle" >0.67</td></tr><tr><td align="center" valign="middle"  colspan="4"  >(S.S)<sub>ASS,1</sub></td></tr><tr><td align="center" valign="middle" ></td><td align="center" valign="middle" >Al<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >FeO/Fe<sub>2</sub>O<sub>3</sub> (%)</td><td align="center" valign="middle" >SiO<sub>2</sub> (%)</td></tr><tr><td align="center" valign="middle" >Sample 1</td><td align="center" valign="middle" >0.87</td><td align="center" valign="middle" >0.00</td><td align="center" valign="middle" >98.94</td></tr><tr><td align="center" valign="middle" >sample 2</td><td align="center" valign="middle" >0.22</td><td align="center" valign="middle" >0.12</td><td align="center" valign="middle" >99.53</td></tr><tr><td align="center" valign="middle" >sample 3</td><td align="center" valign="middle" >0.22</td><td align="center" valign="middle" >0.26</td><td align="center" valign="middle" >99.61</td></tr><tr><td align="center" valign="middle" >Mean</td><td align="center" valign="middle" >0.44</td><td align="center" valign="middle" >0.13</td><td align="center" valign="middle" >99.44</td></tr><tr><td align="center" valign="middle" >Std. deviation</td><td align="center" valign="middle" >0.37</td><td align="center" valign="middle" >0.13</td><td align="center" valign="middle" >0.27</td></tr></tbody></table></table-wrap><p>Energy dispersive spectrometry revealed that the raw sand from Maf&#233;r&#233; contains 98.73% &#177; 0.15% silica. This sand also contains 0.94% &#177; 0.07% iron oxide and 0.33% &#177; 0.22% alumina. After treatment, the chemical composition of this sand changes. The proportion of mineral silica increases to 99.92% &#177; 0.05%. The content of other oxides is reduced. The iron oxide remains at 0.03% &#177; 0.01% in this sand. And there remains 0.06% &#177; 0.06% of alumina (see <xref ref-type="table" rid="table8">Table 8</xref>).</p><p>Moreover, the raw sand of Assinie contains 98.82% &#177; 0.67% silica. This sand also contains 0.23% &#177; 0.04% iron oxide and 0.95% &#177; 0.68% alumina. After processing, the chemical composition of this sand also changes. The proportion of mineral silica increases to 99.44% &#177; 0.27%. The content of other oxides was reduced while the iron oxide remains at 0.13% &#177; 0.13% and alumina at 0.44% &#177; 0.37% (see <xref ref-type="table" rid="table9">Table 9</xref>).</p><p>The chemical compositions revealed by energy dispersive spectrometry are illustrated by the spectra in <xref ref-type="fig" rid="fig8">Figure 8</xref> and <xref ref-type="fig" rid="fig9">Figure 9</xref>. These Figures showed the energy spectra of the six EDS analyses carried out on the sand of Maf&#233;r&#233; and Assinie respectively.</p><p>The energy bands (in yellow) are characteristic of the chemical compounds present in the samples. Iron (Fe) appears at several locations in these spectra. The multiple appearance of iron is explained by the fact that its detection depends on its degree of oxidation. Thus, it can be FeO, Fe<sub>2</sub>O<sub>3</sub> and Fe<sub>3</sub>O<sub>4</sub>. However, the proportion of iron in the samples is the accumulation of the rates of these different forms of oxidation detected.</p><p>Processing weight efficiency</p><p>The results of the performance evaluation of the treatment method employed using the formulas in <xref ref-type="table" rid="table3">Table 3</xref> and <xref ref-type="table" rid="table4">Table 4</xref> are in <xref ref-type="table" rid="table1">Table 1</xref>0.</p><p>Wet sieving with attrition increased the silica content from 98.73% to 99.92%, a yield of 93.7% for the Maf&#233;r&#233; sand, while for the sand of Assinie, the proportion of silica increases from 98.82% to 99.44%, a yield of 52.53% (see <xref ref-type="table" rid="table8">Table 8</xref>). The rate of impurities in the sand of Maf&#233;r&#233; is reduced from 0.94% to 0.03%, a yield of 96.81% for iron oxide, and a reduction from 0.33% to 0.06%, a yield of 81.82% for alumina.</p><table-wrap id="table10" ><label><xref ref-type="table" rid="table1">Table 1</xref>0</label><caption><title> Performance of the treatment method used</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Compound</th><th align="center" valign="middle"  colspan="2"  >Processing weight efficiency</th></tr></thead><tr><td align="center" valign="middle" >(MAF): Maf&#233;r&#233; Sample</td><td align="center" valign="middle" >(ASS): Assinie Sample</td></tr><tr><td align="center" valign="middle" >Silica</td><td align="center" valign="middle" >93.70%</td><td align="center" valign="middle" >52.53%</td></tr><tr><td align="center" valign="middle" >Iron oxide</td><td align="center" valign="middle" >96.81%</td><td align="center" valign="middle" >76.92%</td></tr><tr><td align="center" valign="middle" >Alumina</td><td align="center" valign="middle" >81.82%</td><td align="center" valign="middle" >53.68%</td></tr></tbody></table></table-wrap><p>In the sand of Assinie, the rate of impurities is also reduced after treatment. The content of iron oxide is reduced from 0.23% to 0.13%, a yield of 76.92%. A reduction from 0.95% to 0.44% is noted for alumina, a yield of 53.68%.</p><p>Considering these results, we note that the treatment technique used allows the increase in the content of silica while reducing that of the other oxides. Better results were obtained in this study with the sand of Maf&#233;r&#233; compared to the result obtained by Marouan Khalifa et al. (2019) in their process to produce high purity silica sand by heat treatment and acid leaching process [<xref ref-type="bibr" rid="scirp.110611-ref21">21</xref>]. In addition, all our treated samples have a higher silica content (at least 99%) than that of the samples obtained (98.1%) in the work of Sundararajan et al. (2009) [<xref ref-type="bibr" rid="scirp.110611-ref13">13</xref>].</p><p>In the following, we present images of the samples. Also, the grain morphology of the sands was evaluated using scanning electron microscope (SEM).</p><p>Micrography and Exoscopy of quartz grains</p><p><xref ref-type="fig" rid="fig1">Figure 1</xref>0 and <xref ref-type="fig" rid="fig1">Figure 1</xref>1 are images of the raw and processed samples from Assinie and Maf&#233;r&#233;. These images are visual indicators of the purification of these sands.</p><p>It was observed that the treated samples reflect more brightness (matte, vitreous) and color (white) of quartz (the natural silica). In the raw sand of Assinie, the treatment allows a notable reduction (as seen in <xref ref-type="fig" rid="fig1">Figure 1</xref>0) of the organic matter (dark fraction)</p><p>The raw sand from Maf&#233;r&#233; has less organic matter than the sand from Assinie (<xref ref-type="fig" rid="fig1">Figure 1</xref>1). However, there is more clay (very fine phase) in the sand of Maf&#233;r&#233;. The treatment reduces the proportion of clay and provides a sand containing clean quartz grains.</p><p>In addition, the SEM images below indicates the presence of different shapes of sand with irregular morphologies, for instance <xref ref-type="fig" rid="fig1">Figure 1</xref>2 and <xref ref-type="fig" rid="fig1">Figure 1</xref>3 show some rounded grains, whereas others are sub-rounded or elongated and sub-angular.</p><p>Generally, this indicates that the grains of these sands have undergone long transport, thereby, falls into the category of sands with blunt grains. Thus, these detritus have an origin further upstream in the crystalline basement of the C&#244;te d’Ivoire.</p><p>Furthermore, the surface of the quartz grains observed at X500 magnification (see <xref ref-type="fig" rid="fig1">Figure 1</xref>2(b); <xref ref-type="fig" rid="fig1">Figure 1</xref>3(b)) is marked by numerous traces. The existence of these traces suggests a displacement of these grains in a turbulent environment. The primary deposits of these quartz grains are found in the basement rocks further upstream from the sampling sites.</p></sec></sec><sec id="s4"><title>4. Conclusions</title><p>We have carried out a purification treatment of sand samples taken from the sedimentary basin of Ivory Coast in West Africa. The objective of this study was to obtain silica sand ideal to produce glazing glass. Wet sieving and attrition technique were implemented in this purification process. The results from the analysis of the chemical composition of the raw and treated samples show a significant increase in the silica content and a significant reduction of impurities. The silica content (SiO<sub>2</sub>) of the Maf&#233;r&#233; sand increased from 98.73% &#177; 0.15% to 99.92% &#177; 0.05%, i.e., a yield of 93.70%, while of Assinie increased from 98.82% &#177; 0.67% in the raw samples to 99.44% &#177; 0.27% after treatment, a yield of 52.53%. The rate of iron oxide is reduced from 96.81% for the sand of Maf&#233;r&#233; against 76.92% for that of Assinie. Also, the proportion of alumina is reduced by 81.82% against 53.68% for the sand of Maf&#233;r&#233; and Assinie respectively. The sand of Maf&#233;r&#233; contains 53.2% of grains smaller than 500 microns and that of Assinie contains 29.30%. The technique of treatment used is more effective for the sand of Maf&#233;r&#233; containing more clay. Regarding the chemical composition of the said purified sands, they comply with the standard BS2975s of the American Ceramic Society and the National Bureau of Standards for the manufacture of window glass.</p><p>These results pave the way for feasibility studies for the opening of a sand quarry on these sites.</p></sec><sec id="s5"><title>Conflicts of Interest</title><p>The authors declare no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s6"><title>Cite this paper</title><p>Thio, P.R., Koffi, K.B., Konan, K.D. and Yao, K.A. (2021) Production of High-Purity Silica Sand from Ivorian Sedimentary Basin by Attrition without Acid Leaching Process for Windows Glass Making. 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