<?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">OJG</journal-id><journal-title-group><journal-title>Open Journal of Geology</journal-title></journal-title-group><issn pub-type="epub">2161-7570</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ojg.2018.89049</article-id><article-id pub-id-type="publisher-id">OJG-86459</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>
 
 
  Copper Oxide Ore Leaching Ability and Cementation Behavior, Mesgaran Deposit in IRAN
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Shayan</surname><given-names>Khakmardan</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>Aref</surname><given-names>Shirazi</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>Adel</surname><given-names>Shirazy</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Hassan</surname><given-names>Hosseingholi</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib></contrib-group><aff id="aff3"><addr-line>Sormak Mining Company, Tehran, Iran</addr-line></aff><aff id="aff2"><addr-line>Shahrood University of Technology, Shahrood, Iran</addr-line></aff><aff id="aff1"><addr-line>AmirKabir University of Technology (Tehran Polytechnic), Tehran, Iran</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>adel.shirazy@gmail.com(AS)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>03</day><month>08</month><year>2018</year></pub-date><volume>08</volume><issue>09</issue><fpage>841</fpage><lpage>858</lpage><history><date date-type="received"><day>16,</day>	<month>July</month>	<year>2018</year></date><date date-type="rev-recd"><day>31,</day>	<month>July</month>	<year>2018</year>	</date><date date-type="accepted"><day>3,</day>	<month>August</month>	<year>2018</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>
 
 
  One of the Iranian copper deposits that is located east of Iran and also known as a primeval one in that area is Mesgaran Field. Old mining works have been clearly seen in the area. Iran is located on global copper belt and as a result it has numerous potential areas as copper deposits. The purpose of this study is identifying possible potentialities of copper mining in less developed regions of Iran with basic modern technologies. In this study, laboratory investigations of this field were done on samples via leaching and the cementation method. According to the study purposes, acid concentration, temperature, time and pulp density were selected as the main factors that were tested in leaching studies. Moreover, pH, temperature, time and the amount of iron powder were factors which were tested for copper cementation. Optimum conditions of leaching studies with 99.11% recovery rate were obtained after 120 grams per liter of H
  <sub>2</sub>SO
  <sub>4</sub>, 80 degrees Celsius, 2 hours and 100 grams per liter of solid to liquid. On the other hand, optimum conditions of cementation by iron powder were resulted at more than 95% with a pH of 3, 45 degrees Celsius, 1 hour and 1.5 times more than the stoichiometric equation of required iron powder amount to precipitate copper.
 
</p></abstract><kwd-group><kwd>Leaching</kwd><kwd> Cementation</kwd><kwd> Copper Oxide</kwd><kwd> Malachite</kwd><kwd> VMS Copper Deposit</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Mineral processing studies begin from initial exploration stage. As in the exploration using the geostatistics and the detection of the anomalous elements of the economic mineralization in the region [<xref ref-type="bibr" rid="scirp.86459-ref1">1</xref>] , it should be confirmed by analyzing the scale of the laboratory and generalizing it to the industrial scale of the economic existence of these minerals [<xref ref-type="bibr" rid="scirp.86459-ref2">2</xref>]. Remote sensing was used earlier in the initial investigations of the Mesgaran area for potential and detection of general alterations and lithology [<xref ref-type="bibr" rid="scirp.86459-ref3">3</xref>]. And the mineral anomalies of the area were also separated by statistical methods [<xref ref-type="bibr" rid="scirp.86459-ref4">4</xref>]. Copper extraction from raw materials is obtained by two main methods, Pyrometallurgy and Hydrometallurgy [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>]. About 80% copper-from-ore is obtained by flotation, smelting and refining; nearly all sulfide type minerals such as Chalcopyrite, Covellite, Chalcocite and Bornite processed by this method which is known as the pyrometallurgy method [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref6">6</xref>]. The remaining copper minerals proportion is called oxide types, and is treated by acid and bases reagents in the hydrometallurgy method [<xref ref-type="bibr" rid="scirp.86459-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref8">8</xref>].</p><p>Nowadays, sulfide minerals are not as pure as 50 years ago to smelt directly in a flash furnace and as a result, these low grade raw materials (less than 1% Copper included) should be processed by the flotation method to reach to an acceptable grade (more than 22% Copper included). After this step, matte smelting, matte converting and refining are applied to the product of the flotation step to obtain copper with more than 99% purity [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref6">6</xref>].</p><p>Oxide minerals as described formerly can be treated by the hydrometallurgy method that contains three main steps 1) Leaching, 2) Solvent Extraction (SX) and 3) Electrowinning (EW) [<xref ref-type="bibr" rid="scirp.86459-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref10">10</xref>] There are other methods to recover copper after leaching [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>]. Cementation and Ion Exchange (IX) are the two main methods [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref7">7</xref>]. Cementation is the basic method of hydrometallurgy that was applied by alchemists many years ago [<xref ref-type="bibr" rid="scirp.86459-ref6">6</xref>]. Cementation is not the most economical, fastest and selective way to recover copper; however it is the cheapest method besides being easy to operate [<xref ref-type="bibr" rid="scirp.86459-ref11">11</xref>].</p><p>Sulfuric Acid (H<sub>2</sub>SO<sub>4</sub>) is the most common chemical reagent that is used for the leaching of oxide minerals including copper ones [<xref ref-type="bibr" rid="scirp.86459-ref5">5</xref>]. Among the most important factors of leaching are reagent type, temperature, time and pulp density [<xref ref-type="bibr" rid="scirp.86459-ref12">12</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref13">13</xref>].</p><p>The principle of cementation is based on electrochemical differences between ions capacity. Lead, Iron, Zinc and Aluminum are respectively the best metals that can recover copper from PLS [<xref ref-type="bibr" rid="scirp.86459-ref6">6</xref>]. Cementation is widely used for Gold recovery from PLS by Zinc powder [<xref ref-type="bibr" rid="scirp.86459-ref14">14</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref15">15</xref>].</p><p>This technical note is to report and document initial experimental findings that could lead to a new understanding of the role of Sulfuric Acid in the recovery of copper from oxide minerals.</p></sec><sec id="s2"><title>2. Data and Analytical Procedures</title><sec id="s2_1"><title>2.1. Geolocation of Mesgaran Copper Deposit</title><p>Mesgaran Copper Field is located 29 km south of Sarbisheh City, east of Iran. Accessibility to the field is possible via Nehbandan-Sarbisheh Road. There is no rough topographic area in the field and nearly all of the field is accessible by usual cars. The geological structure of the area contains of mafic and ultramafic rocks. This field is a part of the Gold zone of Ahangaran-Bandan metallogenic province (<xref ref-type="fig" rid="fig1">Figure 1</xref>) [<xref ref-type="bibr" rid="scirp.86459-ref16">16</xref>].</p></sec><sec id="s2_2"><title>2.2. Ore Geology and Mineralization</title><p>In Mesgaran mining area Copper mineralization has occurred in pillow-lava and andesite-basalt sequences of eastern Iran (<xref ref-type="fig" rid="fig2">Figure 2</xref>). Two mineralization zones were identified as sulfide mineralization with silicified stockworks (primary mineralization) and supergene mineralization. The primary copper mineralization in this region is mostly in accordance to silicified or carbonate veins with epidote and chlorite in volcanic basalt [<xref ref-type="bibr" rid="scirp.86459-ref3">3</xref>].</p><p>These veins cross out the volcanic complex as stockworks which include Chalcopyrite, Bournite and Pyrite. In this region, we observed no evidence proving massive deposit or lens shape deposit creation. The main observed minerals</p><p>are sulfide and oxide forms of copper. Malachite, Azurite and lower amounts of Tenorite and native copper in oxide supergene zone and chalcopyrite and bournite as the primary sulfides have been detected. Oxidation and erosion caused geotite and hematite around sulfide minerals like Chalcopyrite and Pyrite (<xref ref-type="fig" rid="fig3">Figure 3</xref>). Alteration is observed almost everywhere on the surface but the degree of alteration varies. Generally alteration occurs when rocks react to hydrothermal and magmatic fluids and this reaction leads to chemical and mineralogic changes. Chlorite alteration has occurred in large scale which is a specific form of Propylitic alteration. Al, Fe and Mg rich fluids cased chlorite alteration in basic rocks [<xref ref-type="bibr" rid="scirp.86459-ref18">18</xref>].</p><p>In this region, argillic alteration (presence of Montmorillonite mineral) as a secondary alteration process is observed too. Most of the copper is in oxide form on the surface and because of high degree of oxidation and erosion, sulfide mineralization is rare in outcrops so deeper samples are needed to study the deposit. Drilling is the best choice in such situations. According to mineralization and the host rock (pillow lava and andesite-basalt), the mineralization type seems to be categorized as a massive sulfide and redbed type. Generally the mineralization manner (copper mineralization as stockworks), the host rock (pillow lava and andesite-basalt), the deposit development environment (a volcanic part of an</p><p>Ophiolite sequence) and the alterations (quartz-carbonate, epidote and chlorite) observed in this region and comparing them to the massive sulfide types leads to classify Mesgaran deposit as a Volcanic Massive Sulfide (VMS) type. But still more studies are needed to prove this claim with higher accuracy [<xref ref-type="bibr" rid="scirp.86459-ref18">18</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref19">19</xref>] (see <xref ref-type="fig" rid="fig4">Figure 4</xref>).</p></sec><sec id="s2_3"><title>2.3. Reagents and Sample Preparation</title><p>200 kg of the sample is taken from Mesgaran Field after excavation. Then the sample is crushed by a jaw crusher and milled to obtain minus 120 microns size. After milling, XRF and XRD are applied to the sample to study phases and chemical composition. All tests and devices took place in laboratories of Amirkabir University of Technology. The main copper mineral phase in the sample is malachite and the main mineral phase of the sample is quartz that does not react with sulfuric acid. XRF device was X’Unique II Philips (<xref ref-type="table" rid="table1">Table 1</xref>).</p></sec><sec id="s2_4"><title>2.4. Leaching Tests</title><p>For leaching tests, sulfuric acid of Merck Company is selected and distilled water is used for dilution. Moreover, a hotplate and 250 ml beaker are used for these tests. The hotplate has a digital temperature regulator and magnetic stirrer. First,</p><p>the solution is prepared for each test in a beaker together with specified pH and after reaching a defined temperature, a certain amount of copper ore with a size fraction of minus 120 micron is added to the solution for doing leaching tests in certain time periods. Four factors of acid concentrations, temperature, time and pulp density has been studied in three levels by the Taguchi method. As a consequence, L9 Taguchi orthogonal array has been selected for leaching tests. Tests are designed with the Taguchi method and Variance analysis (ANOVA) has been done in Design Expert for leaching tests and Microsoft Excel for cementation tests. The value of each parameter at every level has been presented in <xref ref-type="table" rid="table2">Table 2</xref>.</p></sec><sec id="s2_5"><title>2.5. Cementation Tests</title><p>The cementation process of copper by iron powder is provided by following equation:</p><p>Cu 2 + + Fe ⇒ Cu + Fe 2 + <sup> </sup></p><p>As a result of the differences in electrochemical potentials, a reaction will take place. The reaction potential of Iron and Copper is presented in <xref ref-type="table" rid="table3">Table 3</xref>.</p><p>(∆G˚)<sub>298</sub>= −20.29 − 15.54 = −35.83 Kcal</p><p>According to the Gibbs free energy equation, the reaction will be obtained</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> XRF analysis of sample</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Compound</th><th align="center" valign="middle" >Quantity%</th><th align="center" valign="middle" >Compound</th><th align="center" valign="middle" >Quantity%</th></tr></thead><tr><td align="center" valign="middle" >SiO<sub>2</sub></td><td align="center" valign="middle" >53.8</td><td align="center" valign="middle" >Cu<sub>2</sub>O</td><td align="center" valign="middle" >3.2</td></tr><tr><td align="center" valign="middle" >Fe<sub>2</sub>O<sub>3</sub></td><td align="center" valign="middle" >21.5</td><td align="center" valign="middle" >MnO</td><td align="center" valign="middle" >0.4</td></tr><tr><td align="center" valign="middle" >Al<sub>2</sub>O<sub>3</sub></td><td align="center" valign="middle" >10.9</td><td align="center" valign="middle" >SO<sub>3</sub></td><td align="center" valign="middle" >0.7</td></tr><tr><td align="center" valign="middle" >MgO</td><td align="center" valign="middle" >5.5</td><td align="center" valign="middle" >P<sub>2</sub>O<sub>5</sub></td><td align="center" valign="middle" >0.5</td></tr><tr><td align="center" valign="middle" >CaO</td><td align="center" valign="middle" >3.4</td><td align="center" valign="middle" >Total</td><td align="center" valign="middle" >100</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Levels of factors in leaching tests</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Parameter</th><th align="center" valign="middle"  colspan="3"  >Level</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td></tr><tr><td align="center" valign="middle" >Acid concentration (gr/l)</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >120</td></tr><tr><td align="center" valign="middle" >Time (minute)</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >90</td><td align="center" valign="middle" >120</td></tr><tr><td align="center" valign="middle" >Temperature (Celsius)</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >80</td></tr><tr><td align="center" valign="middle" >Pulp density (gr/l)</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >150</td><td align="center" valign="middle" >200</td></tr></tbody></table></table-wrap><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Reaction equations of copper and iron</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Half Reaction</th><th align="center" valign="middle" >Standard reduction potential (E˚)</th><th align="center" valign="middle" >Gibbs free energy (∆G˚)</th></tr></thead><tr><td align="center" valign="middle" >Cu<sup>2+</sup> + 2e =&gt; Cu</td><td align="center" valign="middle" >−0.337</td><td align="center" valign="middle" >15.54</td></tr><tr><td align="center" valign="middle" >Fe<sup>2+</sup> + 2e =&gt; Fe</td><td align="center" valign="middle" >0.44</td><td align="center" valign="middle" >−20.29</td></tr></tbody></table></table-wrap><p>spontaneously. In order to perform cementation tests, 100 ml of copper ore was dissolved in the solution and added up to a 250 ml beaker, and after regulating pH, the temperature will be adjusted by the hotplate. After these steps, iron powder will be added up to the solution in order to study the test.</p><p>In order to study the cementation of copper by iron powder, four parameters of pH, temperature, time and amount of iron powder were optimized in three levels by the Taguchi method. The value of each parameter at every level has been presented in <xref ref-type="table" rid="table4">Table 4</xref>.</p></sec><sec id="s2_6"><title>2.6. Taguchi Method</title><p>The technique of defining and investigating all the possible conditions in an experiment involving multiple factors is known as the design of experiments. Basically, classical parameter design, developed by Fisher, is complicated and not easy to use. Especially, a large number of experiments must be conducted when the number of the process parameters increases. To solve this problem, Taguchi method uses a special design of orthogonal arrays to study the entire parameter space with a small number of experiments only [<xref ref-type="bibr" rid="scirp.86459-ref20">20</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref21">21</xref>].</p><p>Experimental designs were first introduced by Fisher as an agricultural research tool in the 1920s [<xref ref-type="bibr" rid="scirp.86459-ref22">22</xref>]. His primary aim was to obtain the most information possible about a process with the least number of experiments. Experimental designs and optimization methods for chemists and other engineering branches were reviewed by Bayne and Rubin [<xref ref-type="bibr" rid="scirp.86459-ref23">23</xref>] , Debets [<xref ref-type="bibr" rid="scirp.86459-ref24">24</xref>] and Duckworth [<xref ref-type="bibr" rid="scirp.86459-ref25">25</xref>] , Taguchi [<xref ref-type="bibr" rid="scirp.86459-ref26">26</xref>] simplified the application of experimental design by using standardized library of basic designs called orthogonal arrays, along with some simple methods to modify these layout to fit individual situations. His methodology was also developed within an industrial environment and favoured productivity and cost effectiveness over the statistical rigor. Orthogonal arrays were used to assign factors to a series of experimental combinations which results could then be analyzed by using a common mathematical procedure. The main effect of these factors and preselected interactions between the factors were independently extracted. The identification of controlling factors and the quantitation of the magnitude of the effects was emphasized rather than just the identification of statistically significant effects. The number of trial chosen for an experimental design was based on the resolution desired. In a factorial design, one could study main effects as well as interactions between factors. This latter</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Levels of factors in cementation tests</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Parameter</th><th align="center" valign="middle"  colspan="3"  >Level</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >2</td><td align="center" valign="middle" >3</td></tr><tr><td align="center" valign="middle" >pH</td><td align="center" valign="middle" >0</td><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >3</td></tr><tr><td align="center" valign="middle" >Temperature (Celsius)</td><td align="center" valign="middle" >25</td><td align="center" valign="middle" >35</td><td align="center" valign="middle" >45</td></tr><tr><td align="center" valign="middle" >Time (hour)</td><td align="center" valign="middle" >0.5</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1.5</td></tr><tr><td align="center" valign="middle" >Iron powder (stoichiometric amount)</td><td align="center" valign="middle" >1</td><td align="center" valign="middle" >1.5</td><td align="center" valign="middle" >2</td></tr></tbody></table></table-wrap><p>characteristic was a major advantage of the technique but a major disadvantage of one-at-a-time variable testing. Main effects and interactions could be confounded, with one another if the experimental design of low resolution were chosen [<xref ref-type="bibr" rid="scirp.86459-ref27">27</xref>] [<xref ref-type="bibr" rid="scirp.86459-ref28">28</xref>].</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Leaching Ability</title><p>The L9 array leaching tests which are modeled by the Taguchi method are inserted in <xref ref-type="table" rid="table5">Table 5</xref>.</p><sec id="s3_1_1"><title>3.1.1. Effects of Acid Concentration in Leaching</title><p>After 9 tests with the Taguchi method, 1 factor diagrams of acid concentration to recovery rate was obtained as shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>. The greater acid concentration causes more H<sup>+</sup> cation in the solution which increases the recovery rate individually.</p></sec><sec id="s3_1_2"><title>3.1.2. Effect of Time in Leaching</title><p>According to <xref ref-type="fig" rid="fig6">Figure 6</xref>, time factor affect has an increasing role in recovery rate, but optimum conditions should be checked via more tests. Time is always a critical factor in leaching tests which can result in diverse outcomes related to nature of the element. In this study, effect of time is complex due to behavior of sample and related to interaction with other factors.</p></sec><sec id="s3_1_3"><title>3.1.3. Effect of Temperature in Leaching</title><p>According to chemistry principles, an increase in temperature will result in a progress of elements motion which means it will lead to more reactivity of complex. Based on our test results which can be seen in <xref ref-type="fig" rid="fig7">Figure 7</xref>. There is a gradual progress in recovery rate with an increase in amount of the temperature.</p></sec><sec id="s3_1_4"><title>3.1.4. Effect of Pulp Density in Leaching</title><p>Similar to most leaching tests, increasing the pulp density will cause a decrease</p><table-wrap id="table5" ><label><xref ref-type="table" rid="table5">Table 5</xref></label><caption><title> L9 array tests with Taguchi method</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >No.</th><th align="center" valign="middle" >Acid concentration (gr/l)</th><th align="center" valign="middle" >Time (minute)</th><th align="center" valign="middle" >Temperature (Celsius)</th><th align="center" valign="middle" >Pulp density (gr/l)</th><th align="center" valign="middle" >Cu recovery (%)</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >82.74</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >90</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >150</td><td align="center" valign="middle" >62.67</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >78.75</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >86.96</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >90</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >92.44</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >150</td><td align="center" valign="middle" >77.75</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >80</td><td align="center" valign="middle" >150</td><td align="center" valign="middle" >84.10</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >90</td><td align="center" valign="middle" >40</td><td align="center" valign="middle" >200</td><td align="center" valign="middle" >81.02</td></tr><tr><td align="center" valign="middle" >9</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >120</td><td align="center" valign="middle" >60</td><td align="center" valign="middle" >100</td><td align="center" valign="middle" >99.11</td></tr></tbody></table></table-wrap><p>in recovery rate, where in some tests it has been seen that after a maximum level for pulp density, reactions will come to an end. In this case, the anomaly point has occurred where it is expected to further decrease the recovery rate. Incidentally, the lower level in pulp density will result in a greater recovery rate (<xref ref-type="fig" rid="fig8">Figure 8</xref>).</p></sec><sec id="s3_1_5"><title>3.1.5. Effect of Factor Interactions in Leaching</title><p>According to the obtained models in the software, factor interactions have been investigated to gain better cognition of the process and increase the efficiency of operation. For this purpose, interaction of temperature and pulp density are depicted in <xref ref-type="fig" rid="fig9">Figure 9</xref> where increasing the temperature and decreasing the pulp density results in a greater recovery rate of the operation. Also, interaction of time and pulp density covered in <xref ref-type="fig" rid="fig1">Figure 1</xref>0 indicate that increasing time and</p><p>decreasing pulp density results in a greater recovery rate of the operation, while time played a twofold role in this diagram. In addition, interaction of time and temperature as shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>1 where the increasing level of time and temperature together lead to more recovery rate, while time played a twofold role in this diagram once more. The interaction of acid concentration and temperature is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>2 where an increase of acid concentration and temperature together caused a greater recovery rate.</p><p>Interaction of acid concentration and time is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>3 where, recovery rate stepped up with an increase of acid concentration and temperature together, to further illustrate the factors which are involved in reactions, acid concentration has the most influence besides temperature. The interaction of acid concentration and pulp density is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>4, where an increase of acid concentration and a decrease of pulp density results in a greater recovery rate of the operation. More diagrams have been given in <xref ref-type="fig" rid="fig1">Figure 1</xref>5 where 3D factor diagrams have simplified the interactions cognition.</p></sec></sec><sec id="s3_2"><title>3.2. Cementation Behavior</title><sec id="s3_2_1"><title>3.2.1. Effect of pH in Cementation</title><p>According to the obtained diagram in <xref ref-type="fig" rid="fig1">Figure 1</xref>6, as obtained from the experiments, pH has an increasing linear boost in copper recovery rate curve in cementation operation, which it shows a decrease in amount of H<sup>+</sup> cations will</p><p>lead to substitution of Copper ions with Iron ions in solution.</p></sec><sec id="s3_2_2"><title>3.2.2. Effect of Temperature in Cementation</title><p>With a more detailed look at <xref ref-type="fig" rid="fig1">Figure 1</xref>7, it is obvious that a raise in the temperature level will cause an increase in recovery rate and it is logical from thermodynamic aspects of the reactions.</p></sec><sec id="s3_2_3"><title>3.2.3. Effect of Time in Cementation</title><p>As it has been seen in <xref ref-type="fig" rid="fig1">Figure 1</xref>8, after a sharp increasing result of recovery rate from 30 minutes to 60 minutes, the recovery still increases but in a gradual pattern, which shows that the optimum point is 1 hour for further economic aspects. So, according to this diagram the optimum condition of time for cementation of copper with iron powders is about 1 hour.</p></sec><sec id="s3_2_4"><title>3.2.4. Effect of Iron Powder on Cementation</title><p>The last parameter which is examined in the tests was the total amount of iron powder that is needed for the reaction. Due to test results, increasing the amount of iron powder that is measured by stoichiometric quantities, tends to increase the copper recovery rate of the cementation process (<xref ref-type="fig" rid="fig1">Figure 1</xref>9).</p></sec></sec></sec><sec id="s4"><title>4. Conclusions</title><p>Mesgaran copper field which is also known as one of the primeval mines in east of Iran, was examined with numerous tests to be run as a modern mine with new technologies. As it has been observed, the economic mineral in this field is</p><p>malachite which is encompassed by quartz gangues that leads the experiments to leaching tests with H<sub>2</sub>SO<sub>4</sub> instead of flotation or physical separation methods. Hence, after taking samples from the field, the test was designed via the Taguchi and Variance analysis method. Afterward, tests were performed in the Amirkabir University of Technology laboratory to gain optimum conditions of leaching and cementation operation. In the leaching operation, four factors of acid concentration, temperature, time and pulp density have been studied at three levels. Moreover, in order to study copper cementation by iron powder, four factors of pH, temperature, time and amount of iron powder, are optimized at three levels.</p><p>Finally, it is found that increasing acid concentration, temperature and time will cause an increase in the copper recovery of ores with the leaching method. On the other hand, increasing pulp density will have a reverse reaction. From another stance, in the cementation process, the recovery rate of copper increased by maximization of pH, temperature and a lower rise in time and iron powder amount. Optimum conditions of leaching studies with 99.11% recovery rate came after 120 gram per liter of H<sub>2</sub>SO<sub>4</sub>, 80 degrees Celsius, 2 hours and 100 gram per liter of solid to liquid. In addition, the optimum conditions of parameters during the cementation process with iron powder were obtained at more than 95% with a pH of 3, 45 degrees Celsius, 1 hour and 1.5 times more than the stoichiometric amount of copper.</p></sec><sec id="s5"><title>Acknowledgements</title><p>Technical and data supports from Amirkabir University of Technology (Tehran Polytechnic), Prof. Ardeshir Hezarkhani and Tehranpadir Co. are acknowledged.</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>Khakmardan, S., Shirazi, A., Shirazy, A., Hosseingholi, H. (2018) Copper Oxide Ore Leaching Ability and Cementation Behavior, Mesgaran Deposit in IRAN. 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