<?xml version="1.0" encoding="utf-8"?>
<journal>
<title>Iranian Journal of Materials Science and Engineering</title>
<title_fa>فصلنامه علم و مهندسی مواد ایران</title_fa>
<short_title>IJMSE</short_title>
<subject>Engineering &amp; Technology</subject>
<web_url>http://ijmse.iust.ac.ir</web_url>
<journal_hbi_system_id>18</journal_hbi_system_id>
<journal_hbi_system_user>agent2</journal_hbi_system_user>
<journal_id_issn>1735-0808</journal_id_issn>
<journal_id_issn_online>2383-3882</journal_id_issn_online>
<journal_id_pii></journal_id_pii>
<journal_id_doi></journal_id_doi>
<journal_id_iranmedex></journal_id_iranmedex>
<journal_id_magiran></journal_id_magiran>
<journal_id_sid></journal_id_sid>
<journal_id_nlai></journal_id_nlai>
<journal_id_science></journal_id_science>
<language>en</language>
<pubdate>
	<type>jalali</type>
	<year>1390</year>
	<month>6</month>
	<day>1</day>
</pubdate>
<pubdate>
	<type>gregorian</type>
	<year>2011</year>
	<month>9</month>
	<day>1</day>
</pubdate>
<volume>8</volume>
<number>3</number>
<publish_type>online</publish_type>
<publish_edition>1</publish_edition>
<article_type>fulltext</article_type>
<articleset>
	<article>


	<language>en</language>
	<article_id_doi></article_id_doi>
	<title_fa></title_fa>
	<title>EFFECTOFTHE TYPE OFCARBON MATERIALON THE REDUCTION KINETICS OFBARIUM SULFATE</title>
	<subject_fa></subject_fa>
	<subject></subject>
	<content_type_fa>Research Paper</content_type_fa>
	<content_type>Research Paper</content_type>
	<abstract_fa></abstract_fa>
	<abstract>&lt;font face=&quot;TimesNewRomanPS-BoldItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-BoldItalicMT&quot;&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;Abstract: &lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;the reduction agent. Pellets of barite ore containing about 95% BaSO&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;temperature, time, ore grain size and the type and grain size of the carbon materials. Graphite, coke and charcoal have&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;been used as the reducing agent and the reduction experiments have been performed in the temperature range of 925-&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;1150 °C. Apart from conducting the experiments using pellets made of ore powder, kinetic analysis of the experimental&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;data by use of the reduced (dimensionless) time method has been another unique feature of the present study.&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;Experimental results show that grain size of either carbon material or barite ore has not appreciable effect on the&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;reaction rate. Kinetic analysis of the experimental data revealed the rate is strongly controlled by the chemical reaction&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;of carbon gasification (Boudouard reaction). The reaction rate is very considerably related to the type of carbon&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;material so that the activation energy varies from 15.6 kcal.mol&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;kcal.mol&lt;/font&gt;&lt;/p&gt;&lt;p align=&quot;left&quot;&gt;&lt;font size=&quot;2&quot;&gt;gasification.&lt;/font&gt;&lt;/p&gt;&lt;/font&gt;&lt;/font&gt;&lt;font size=&quot;2&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;The present study deals with the reduction of barium sulfate (Barite) to barium sulfide by use of carbon as&lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;4 &lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;has been reduced under different conditions of&lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;-1 &lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;for charcoal to 26.3 kcal.mol&lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;-1 &lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;for graphite and 20.8&lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;-1 &lt;/font&gt;&lt;/font&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;&lt;font face=&quot;TimesNewRomanPS-ItalicMT&quot;&gt;for coke. This behavior provides further support for the postulated reaction mechanism, i.e., carbon&lt;/font&gt;&lt;/font&gt; &lt;/font&gt;</abstract>
	<keyword_fa></keyword_fa>
	<keyword>Keywords: Barite, carbothermic reduction, kinetic analysis, carbon gasification, activation energy.</keyword>
	<start_page>1</start_page>
	<end_page>7</end_page>
	<web_url>http://ijmse.iust.ac.ir/browse.php?a_code=A-10-3-150&amp;slc_lang=en&amp;sid=1</web_url>


<author_list>
	<author>
	<first_name></first_name>
	<middle_name></middle_name>
	<last_name>M. Sh. Bafghi</last_name>
	<suffix></suffix>
	<first_name_fa></first_name_fa>
	<middle_name_fa></middle_name_fa>
	<last_name_fa></last_name_fa>
	<suffix_fa></suffix_fa>
	<email>* msbafghi@iust.ac.ir</email>
	<code>180031947532846001226</code>
	<orcid>180031947532846001226</orcid>
	<coreauthor>Yes
</coreauthor>
	<affiliation>1 School of Metallurgy and Materials Engineering, Iran University of Science &amp; Technology, Tehran, Iran.</affiliation>
	<affiliation_fa></affiliation_fa>
	 </author>


	<author>
	<first_name></first_name>
	<middle_name></middle_name>
	<last_name>A. Yarahmadi</last_name>
	<suffix></suffix>
	<first_name_fa></first_name_fa>
	<middle_name_fa></middle_name_fa>
	<last_name_fa></last_name_fa>
	<suffix_fa></suffix_fa>
	<email></email>
	<code>180031947532846001227</code>
	<orcid>180031947532846001227</orcid>
	<coreauthor>No</coreauthor>
	<affiliation>2 Department of Mining Engineering, Faculty of Engineering, Yazd University, Yazd, Iran.</affiliation>
	<affiliation_fa></affiliation_fa>
	 </author>


	<author>
	<first_name></first_name>
	<middle_name></middle_name>
	<last_name>A. Ahmadi</last_name>
	<suffix></suffix>
	<first_name_fa></first_name_fa>
	<middle_name_fa></middle_name_fa>
	<last_name_fa></last_name_fa>
	<suffix_fa></suffix_fa>
	<email></email>
	<code>180031947532846001228</code>
	<orcid>180031947532846001228</orcid>
	<coreauthor>No</coreauthor>
	<affiliation>3 School of Metallurgy and Materials Engineering, Iran University of Science &amp; Technology, Tehran, Iran.</affiliation>
	<affiliation_fa></affiliation_fa>
	 </author>


	<author>
	<first_name></first_name>
	<middle_name></middle_name>
	<last_name>H. Mehrjoo</last_name>
	<suffix></suffix>
	<first_name_fa></first_name_fa>
	<middle_name_fa></middle_name_fa>
	<last_name_fa></last_name_fa>
	<suffix_fa></suffix_fa>
	<email></email>
	<code>180031947532846001229</code>
	<orcid>180031947532846001229</orcid>
	<coreauthor>No</coreauthor>
	<affiliation>3 School of Metallurgy and Materials Engineering, Iran University of Science &amp; Technology, Tehran, Iran.</affiliation>
	<affiliation_fa></affiliation_fa>
	 </author>


</author_list>


	</article>
</articleset>
</journal>
