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<ArticleSet>
<Article>
<Journal>
				<PublisherName>Shahrood University of Technology</PublisherName>
				<JournalTitle>Journal of Mining and Environment</JournalTitle>
				<Issn>2251-8592</Issn>
				<Volume>8</Volume>
				<Issue>2</Issue>
				<PubDate PubStatus="epublish">
					<Year>2017</Year>
					<Month>04</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Gallium extraction from Jajarm Bayer process liquor using micro-emulsions</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>269</FirstPage>
			<LastPage>276</LastPage>
			<ELocationID EIdType="pii">780</ELocationID>
			
<ELocationID EIdType="doi">10.22044/jme.2016.780</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>H.</FirstName>
					<LastName>Amani</LastName>
<Affiliation>Department of Mining and Metallurgical Engineering, Yazd University, Yazd, Iran</Affiliation>

</Author>
<Author>
					<FirstName>H.</FirstName>
					<LastName>Naderi</LastName>
<Affiliation>Department of Mining and Metallurgical Engineering, Yazd University, Yazd, Iran</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2016</Year>
					<Month>08</Month>
					<Day>19</Day>
				</PubDate>
			</History>
		<Abstract>Gallium extraction from Jajarm Bayer process liquor (Jajarm, Iran) was investigated using microemulsions. Also the behavior of aluminum was studied as an impurity. Kelex100 (4-ethyl, 1-methyl, 7-octyl, 8-hydroxyquinoleine), &lt;em&gt;iso&lt;/em&gt;-decanol and &lt;em&gt;n&lt;/em&gt;-butanol, and kerosene were used as the surfactant, co-surfactant, and oil phase, respectively. Ternary phase diagrams were produced using various co-surfactants at different C/S ratios. The results obtained show that Winsor II is the predominant region, and the least area was obtained using &lt;em&gt;iso&lt;/em&gt;-decanol at C/S = 4. Using &lt;em&gt;n&lt;/em&gt;-butanol or &lt;em&gt;iso&lt;/em&gt;-decanol at C/S = 2, 100% of gallium was extracted. The equations of the statistical models for the gallium and aluminum extractions using different co-surfactants were calculated. While the highest gallium extraction (100%) was obtained using &lt;em&gt;n&lt;/em&gt;-butanol, due to the high co-extraction of aluminum, the lowest separation and enrichment factors were obtained for this system. The highest separation and enrichment factors were obtained using &lt;em&gt;iso&lt;/em&gt;-decanol at C/S = 2. The point with the compositions of X&lt;sub&gt;AF&lt;/sub&gt; = 30, X&lt;sub&gt;OF&lt;/sub&gt; = 20, and X&lt;sub&gt;C/S&lt;/sub&gt; = 50 was found to be a suitable choice, and led to 74% and 14% extractions for gallium and aluminum, respectively. An enrichment factor of 5.28 was obtained.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Micro-Emulsion</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Gallium</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Bayer Process</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Jajarm</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Solvent extraction</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://jme.shahroodut.ac.ir/article_780_928ed8b315d7ac871924016f71b1526f.pdf</ArchiveCopySource>
</Article>
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