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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>12</Volume>
				<Issue>3</Issue>
				<PubDate PubStatus="epublish">
					<Year>2021</Year>
					<Month>07</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>An Investigation on Tailing Slurry Transport in Kooshk lead-Zinc Mine in Iran Based on Non-Newtonian Fluid Rheology: an Experimental Study</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>877</FirstPage>
			<LastPage>893</LastPage>
			<ELocationID EIdType="pii">2185</ELocationID>
			
<ELocationID EIdType="doi">10.22044/jme.2021.11105.2093</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>J. Vazifeh</FirstName>
					<LastName>Mehrabani</LastName>
<Affiliation>Department of Mineral Processing, Faculty of Mining Engineering, Sahand University of Technology, Sahand New Town, Tabriz, Iran</Affiliation>

</Author>
<Author>
					<FirstName>M.</FirstName>
					<LastName>Goharkhah</LastName>
<Affiliation>Faculty of Mechanical Engineering, Sahand University of Technology, Sahand New Town, Tabriz, Iran</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2021</Year>
					<Month>08</Month>
					<Day>24</Day>
				</PubDate>
			</History>
		<Abstract>In the current research work, a piping system is designed for slurry transport to the tailing dam in the Kooshk lead-zinc mine, Iran. The experiments are carried out primarily to investigate the rheological behavior of the slurry at different densities and obtain a non-Newtonian model for the shear stress variation with the deformation rate. It is shown that the shear stress of concentrated slurry follows the plastic Bingham model. The results obtained also indicate the increasing trend of the yield stress and the apparent viscosity of the slurry with the density. Appropriate correlations are proposed for the apparent viscosity and yield stress as a function of pulp concentration. At the next step, the required design parameters such as the slurry flow rate, pressure drop, critical velocity, and minimum required head for flow initiation and head losses are calculated for different slurry densities and pipe sizes. The appropriate piping system is finally designed based on the experimental data and the calculated parameters. It is concluded that the 3 in diameter pipe can be used to deliver the slurry with solid concentrations between 44% &lt; C&lt;sub&gt;w &lt;/sub&gt;&lt; 60% by weight, without a pumping system.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Tailing slurry</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">critical velocity</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">pipe design</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Bingham model</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Kooshk mine</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://jme.shahroodut.ac.ir/article_2185_2e7ba565dcf33fb3d7ef58be1633bb12.pdf</ArchiveCopySource>
</Article>
</ArticleSet>
