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<ArticleSet>
<Article>
<Journal>
				<PublisherName>Iranian Association of Chemical Engineering (IAChE)</PublisherName>
				<JournalTitle>Iranian Journal of Chemical Engineering (IJChE)</JournalTitle>
				<Issn>1735-5397</Issn>
				<Volume>9</Volume>
				<Issue>3</Issue>
				<PubDate PubStatus="epublish">
					<Year>2012</Year>
					<Month>07</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Compartment Mixing Model in a Stirred Tank Equipped Dual Rushton Turbine</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>14</FirstPage>
			<LastPage>21</LastPage>
			<ELocationID EIdType="pii">10257</ELocationID>
			
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>F.</FirstName>
					<LastName>Fakheri</LastName>
<Affiliation>Transport Phenomena Research Center, Chemical Engineering Faculty,
Sahand University of Technology, Tabriz, Iran</Affiliation>

</Author>
<Author>
					<FirstName>J.</FirstName>
					<LastName>Moghaddas</LastName>
<Affiliation>Transport Phenomena Research Center, Chemical Engineering Faculty,
Sahand University of Technology, Tabriz, Iran</Affiliation>
<Identifier Source="ORCID">0000-0001-7817-405X</Identifier>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2015</Year>
					<Month>07</Month>
					<Day>28</Day>
				</PubDate>
			</History>
		<Abstract>Knowledge of mixing time is of fundamental importance for investigation of mixing efficiency in agitation systems. The mixing time obtained by using the correlation and formula in large scale mixing systems was incorrect. Again, the number of available correlations in this scale of mixing systems is limited. To predict the mixing time of stirred tanks with dual impellers commonly used in industry, a third-compartment mixing model was used. The time of homogenization of the charge (mixing time) was calculated from the time dependency of the local concentration of tracer measured at various locations. Experimental data on mixing time were obtained with a conductivity technique. In the present study distribution of tracer in the bulk of the liquid was described by compartment model (CM) as well as for stirred vessel with dual Rushton impellers. As for the model, a good agreement between the experimental data and the calculated values was apparent.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Mixing time</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Compartment Model</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Rushton turbine</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Tracer</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">conductivity</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://www.ijche.com/article_10257_9578a63fbe545bd82cc5bbe749636af1.pdf</ArchiveCopySource>
</Article>
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