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<Article>
<Journal>
				<PublisherName>Iranian Association of Chemical Engineering (IAChE)</PublisherName>
				<JournalTitle>Iranian Journal of Chemical Engineering (IJChE)</JournalTitle>
				<Issn>1735-5397</Issn>
				<Volume>6</Volume>
				<Issue>4</Issue>
				<PubDate PubStatus="epublish">
					<Year>2009</Year>
					<Month>10</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Optimization of Integrated Low-Temperature Gas Separation Processes Using SA Method and Different Refrigerants</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>27</FirstPage>
			<LastPage>33</LastPage>
			<ELocationID EIdType="pii">15174</ELocationID>
			
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>N.</FirstName>
					<LastName>Tahouni</LastName>
<Affiliation>Dept. of Chemical Engineering, University of Tehran, Tehran, Iran</Affiliation>

</Author>
<Author>
					<FirstName>M. H.</FirstName>
					<LastName>Panjeshahi</LastName>
<Affiliation>Dept. of Chemical Engineering, University of Tehran, Tehran, Iran</Affiliation>

</Author>
<Author>
					<FirstName>R.</FirstName>
					<LastName>Smith</LastName>
<Affiliation>Centre for Process Integration, School of Chemical Engineering and
Analytical Science, University of Manchester, Manchester, UK</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2016</Year>
					<Month>05</Month>
					<Day>29</Day>
				</PubDate>
			</History>
		<Abstract>&lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;In low-temperature processes, heat rejected from separation columns is removed by&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;refrigeration systems to heat sinks (reboilers &amp; pre-heaters), process streams, other&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;refrigeration streams, or external utilities. The need for efficient utilization and&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;recovery of energy in sub-ambient gas separation processes is still challenging.&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;Performance and reliability of Simulated Annealing (SA) for simultaneous design and&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;optimization of such systems has been investigated previously. In this work, the effect of&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;different refrigerants satisfying a set of process cooling duties at different temperatures&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;is addressed. Cost reduction can be realized by encompassing both effective screening&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;of heat-integrated separation columns and selecting the best refrigerants. A 29.7% cost&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;savings has been shown through a case study. Afterwards, a comprehensive&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;thermodynamic analysis has been carried out on achieved solutions to verify the&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;accuracy of existing shortcut models and robustness of optimized structure. It has been&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;shown that exergy analysis using two different approaches (i.e. stream wise and unit&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;operation wise) are the same, which indicate the accuracy of the used models.&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;Moreover, we have indicated that both utility costs and exergy losses can be considered&lt;/em&gt; &lt;span style=&quot;font-size: 10pt; color: #000000; font-style: normal; font-variant: normal;&quot;&gt;&lt;em&gt;as an objective function when optimizing the designs.&lt;/em&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;br style=&quot;font-style: normal; font-variant: normal; font-weight: normal; letter-spacing: normal; line-height: normal; orphans: 2; text-align: -webkit-auto; text-indent: 0px; text-transform: none; white-space: normal; widows: 2; word-spacing: 0px; -webkit-text-size-adjust: auto; -webkit-text-stroke-width: 0px;&quot; /&gt;&lt;br class=&quot;Apple-interchange-newline&quot; /&gt;&lt;/span&gt;</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Low-temperature Process</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Different Refrigerants</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">optimization</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Exergy analysis</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Simulated Annealing</Param>
			</Object>
		</ObjectList>
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