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<!DOCTYPE ArticleSet PUBLIC "-//NLM//DTD PubMed 2.7//EN" "https://dtd.nlm.nih.gov/ncbi/pubmed/in/PubMed.dtd">
<ArticleSet>
<Article>
<Journal>
				<PublisherName>Iranian Association of Chemical Engineering (IAChE)</PublisherName>
				<JournalTitle>Iranian Journal of Chemical Engineering (IJChE)</JournalTitle>
				<Issn>1735-5397</Issn>
				<Volume>8</Volume>
				<Issue>2</Issue>
				<PubDate PubStatus="epublish">
					<Year>2011</Year>
					<Month>04</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Comparative Study of Two Various Percent of CO Injection Effect to Cascade Methanol Synthesis Reactor in the Presence of Long-term Catalyst Deactivation</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>69</FirstPage>
			<LastPage>80</LastPage>
			<ELocationID EIdType="pii">10291</ELocationID>
			
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>M.</FirstName>
					<LastName>Bayat</LastName>
<Affiliation>Department of Chemical Engineering, School of Chemical and Petroleum
Engineering, Shiraz University, Shiraz, Iran</Affiliation>

</Author>
<Author>
					<FirstName>F.</FirstName>
					<LastName>Rahmani</LastName>
<Affiliation></Affiliation>

</Author>
<Author>
					<FirstName>T.</FirstName>
					<LastName>Ghiyami</LastName>
<Affiliation></Affiliation>

</Author>
<Author>
					<FirstName>M. R.</FirstName>
					<LastName>Rahimpour</LastName>
<Affiliation></Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2015</Year>
					<Month>07</Month>
					<Day>28</Day>
				</PubDate>
			</History>
		<Abstract>In this paper, a heterogeneous one-dimensional model for simulation of cascade methanol reactor has been developed, while the various percent of CO was injected to these reactors. In the cascade reactor configuration, a system with two-catalyst bed instead of one single catalyst bed is applied for methanol synthesis. In the first catalyst bed, the synthesis gas is partly converted to methanol in a water-cooled reactor. In the second bed, which is a gas-cooled reactor, the reaction heat is used to preheat the feed gas to the first bed. In this study, the various percent CO injections of feed entrance (1% and 2%) to different reactors (first and second reactor) of conventional dual type methanol reactor have been considered. The simulation results represent 5.127% and 4.158% enhancement in the yield of methanol production in comparison with conventional dual type methanol reactor (CDMR) and membrane dual type methanol reactor (MDMR) respectively, while 2% CO was injected to the first reactor. Also, by CO injection to the feed, water produced during methanol synthesis via CO2 hydrogenation which accelerates the catalyst deactivation and reduces methanol&lt;br /&gt;production rate, is reduced greatly.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Methanol Synthesis</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">CO Injection</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Cascade Reactor</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Catalyst deactivation</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://www.ijche.com/article_10291_ef1890585bae446a0668afed3012daa2.pdf</ArchiveCopySource>
</Article>
</ArticleSet>
