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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>18</Volume>
				<Issue>1</Issue>
				<PubDate PubStatus="epublish">
					<Year>2021</Year>
					<Month>03</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Medium Temperature Shift Reaction Over Copper-Ceria catalyst in Fixed-Bed and Microchannel Reactors</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>46</FirstPage>
			<LastPage>51</LastPage>
			<ELocationID EIdType="pii">139288</ELocationID>
			
<ELocationID EIdType="doi">10.22034/ijche.2021.139288</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>A.</FirstName>
					<LastName>Irankhah</LastName>
<Affiliation>Hydrogen and Fuel Cell Research Lab., Chemical Engineering Dep., Engineering Faculty, University of Kashan</Affiliation>
<Identifier Source="ORCID">0000-0002-3901-4552</Identifier>

</Author>
<Author>
					<FirstName>Y.</FirstName>
					<LastName>Davoodbeygi</LastName>
<Affiliation>Department of chemical Engineering, University of Hormozgan, Bandar Abbas, Iran</Affiliation>
<Identifier Source="ORCID">0000-0003-1191-8119</Identifier>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2021</Year>
					<Month>10</Month>
					<Day>26</Day>
				</PubDate>
			</History>
		<Abstract>One of the effective catalysts for hydrogen purification and production via medium temperature shift reaction, is Cu-Ce solid solution. Cu0.1Ce0,9O1.9 was produced using co-precipitation method and then was utilized as support for 5Cu/Ce0.9Cu0.1O1.9 catalyst which was synthesized employing wet impregnation method. X-ray diffraction (XRD) analysis showed that crystalline sizes of Ce0.9Cu0.1O1.9 and 5Cu/Cu0.1Ce0,9O1.9 were 9.22 and 18.33 nm, respectively. The Catalysts were evaluated in medium temperature shift reaction at 300-390 °C and at gas hourly space velocities (GHSV) of 12000 and 30000 h-1, in a fixed bed reactor. Due to higher concentration of Cu and synergic positive effects of both active metal and support, 5Cu/Cu0.1Ce0,9O1.9 catalyst showed better performance. It was also concluded that, because of low residence time at high levels of GHSV, increasing GHSV leads to decrease CO conversion. Then 5Cu/Cu0.1Ce0,9O1.9 was evaluated in microchennel reactor in 2 GHSVs of 12000 and 30000 h-1 and results were compared with the fixed-bed reactor. It can be concluded that microchannel reactor is better in higher GHSVs (lower residence time of gas flow). A microchannel reactor provides a high surface-to-volume ratio and gases pass over the thin layer of catalyst on the coated plates. Hence, due to the better access to the catalytic bed, the reactants react even in a short time, which improves the microchannel performance compared to the fixed bed reactor</Abstract>
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			<Object Type="keyword">
			<Param Name="value">Catalyst</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">hydrogen</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Medium temperature shift</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Copper-Ceria</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Microchannel</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://www.ijche.com/article_139288_bdba47c6c81b8663618df587da5da92a.pdf</ArchiveCopySource>
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