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<Article>
<Journal>
				<PublisherName>University of Isfahan</PublisherName>
				<JournalTitle>Gas Processing Journal</JournalTitle>
				<Issn>2322-3251</Issn>
				<Volume>12</Volume>
				<Issue>1</Issue>
				<PubDate PubStatus="epublish">
					<Year>2024</Year>
					<Month>03</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Numerical Investigation of CO2 Capture from N2-Rich Gas Mixtures Using a Zeolite 13X Packed Bed with Aluminum Foam Heat Transfer Enhancement</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>1</FirstPage>
			<LastPage>16</LastPage>
			<ELocationID EIdType="pii">30774</ELocationID>
			
<ELocationID EIdType="doi">10.22108/gpj.2026.149197.1147</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>Mojtaba</FirstName>
					<LastName>Mahdavi Asl</LastName>
<Affiliation>Department of Chemical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran</Affiliation>

</Author>
<Author>
					<FirstName>Mohammad</FirstName>
					<LastName>Hojjat</LastName>
<Affiliation>Department of Chemical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran</Affiliation>

</Author>
<Author>
					<FirstName>Mohsen</FirstName>
					<LastName>Gholami</LastName>
<Affiliation>Department of Chemical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran
/ Department of Chemical Engineering, Vrije Universiteit Brussel, 1050 Brussels, Belgium</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2026</Year>
					<Month>06</Month>
					<Day>05</Day>
				</PubDate>
			</History>
		<Abstract>A numerical investigation of CO&lt;sub&gt;2&lt;/sub&gt; adsorption and desorption in a 13X zeolite packed bed enhanced with aluminum foam for thermal management is presented using a two-dimensional transient model. The rectangular bed (10–30 mm thick) with a 15 mm gas channel is simulated via the finite element method, solving coupled momentum, mass, and energy equations under local thermal equilibrium. Effects of inlet gas velocity, cooling/heating fluid temperatures, and bed thickness on breakthrough, temperature, capacity, desorption, and thermal efficiency are examined with and without foam. Results show that increasing inlet velocity from 0.001 to 0.01 m/s reduces breakthrough time (defined as C&lt;sub&gt;out&lt;/sub&gt;/C&lt;sub&gt;in&lt;/sub&gt;=0.05) from ~300 s to 38 s due to faster saturation. Aluminum foam enhances heat transfer, reducing the time to reach 2.6 mol/kg adsorption capacity in a 30 mm bed from 1995 s to 1540 s (23% reduction). During desorption at 470 K, foam reduces the time for CO&lt;sub&gt;2&lt;/sub&gt; loading to drop from 2.72 to 2.38 mol/kg from 1680 s to 1420 s. Higher cooling fluid temperature raises bed temperature and lowers capacity, while higher desorption temperature accelerates regeneration. Thicker beds improve adsorption performance but reduce thermal efficiency due to thermal inertia. Aluminum foam causes a ~5% reduction in thermal efficiency from added thermal mass. Overall, aluminum foam significantly enhances heat transfer and dynamic adsorption performance, demonstrating the potential of foam-enhanced zeolite beds for compact temperature swing CO&lt;sub&gt;2&lt;/sub&gt; capture systems.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Carbon Capture</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Aluminum Foam</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Zeolite 13X</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Adsorption</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">TSA</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Numerical Modeling</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://gpj.ui.ac.ir/article_30774_7aeecbc770c97b68a4a33aed014cbc24.pdf</ArchiveCopySource>
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