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<ArticleSet>
<Article>
<Journal>
				<PublisherName>Iran Energy Association (IEA)</PublisherName>
				<JournalTitle>Journal of Energy Management and Technology</JournalTitle>
				<Issn>2588-3372</Issn>
				<Volume>2</Volume>
				<Issue>1</Issue>
				<PubDate PubStatus="epublish">
					<Year>2018</Year>
					<Month>04</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Experimental investigation of Methane Partial Oxidation for Hydrogen Production</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>18</FirstPage>
			<LastPage>22</LastPage>
			<ELocationID EIdType="pii">59513</ELocationID>
			
<ELocationID EIdType="doi">10.22109/jemt.2018.110940.1051</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>Hamid Reza</FirstName>
					<LastName>Lari</LastName>
<Affiliation>Director of wind Turbine Technology Development Center</Affiliation>

</Author>
<Author>
					<FirstName>Mohammad Reza</FirstName>
					<LastName>Shahnazari</LastName>
<Affiliation>Associate Professor of K.N.Toosi University of Technology,</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2017</Year>
					<Month>12</Month>
					<Day>16</Day>
				</PubDate>
			</History>
		<Abstract>The thermal partial oxidation process of methane was investigated experimentally. Compared with the other reforming technologies partial oxidation process has several advantageous. There is no need for external heat sources and additional feeds like water as in steam reforming. Moreover, the process is catalyst free and thus catalyst deactivation problems are completely out of consideration. Thermodynamic calculations and kinetic simulation were performed to determine the practical operating conditions. Experimentally, a porous material-based reactor was built to perform the partial oxidation process. Al2O3 granular with different size selected as porous structures and installed in the reaction zone. Physical parameters include diameter of the rector is considered for other experimental test. As the result the temperature profiles along the reactor central axis and concentration profiles of CO and H2 were measured. Also the effects of equivalence air ratio on the reforming process were investigated. Different equivalence air ratio 1.5 and 2 was considered to perform the partial oxidation process.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">methane reforming</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">hydrogen</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">partial Oxidation</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Porous media</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Combustion</Param>
			</Object>
		</ObjectList>
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</Article>
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