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<ArticleSet>
<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>3</Issue>
				<PubDate PubStatus="epublish">
					<Year>2021</Year>
					<Month>09</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Investigating the Activity of the Supported Bimetallic Ni-Co Catalysts on the Dry Reforming of Methane</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>63</FirstPage>
			<LastPage>73</LastPage>
			<ELocationID EIdType="pii">144892</ELocationID>
			
<ELocationID EIdType="doi">10.22034/ijche.2022.315787.1416</ELocationID>
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>Gholamreza</FirstName>
					<LastName>Moradi</LastName>
<Affiliation>Razi University</Affiliation>
<Identifier Source="ORCID">0000-0002-6006-0270</Identifier>

</Author>
<Author>
					<FirstName>Hamed</FirstName>
					<LastName>Hemmati</LastName>
<Affiliation>Razi University</Affiliation>

</Author>
<Author>
					<FirstName>Sahar</FirstName>
					<LastName>Rostami</LastName>
<Affiliation>Chemical Engineering Departement,Faculty of engineering, Razi University</Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2021</Year>
					<Month>11</Month>
					<Day>20</Day>
				</PubDate>
			</History>
		<Abstract>&lt;em&gt;In this work, the effect of the Si/Al ratio on the activity of zeolite supported bimetallic (Ni-Co) catalysts for Dry Reforming of Methane (DRM) has been studied. Samples are prepared with impregnation and sol-gel methods and then calcined at 550 &lt;/em&gt;&lt;em&gt;°C&lt;/em&gt;&lt;em&gt; for 2 h. The catalysts were characterized by XRD, XRF, FESEM, BET and TGA. All samples were tested in a micro reactor at three different temperatures (i.e. 700, 750, and 800 &lt;/em&gt;&lt;em&gt;°C&lt;/em&gt;&lt;em&gt;). Micro reactor test results showed that 800 &lt;/em&gt;&lt;em&gt;°C&lt;/em&gt;&lt;em&gt; was the proper temperature for DRM. The catalyst with 5 wt % of Ni and 2.5 wt % of Co supported on γ-Alumina have shown a higher H&lt;sub&gt;2&lt;/sub&gt;/CO ratio than other samples. For the zeolite supported catalysts when Ni/Co=2/1, the surface area and pore volume decreased but the H&lt;sub&gt;2&lt;/sub&gt;/CO ratio increased by increasing the Si/Al ratio. Reverse the Water Gas Shift (WGS) reaction was not very active when the catalyst and support showed a basic property. Also, the stability of the catalysts has been tested for 30h on stream.&lt;/em&gt;</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">Bimetallic catalyst</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Dry Reforming</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Ni-Co</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Si/Al Ratio</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">ZSM-5</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://www.ijche.com/article_144892_a268d6ce2359331a7b400f313e0821ec.pdf</ArchiveCopySource>
</Article>
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