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<Journal>
<PublisherName>OICC Press</PublisherName>
<JournalTitle>International Journal of Industrial Chemistry</JournalTitle>
<Issn>2228-5547</Issn>
<Volume>16</Volume>
<Issue>3</Issue>
<PubDate PubStatus="epublish">
<Year>2025</Year>
<Month>12</Month>
<Day>09</Day>
</PubDate>
</Journal>
<ArticleTitle>Study of CO Hydrogenation over Cobalt-based Catalysts: Synergistic Effect</ArticleTitle>
<VernacularTitle></VernacularTitle>
<FirstPage></FirstPage>
<LastPage></LastPage>
<ELocationID EIdType="doi">10.57647/j.ijic.2025.1603.13</ELocationID>
<Language>EN</Language>
<AuthorList>
<Author>
<FirstName>Arefeh</FirstName>
<LastName>Sadeghi Nikou</LastName>
<Affiliation>Department of Chemistry, NT.C., Islamic Azad University, Tehran, Iran</Affiliation>
<Identifier Source="ORCID"></Identifier>
</Author>
<Author>
<FirstName>Shahram</FirstName>
<LastName>Moradi Dehaghi</LastName>
<Affiliation>Department of Chemistry, NT.C., Islamic Azad University, Tehran, Iran</Affiliation>
<Identifier Source="ORCID"></Identifier>
</Author>
<Author>
<FirstName>Yahya</FirstName>
<LastName>Zamani</LastName>
<Affiliation>Department of Chemistry, NT.C., Islamic Azad University, Tehran, Iran; Gas Research Division, Research Institute of Petroleum Industry, Tehran, Iran</Affiliation>
<Identifier Source="ORCID"></Identifier>
</Author>
<Author>
<FirstName>Jafar</FirstName>
<LastName>Sadeghzadeh Ahari</LastName>
<Affiliation>Department of Chemistry, NT.C., Islamic Azad University, Tehran, Iran; Gas Research Division, Research Institute of Petroleum Industry, Tehran, Iran</Affiliation>
<Identifier Source="ORCID"></Identifier>
</Author>
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<PublicationType>Journal Article</PublicationType>
<History>
<PubDate PubStatus="received">
<Year>2025</Year>
<Month>12</Month>
<Day>09</Day>
</PubDate>
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<Abstract>A series of cobalt-based catalysts were prepared using γ-Al2O3 as a support and cerium/zirconium mixed oxides as promoters, with varying Ce/Zr molar ratios. The 15Co/γ-Al2O3, 15Co/3Zr/γAl2O3, 15Co/3Ce/γ-Al2O3 and 15Co/1.5Zr/1.5Ce/γ-Al2O3 were synthesized using the wet impregnation method. BET, TGA, FE-SEM, XRD, H2-TPR, and ICP techniques were used to determine the characteristics of the prepared catalysts. The findings showed that the catalyst (15Co/1.5Zr/1.5Ce/γ-Al2O3) with double promotion exceeded the performance of other catalysts, indicating notable synergistic effects. These effects are expected to play a crucial role in reducing side reactions that affect selectivity towards higher hydrocarbons. The 15Co/1.5Zr/1.5Ce/γAl2O3 catalyst demonstrated enhanced stability and reduced degradation during prolonged operation, resulting in higher CO conversion and effective suppression of excessive carbon chain growth. All prepared catalysts were tested in a fixed-bed reactor under a pressure of 27 bar, a temperature of 220 °C, and an H2/CO ratio of 2. The results showed that the doubly-promoted catalyst achieved superior performance, with CO conversion, C5+ selectivity, and yield reaching 50.4 ± 1.5%, 82.3 ± 0.9%, and 41.5 ± 0.8%, respectively, compared to the other catalysts. In conclusion, these findings confirm the substantial influence of Zr and Ce promoters on the performance of Co-based catalysts during the Fischer-Tropsch synthesis reaction. </Abstract>
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