Bilgilendirme: Sürüm Güncellemesi ve versiyon yükseltmesi nedeniyle, geçici süreyle zaman zaman kesintiler yaşanabilir ve veri içeriğinde değişkenlikler gözlemlenebilir. Göstereceğiniz anlayış için teşekkür ederiz.
 

New Bifunctional Catalysts for the Synthesis of Dimethyl Ether Via Carbon Dioxide Utilization

dc.contributor.author Guliyev, Bilal, V
dc.contributor.author Zahidova, Aysel
dc.contributor.author Tuncer, Bashak
dc.contributor.author Sheker, Erol
dc.contributor.author Nasirov, Fizuli A.
dc.date.accessioned 2025-08-27T16:39:35Z
dc.date.available 2025-08-27T16:39:35Z
dc.date.issued 2025
dc.description.abstract The increasing demand for sustainable energy sources has intensified research into carbon dioxide (CO2) utilization for the synthesis of clean alternative fuels such as dimethyl ether. This study investigates the direct synthesis of dimethyl ether from CO2 using bifunctional copper-based hybrid catalysts (SCR-A, SCR-B, and SCR-C) synthesized via the sol-gel method. These catalysts integrate oxidative and acidic functionalities within a single system, enabling methanol synthesis and subsequent dehydration into dimethyl ether in a one-step process. Experimental evaluations were conducted under varying pressures ranging from atmospheric to 40 bar and temperatures between 200-350 degrees C, using both low-and high-pressure reactors to assess performance. The results indicate that under atmospheric conditions, methanol conversion reached 87%, with 82% dimethyl ether selectivity, demonstrating the bifunctional character of the catalysts. Among them, SCR-A exhibited the most favorable performance in terms of conversion and product distribution. Under high-pressure conditions (5 and 7 bar), CO2 conversion remained constant at 50%, while selectivity was influenced by temperature and reactor pressure. At 40 bar and 300 degrees C, dimethyl ether selectivity reached its peak at 60%, confirming this range as the optimal operational window for maximizing dimethyl ether yield. However, a notable decrease in selectivity was observed at 350 degrees C, likely due to catalyst deactivation or the promotion of undesired side reactions. These findings underline the thermodynamic and operational benefits of direct dimethyl ether synthesis over the conventional two-step route, as it simplifies process design, enhances CO2 utilization, and reduces energy and cost demands en_US
dc.identifier.doi 10.62972/1726-4685.si2025.1.286
dc.identifier.issn 1726-4685
dc.identifier.issn 2519-2876
dc.identifier.uri https://doi.org/10.62972/1726-4685.si2025.1.286
dc.identifier.uri https://hdl.handle.net/11147/18362
dc.language.iso en en_US
dc.publisher Y H Mammadaliyev inst Petrochemical Proc, Natl Acad Sci, Baku, Azerbaijan en_US
dc.relation.ispartof Processes of Petrochemistry and Oil Refining en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject CO2 Utilization en_US
dc.subject Bifunctional Catalysts en_US
dc.subject Methanol en_US
dc.subject Dimethyl Ether en_US
dc.subject Oxidative And Acidic Functionalities en_US
dc.title New Bifunctional Catalysts for the Synthesis of Dimethyl Ether Via Carbon Dioxide Utilization en_US
dc.type Article en_US
gdc.author.wosid Nasirov, Fuzuli/V-7211-2019
gdc.description.department İzmir Institute of Technology en_US
gdc.description.departmenttemp [Guliyev, Bilal, V; Zahidova, Aysel; Tuncer, Bashak] SOCAR Turkey Res & Dev & Innovat Inc, Siteler Mahallesi Necmettin Giritlioglu Cad, Aliaga Izmir, Turkiye; [Sheker, Erol] Izmir Inst Technol, Dept Energy Syst Engn, Gulbahce Kampusu 35430, Urla Izmir, Turkiye; [Nasirov, Fizuli A.] Minist Sci & Educ Republ Azerbaijan, YH Mammadaliyev Inst Petrochem Proc, 30 Khojaly ave, AZ-1025 Baku, Azerbaijan en_US
gdc.description.endpage 293 en_US
gdc.description.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
gdc.description.scopusquality N/A
gdc.description.startpage 286 en_US
gdc.description.woscitationindex Emerging Sources Citation Index
gdc.description.wosquality N/A
gdc.identifier.wos WOS:001531273900031

Files