Dimethyl ether synthesis on clinoptilolite zeolite and HZSM5-based hybrid catalysts in a fixed-bed reactor
dc.authorid | Yasar, Muzaffer/0000-0001-5877-8008 | |
dc.contributor.author | Gurdal, Savas | |
dc.contributor.author | Yasar, Muzaffer | |
dc.date.accessioned | 2025-01-27T20:25:10Z | |
dc.date.available | 2025-01-27T20:25:10Z | |
dc.date.issued | 2023 | |
dc.department | Çanakkale Onsekiz Mart Üniversitesi | |
dc.description.abstract | In this study 4 different acid catalysts were prepared and mixed with commercial CZA catalysts and investigated in direct DME synthesis. Some of the used acid catalysts were not investigated in the literature therefore the work involves novelty. In a fixed-bed reactor, dimethyl ether (DME) was synthesized from the synthesis gas on two catalysts from, natural clinoptilolite and zeolite catalysts. The clinoptilolite (HK and DK) and two (HZSM5(117) and HZSM5(360)) catalysts mixed with commercial CuO/ZnO/Al2O3 (CZN) catalysts. The catalysts were also characterized by analytical chemistry techniques such as XRD, BET, TGA, and FTIR. Four different catalysts (HK, DK, HZSM5(117) and HZSM5(360)) and CZA catalysts were mixed at a ratio of 3/1, respectively, and studies were carried out in a fixed-bed reactor. Four different catalyst composition activity tests were made at tem-peratures 250, 275, and 300 & DEG;C. At the same time, the pressure was 30 and 40 bar and four different times (30, 60, 90, and 120 min). The composition of the gases fed to the system for DME was adjusted to N2/CO2/CO/H2 = 36/10/18/36 by volume. DME selectivity (SDME) and total carbon (XC) conversion were calculated for each condition. The experimental results showed that the highest DME selectivity of 96.50% was observed in the reaction of the DK + CZA catalyst mixture at 250 & DEG;C and 30 min at 40 bar. In addition, high DME selectivity was obtained in all reactions of DK + CZA and HK + CZA catalyst compositions at three different temperatures. The highest DME selectivity obtained is 89.69% for the reaction of the HK + CZA catalyst mixture at 300 & DEG;C and 60 min at 30 bar. Experimental results gave insights into Dimethyl ether synthesis from syngas on clinoptilolite zeolite and HZSM5-based hybrid catalysts in a fixed-bed reactor.& COPY; 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved. | |
dc.description.sponsorship | Scientific and Technological Research Council of Turkey 2211-C Program [1649B03150346]; Istanbul University-Cerrahpasa Scientific Research Projects [FDK-2017-24933] | |
dc.description.sponsorship | This publication was created within the scope of Savas Gurdal's doctoral thesis. This study was supported by The Scientific and Technological Research Council of Turkey 2211-C Program with number 1649B03150346 and Istanbul University-Cerrahpasa Scientific Research Projects project number FDK-2017-24933. | |
dc.identifier.doi | 10.1016/j.ijhydene.2023.01.188 | |
dc.identifier.endpage | 22987 | |
dc.identifier.issn | 0360-3199 | |
dc.identifier.issn | 1879-3487 | |
dc.identifier.issue | 60 | |
dc.identifier.scopus | 2-s2.0-85150789637 | |
dc.identifier.scopusquality | Q1 | |
dc.identifier.startpage | 22978 | |
dc.identifier.uri | https://doi.org/10.1016/j.ijhydene.2023.01.188 | |
dc.identifier.uri | https://hdl.handle.net/20.500.12428/22450 | |
dc.identifier.volume | 48 | |
dc.identifier.wos | WOS:001028144300001 | |
dc.identifier.wosquality | Q1 | |
dc.indekslendigikaynak | Web of Science | |
dc.indekslendigikaynak | Scopus | |
dc.language.iso | en | |
dc.publisher | Pergamon-Elsevier Science Ltd | |
dc.relation.ispartof | International Journal of Hydrogen Energy | |
dc.relation.publicationcategory | info:eu-repo/semantics/openAccess | |
dc.rights | info:eu-repo/semantics/closedAccess | |
dc.snmz | KA_WoS_20250125 | |
dc.subject | Dimethyl ether | |
dc.subject | Clinoptilolite | |
dc.subject | Synthesis gas | |
dc.subject | Catalysts | |
dc.subject | Fixed-bed reactor | |
dc.title | Dimethyl ether synthesis on clinoptilolite zeolite and HZSM5-based hybrid catalysts in a fixed-bed reactor | |
dc.type | Article |