Cd/SBA-15 heterogeneous catalyst used for acetic acid conversion: pseudo-homogeneous kinetic model, response surface methodology, and historical data design

dc.authorid0000-0002-3518-1572
dc.contributor.authorSimsek, Veli
dc.date.accessioned2025-05-20T18:55:48Z
dc.date.issued2023
dc.departmentBilecik Şeyh Edebali Üniversitesi
dc.description.abstractMesoporous materials (MMs) in the Santa Barbara Amorphous (SBA) family can be used as catalysts or support materials (SMs) for catalysts because they have controllable pore structure, thermal and chemical stability, and their surface properties can be modified easily depending on the desired reaction type. Surfactant (Pluronic p123; it is a symmetric triblock copolymer comprising poly and its chemical formula; HO(CH2CH2O)(20)(CH2CH(CH3)O)(70)(CH2CH2O)(20)H), a silica source (such as Tetraethyl orthosilicate: TEOS; SiC8H20O4), and a solvent are used in the synthesis of the SBA family (SBA-15). The SBA-15 was given with the hydrothermal method (HM) a catalyst feature by loading the active substance at a rate of 10, 25 % (cadmium/silica) by mass. Esterification reactions (ERs) were carried out with Cd-SBA-15 (Cd/Si: 10-25 %) catalyst at a feed rate of 1/2 (methanol/acetic acid), in the presence of 0.4 g catalyst, at a reaction temperature of 373 K and for 6-48 h. After 48 h, the catalytic activity (CA) values were obtained as 65 and 68 %, respectively. The re-usability of the catalysts was repeated two times under the same experimental conditions. It was observed that the catalysts maintained their catalytic activity of 73.35 and 68.72 % (3 x 48 h). In addition, the limited effect of catalyst amount on acetic acid conversion was investigated by Response Surface Methodology, and Historical Data Design. Moreover, k(1), k(2), equilibrium constant and activation energy values were calculated using the pseudo-homogeneous kinetic model. The physical features of the catalysts were investigated by BET, XRD, FTIR, DRIFT, SEM/EDX, and MAPPING analysis methods.
dc.identifier.doi10.1515/zpch-2023-0243
dc.identifier.endpage1456
dc.identifier.issn0942-9352
dc.identifier.issn2196-7156
dc.identifier.issue9
dc.identifier.scopus2-s2.0-85170086885
dc.identifier.scopusqualityQ2
dc.identifier.startpage1443
dc.identifier.urihttps://doi.org/10.1515/zpch-2023-0243
dc.identifier.urihttps://hdl.handle.net/11552/7394
dc.identifier.volume237
dc.identifier.wosWOS:001052310400001
dc.identifier.wosqualityQ3
dc.indekslendigikaynakWoS
dc.indekslendigikaynakScopus
dc.indekslendigikaynakWoS - Science Citation Index Expanded
dc.institutionauthorSimsek, Veli
dc.language.isoen
dc.publisherWalter De Gruyter Gmbh
dc.relation.ispartofZeitschrift Fur Physikalische Chemie-International Journal of Research in Physical Chemistry & Chemical Physics
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20250518
dc.subjectAcetic Acid Conversion
dc.subjectCd/SBA-15
dc.subjectcharacterization
dc.subjectpseudo-homogeneous kinetic model
dc.subjectresponse surface methodology
dc.titleCd/SBA-15 heterogeneous catalyst used for acetic acid conversion: pseudo-homogeneous kinetic model, response surface methodology, and historical data design
dc.typeArticle

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