Publication:
Assessment of acid strength in sodium-exchanged resin catalysts: consequences on glycerol etherification with isobutene in batch and flow reactors

dc.contributor.departmentDepartment of Chemical and Biological Engineering
dc.contributor.departmentN/A
dc.contributor.departmentDepartment of Chemical and Biological Engineering
dc.contributor.kuauthorUzun, Alper
dc.contributor.kuauthorBozkurt, Özge Deniz
dc.contributor.kuprofileFaculty Member
dc.contributor.kuprofilePhD Student
dc.contributor.researchcenterKoç University Tüpraş Energy Center (KUTEM) / Koç Üniversitesi Tüpraş Enerji Merkezi (KÜTEM)
dc.contributor.researchcenterKoç University Surface Science and Technology Center (KUYTAM) / Koç Üniversitesi Yüzey Teknolojileri Araştırmaları Merkezi (KUYTAM)
dc.contributor.schoolcollegeinstituteCollege of Engineering
dc.contributor.schoolcollegeinstituteGraduate School of Sciences and Engineering
dc.contributor.yokid59917
dc.contributor.yokidN/A
dc.date.accessioned2024-11-09T23:44:50Z
dc.date.issued2019
dc.description.abstractConsequences of a decrease in the number of acid sites by the cation exchange on the acid strength of the resin catalysts were assessed using ammonia as a probe molecule. IR spectra illustrated that v(N-H) bands on NH3-saturated Amberlyst 15 (TM) shift linearly to higher frequencies with an increase in the degree of sodium exchange associated with an increase in the Bronsted acid strength. These results were further confirmed by density functional theory calculations illustrating that the deprotonation energy of a sulfonated styrene group decreases upon Na+-exchange on its neighboring counterparts. Consequences of these changes in acid strength were investigated on glycerol etherification with isobutene. Batch reactor measurements at high conversions illustrated that selectivity to desired glycerol ethers increases as that of isobutene dimerization is suppressed with an increase in acid strength. The effects of acid strength on the complex reaction network were further investigated using a once-through flow reactor specifically focusing on low conversions. These measurements showed that mono-tert-butyl glycerol ether and di-isobutene were the primary products on pristine Amberlyst 15 (TM), while di-and tri-tert-butyl glycerol ethers also become a primary product on sodium-exchanged counterpart catalysts.
dc.description.indexedbyWoS
dc.description.indexedbyScopus
dc.description.openaccessNO
dc.description.sponsorshipScientific and Technological Research Council of Turkey (TUBITAK) through Industrial R&D Projects Support Program [1501, 3130673]
dc.description.sponsorshipTUBA-GEBIP Award of Turkish Academy of Sciences
dc.description.sponsorshipBAGEP Award of Science Academy of Turkey
dc.description.sponsorshipTARLA This work was financed by the Scientific and Technological Research Council of Turkey (TUBITAK) through Industrial R&D Projects Support Program (1501) with project number 3130673. We thank to Koc University junior student Seda Sarp for catalyst preparation and titration measurements and to TUPRAS R&D Center laboratory staffs, Erdal Akyiiz and Haluk Uslu for their help in high pressure reactor operations and GC-MS analyses, respectively. We appreciate Irem Atay from Green Chemicals A.S. for the supply of Amberlyst resins. A.U. acknowledges TUBA-GEBIP Award of Turkish Academy of Sciences and the BAGEP Award of Science Academy of Turkey. O.D.B. and A.U. acknowledge the support from TARLA.
dc.description.volume466
dc.identifier.doi10.1016/j.mcat.2018.12.027
dc.identifier.issn2468-8231
dc.identifier.scopus2-s2.0-85059832707
dc.identifier.urihttp://dx.doi.org/10.1016/j.mcat.2018.12.027
dc.identifier.urihttps://hdl.handle.net/20.500.14288/13736
dc.identifier.wos458941000001
dc.keywordsIon exchange resin
dc.keywordsAmberlyst
dc.keywordsCation exchange
dc.keywordsGlycerol etherification with isobutene
dc.keywordsFlow reactor
dc.languageEnglish
dc.publisherElsevier Science Bv
dc.sourceMolecular Catalysis
dc.subjectChemistry, physical and theoretical
dc.titleAssessment of acid strength in sodium-exchanged resin catalysts: consequences on glycerol etherification with isobutene in batch and flow reactors
dc.typeJournal Article
dspace.entity.typePublication
local.contributor.authorid0000-0001-7024-2900
local.contributor.authorid0000-0001-8844-1465
local.contributor.kuauthorUzun, Alper
local.contributor.kuauthorBozkurt, Özge Deniz
relation.isOrgUnitOfPublicationc747a256-6e0c-4969-b1bf-3b9f2f674289
relation.isOrgUnitOfPublication.latestForDiscoveryc747a256-6e0c-4969-b1bf-3b9f2f674289

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