Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/134856
DC FieldValueLanguage
dc.contributor.authorLorenzo Pérez,Beatrizen_US
dc.contributor.authorGraca, Nuno S.en_US
dc.contributor.authorOrtega Saavedra, Juanen_US
dc.contributor.authorRodrigues, Alirio E.en_US
dc.date.accessioned2024-11-28T17:46:51Z-
dc.date.available2024-11-28T17:46:51Z-
dc.date.issued2024en_US
dc.identifier.issn0888-5885en_US
dc.identifier.otherWoS-
dc.identifier.urihttp://hdl.handle.net/10553/134856-
dc.description.abstract1,1-Diethoxybutane (DEB) was synthesized in a Simulated Moving Bed Reactor (SMBR) consisting of eight columns packed with the commercial resin Amberlyst15. The True Moving Bed Reactor (TMBR) model was used to model the reaction/separation process and to select the best experimental conditions for the process. The experiences of two types of assays, named runs 1 and 2, were analyzed with preset conditions as detailed in the article. The best conversion obtained was 94% for run 2 but with low raffinate purity (66%) and productivity (1.8 kgDEBL-1day-1). On the other hand, the best raffinate productivity was 3.7 kgDEBL-1day-1 for run 1, with a lower conversion (88%) and purity (60%). These results show that the SMBR pilot unit has a great potential to be competitive and efficient compared to other traditional processes for the synthesis of 1,1-diethoxybutane, which can be extensible to other acetals. In addition to highlighting that the process proves to be environmentally friendly, it is suggested that improvement in performance would be achieved by working with full resin regeneration in section 1 and full desorbent cleaning in section 4. These recommendations would also improve the quantitative representation of the model, although qualitatively the modeling is considered acceptable.en_US
dc.languageengen_US
dc.relation.ispartofIndustrial & Engineering Chemistry Researchen_US
dc.sourceIndustrial & Engineering Chemistry Research [ISSN 0888-5885], n. 94, p. 124-135en_US
dc.subject330311 Química industrialen_US
dc.subject3303 ingeniería y tecnología químicasen_US
dc.subject.otherPumped storage hydroelectric power planten_US
dc.subject.otherTurbine Energyen_US
dc.subject.otherCarbon dioxideen_US
dc.subject.otherEnvironment Hydrogenen_US
dc.titleOperation and Modeling of a Process for 1,1-Diethoxybutane Synthesis in a Simulated Moving Bed Reactor Pilot Uniten_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1021/acs.iecr.4c02701en_US
dc.identifier.isi001353276300001-
dc.identifier.eissn1520-5045-
dc.description.lastpage135en_US
dc.description.firstpage124en_US
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.contributor.daisngidNo ID-
dc.contributor.daisngidNo ID-
dc.contributor.daisngidNo ID-
dc.contributor.daisngidNo ID-
dc.description.numberofpages10en_US
dc.utils.revisionen_US
dc.contributor.wosstandardWOS:Lorenzo, B-
dc.contributor.wosstandardWOS:Graça, NS-
dc.contributor.wosstandardWOS:Ortega, J-
dc.contributor.wosstandardWOS:Rodrigues, AE-
dc.identifier.ulpgcen_US
dc.contributor.buulpgcBU-INGen_US
dc.description.sjr0,811
dc.description.jcr3,8
dc.description.sjrqQ1
dc.description.jcrqQ2
dc.description.scieSCIE
dc.description.miaricds11,0
item.fulltextCon texto completo-
item.grantfulltextopen-
crisitem.author.deptGIR IDeTIC: División de Ingeniería Térmica e Instrumentación-
crisitem.author.deptIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.deptGIR IDeTIC: División de Ingeniería Térmica e Instrumentación-
crisitem.author.deptIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0003-1154-2633-
crisitem.author.orcid0000-0002-8304-2171-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.fullNameLorenzo Pérez,Beatriz-
crisitem.author.fullNameOrtega Saavedra, Juan-
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