Processing of Solubilized Asphaltene in Aqueous Media

atmire.migration.oldid4880
dc.contributor.advisorPereira-Almao, Pedro
dc.contributor.authorHaghighat, Parsa
dc.contributor.committeememberMaini, Brij
dc.contributor.committeememberDe Visscher, Alex
dc.contributor.committeememberSalahub, Dennis
dc.contributor.committeememberMcCaffrey, William
dc.date.accessioned2016-09-09T21:49:21Z
dc.date.available2016-09-09T21:49:21Z
dc.date.issued2016
dc.date.submitted2016en
dc.description.abstractThe continuous increase of asphaltene production coupled with inefficiencies of conventional asphaltene utilization methods reveals the vital necessity of oil downstream sector to develop new technologies for asphaltene processing. In this research, a novel two-step process for asphaltene conversion in aqueous media is introduced. Through this process, asphaltenes are first solubilized in water via low-temperature oxidation; then, solubilized organic materials are converted to value added product through catalytic reaction. The main focus of this research is studying and understanding the second step of the process. In this regard, the solubilized asphaltene in water (SAW) which is the feedstock of the second reaction was produced in large scale through asphaltene oxidation in aqueous phase. After preparation and characterization of SAW, the impact of effective parameters and operational conditions on progress of SAW catalytic reaction was investigated. The catalytic activity in SAW reaction media was evaluated under two different atmospheres, i.e., in presence and absence of external hydrogen gas. The sulfided NiMo/γ-Al2O3 catalyst showed the best activity among the heterogeneous catalysts tested for SAW reaction with external hydrogen. On the other hand, the reduced form of Cu-Ce/MFI and Cu-MFI catalysts provided the best performance for SAW reaction in absence of external hydrogen. The kinetic study of SAW hydroprocessing was carried out, where the promotional effect of temperature on products yield and quality was observed. A lumped kinetic model containing 6 first order reactions was proposed, which accurately predicted the experimental results; the activation energy of SAW conversion was calculated to be 83 kJ/mol, which is a typical activation energy of biomass crudes reaction in water at sub-cooled conditions. Decarboxylation was a dominant reaction through SAW hydroprocessing, while hydrodeoxygenation, cracking and hydrogenation occurred in parallel.en_US
dc.identifier.citationHaghighat, P. (2016). Processing of Solubilized Asphaltene in Aqueous Media (Doctoral thesis, University of Calgary, Calgary, Canada). Retrieved from https://prism.ucalgary.ca. doi:10.11575/PRISM/27445en_US
dc.identifier.doihttp://dx.doi.org/10.11575/PRISM/27445
dc.identifier.urihttp://hdl.handle.net/11023/3282
dc.language.isoeng
dc.publisher.facultyGraduate Studies
dc.publisher.institutionUniversity of Calgaryen
dc.publisher.placeCalgaryen
dc.rightsUniversity of Calgary graduate students retain copyright ownership and moral rights for their thesis. You may use this material in any way that is permitted by the Copyright Act or through licensing that has been assigned to the document. For uses that are not allowable under copyright legislation or licensing, you are required to seek permission.
dc.subjectEngineering--Chemical
dc.subject.classificationAsphalteneen_US
dc.subject.classificationAqueous Media Reactionen_US
dc.subject.classificationCatalysten_US
dc.subject.classificationChemical Kienticsen_US
dc.subject.classificationHeavy Oil Upgradingen_US
dc.titleProcessing of Solubilized Asphaltene in Aqueous Media
dc.typedoctoral thesis
thesis.degree.disciplineChemical and Petroleum Engineering
thesis.degree.grantorUniversity of Calgary
thesis.degree.nameDoctor of Philosophy (PhD)
ucalgary.item.requestcopytrue

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