Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/80940
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dc.contributorDepartment of Rehabilitation Sciences-
dc.contributorUniversity Research Facility in Life Sciences-
dc.creatorXu, H-
dc.creatorMarotoValer, MM-
dc.creatorNi, M-
dc.creatorCao, J-
dc.creatorXuan, J-
dc.date.accessioned2019-06-27T07:32:33Z-
dc.date.available2019-06-27T07:32:33Z-
dc.identifier.issn0306-2619en_US
dc.identifier.urihttp://hdl.handle.net/10397/80940-
dc.language.isoenen_US
dc.publisherPergamon Pressen_US
dc.rights© 2019 The Authors. Published by Elsevier B.V. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/)en_US
dc.rightsThe following publication Xu, H., Maroto-Valer, M. M., Ni, M., Cao, J., & Xuan, J. (2019). Low carbon fuel production from combined solid oxide CO2 co-electrolysis and Fischer-Tropsch synthesis system: A modelling study. Applied energy, 242, 911-918 is available at https://doi.org/10.1016/j.apenergy.2019.03.145en_US
dc.subjectFischer-Tropsch synthesisen_US
dc.subjectHydrocarbon generationen_US
dc.subjectMathematical modellingen_US
dc.subjectSolid oxide electrolyzer cellen_US
dc.titleLow carbon fuel production from combined solid oxide CO 2 co-electrolysis and Fischer-Tropsch synthesis system : a modelling studyen_US
dc.typeJournal/Magazine Articleen_US
dc.identifier.spage911en_US
dc.identifier.epage918en_US
dc.identifier.volume242en_US
dc.identifier.doi10.1016/j.apenergy.2019.03.145en_US
dcterms.abstractCH 4 -assisted solid oxide electrolyzer cells (SOECs) can co-electrolyze H 2 O and CO 2 effectively for simultaneous energy storage and CO 2 utilization. Compared with conventional SOECs, CH 4 -assisted SOECs consume less electricity because CH 4 in the anode provides part of the energy for electrolysis. As syngas (CO and H 2 mixture) is generated from the co-electrolysis process, it is necessary to study its utilization through the subsequent processes, such as Fischer-Tropsch (F-T) synthesis to produce more value-added products. An F-T reactor can convert syngas into hydrocarbons, and thus it is very suitable for the utilization of syngas. In this paper, the combined CH 4 -assisted SOEC and F-T synthesis system is numerically studied. Validated 2D models for CH 4 -assisted SOEC and F-T processes are adopted for parametric studies. It is found that the cathode inlet H 2 O/CO 2 ratio in the SOEC significantly affects the production components through the F-T process. Other operating parameters such as the operating temperature and applied voltage of the SOEC are found to greatly affect the productions of the system. This model is important for understanding and design optimization of the combined fuel-assisted SOEC and F-T synthesis system to achieve economical hydrocarbon generation.-
dcterms.accessRightsopen accessen_US
dcterms.bibliographicCitationApplied energy, 2019, v. 242, p. 911-918-
dcterms.isPartOfApplied energy-
dcterms.issued2019-
dc.identifier.scopus2-s2.0-85063063999-
dc.identifier.eissn1872-9118en_US
dc.description.validate201906 bcmaen_US
dc.description.oaVersion of Recorden_US
dc.identifier.FolderNumberOA_IR/PIRAen_US
dc.description.pubStatusPublisheden_US
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