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Electrochemical production of syngas from CO2 at pressures up to 30 bar in electrolytes containing ionic liquid

dc.contributor.authorMessias, Sofia
dc.contributor.authorSousa, Miguel M.
dc.contributor.authorPonte, Manuel Nunes
dc.contributor.authorRangel, C. M.
dc.contributor.authorPardal, T.
dc.contributor.authorMachado, Ana
dc.date.accessioned2020-03-25T09:07:09Z
dc.date.available2020-03-25T09:07:09Z
dc.date.issued2019
dc.description.abstractABSTRACT: Electrochemical CO2 reduction in a reactor that can operate up to 100 bar and 80 degrees C, with a configuration similar to that of an alkaline electrolyser, for hydrogen production suitable to be used industrially is reported for the first time. The effect of pressure on the co-electrolysis of CO2 and water was studied. The successful scale-up from a previously reported batch process to electrodes of ca. 30 cm(2) geometrical area (30-fold factor) that combines the use of pressure and an ionic liquid-based electrolyte is presented. Also for the first time, the potential of the system under study to achieve high conversions of CO2 to avoid a purification step of syngas from unreacted CO2 is shown. An inexpensive commercial foil of the common metal zinc was employed. A semi-continuous operation yielded syngas productivities in the range of 0.02-0.04 mmol cm(-2) h(-1) at ca. -1.2 V vs. QRE Ag/Ag+. When an electrolyte consisting of 90 wt% H2O and 10 wt% 1-ethyl-3-methylimidazolium trifluoromethanesulfonate was used, selectivities for CO in the range of 62% to 72% were obtained at 10 bar pressure, whereas selectivities of 82% were obtained at 30 bar pressure. H-2/CO ratios in the range of 1/1 to 4/1 at 10 bar pressure suitable for the synthesis of a variety of fuels, such as hydrocarbons, methanol, methane and chemical building blocks, were observed. An energy efficiency of 44.6% was calculated for a H-2/CO ratio of 2.2 suitable for the synthesis of methanol.pt_PT
dc.description.versioninfo:eu-repo/semantics/publishedVersionpt_PT
dc.identifier.citationMessias, Sofia ... [et.al.] - Electrochemical production of syngas from CO2 at pressures up to 30 bar in electrolytes containing ionic liquid. In: Reaction Chemistry & Engineering, 2019, Vol. 4, p. 1982-1990pt_PT
dc.identifier.doi10.1039/c9re00271ept_PT
dc.identifier.issn2058-9883
dc.identifier.urihttp://hdl.handle.net/10400.9/3200
dc.language.isoengpt_PT
dc.peerreviewedyespt_PT
dc.publisherRoyal Society of Chemistrypt_PT
dc.relationPOCI-01-0145-FEDER-016387pt_PT
dc.relation.publisherversionhttps://doi.org/10.1039/c9re00271ept_PT
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/pt_PT
dc.subjectCarbon dioxidept_PT
dc.subjectElectrochemical reductionpt_PT
dc.subjectEnergy conversionpt_PT
dc.subjectIonic liquidspt_PT
dc.subjectElectrolytespt_PT
dc.titleElectrochemical production of syngas from CO2 at pressures up to 30 bar in electrolytes containing ionic liquidpt_PT
dc.typejournal article
dspace.entity.typePublication
oaire.citation.endPage1990pt_PT
oaire.citation.startPage1982pt_PT
oaire.citation.titleReaction Chemistry and Engineeringpt_PT
oaire.citation.volume4pt_PT
person.familyNameRangel
person.familyNameMachado
person.givenNameCarmen M.
person.givenNameAna
person.identifier1702931
person.identifier.ciencia-idAA13-FF7C-9E29
person.identifier.ciencia-id7E1F-6E0F-F3B6
person.identifier.orcid0000-0001-7996-8142
person.identifier.orcid0000-0002-7432-8725
person.identifier.ridD-5477-2011
person.identifier.scopus-author-id7006108156
rcaap.rightsopenAccesspt_PT
rcaap.typearticlept_PT
relation.isAuthorOfPublication804e595a-d539-46a2-ae78-6cadc8ca9457
relation.isAuthorOfPublicationc37d4a90-59f0-4d44-bee9-9f022529e003
relation.isAuthorOfPublication.latestForDiscovery804e595a-d539-46a2-ae78-6cadc8ca9457

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