A two-step regeneration method for carbon-supported Ru catalysts deactivated by coke and sulfur during hydrothermal gasification

dc.contributor.authorSun, Songlan
dc.contributor.authorBjelić, Saša
dc.contributor.authorHua, Weicheng
dc.contributor.authorVogel, Frédéric
dc.contributor.authorBaudouin, David
dc.date.accessioned2026-06-19T08:24:49Z
dc.date.issued2026
dc.description.abstractCatalytic hydrothermal gasification (cHTG) offers a sustainable pathway for converting wet biomass into methane, but long-term operation is hindered by catalyst deactivation, particularly due to coke deposition and sulfur poisoning. Ruthenium on activated carbon (Ru/AC) is highly active for methane production but gradually loses performance during continuous gasification of biomass or wastes. Conventional high-temperature oxidative regeneration methods, which rely on combustion to remove coke, are unsuitable for carbon supports due to their poor stability in the presence of oxidizing agents. Here, a low-temperature aqueous regeneration strategy was explored using hydrogen peroxide (H 2 O 2 ) oxidation followed by subcritical water flushing. Effluent analysis and catalyst characterization reveal that coke is primarily oxidized and removed during H 2 O 2 oxidation (<120 °C), while sulfur species are oxidized to strongly adsorbed forms (sulfate) that require subsequent desorption via subcritical water flushing. Based on these insights, a two-step regeneration protocol was developed, consisting of two H 2 O 2 oxidation treatments (85–120 °C), each followed by subcritical water flushing (up to 320 °C). This approach achieves (97 ± 2) % sulfur removal while preserving carbon support integrity. The method enables efficient catalyst regeneration targeting both coking and sulfur fouling, offering a practical aqueous strategy to extend the operational lifetime of Ru/AC catalysts in cHTG and related catalytic systems without the need to remove the material from the catalytic reactor for regeneration. • Two-step aqueous regeneration restores Ruthenium catalyst activity. • Low-temperature H 2 O 2 oxidation removes coke and converts sulfur to oxidized forms. • Subcritical water flushing desorbs strongly bound sulfur species. • 97 ± 2% sulfur removal achieved without damaging carbon support. • Enables catalyst regeneration and lifetime extension without reactor disassembly.
dc.identifier.doi10.1016/j.supflu.2026.106970
dc.identifier.issn0896-8446
dc.identifier.issn1872-8162
dc.identifier.urihttps://irf.fhnw.ch/handle/11645/57069
dc.identifier.urihttps://doi.org/10.26041/fhnw-16534
dc.language.isoen
dc.publisherElsevier
dc.relation.ispartofThe Journal of Supercritical Fluids
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/
dc.subject.ddc660 - Technische Chemie
dc.titleA two-step regeneration method for carbon-supported Ru catalysts deactivated by coke and sulfur during hydrothermal gasification
dc.type01A - Beitrag in wissenschaftlicher Zeitschrift
dc.volume234
dspace.entity.typePublication
fhnw.InventedHereYes
fhnw.ReviewTypepeer-reviewed
fhnw.affiliation.hochschuleHochschule für Technik und Umwelt FHNWde_CH
fhnw.affiliation.institutInstitut für Biomasse und Ressourceneffizienzde_CH
fhnw.oastatus.auroraVersion: Accepted *** Embargo: 24 months *** Licence: CC BY-NC-ND *** URL: https://v2.sherpa.ac.uk/id/publication/14185
fhnw.openAccessCategoryHybrid
fhnw.pagination106970
fhnw.publicationStatePublished
fhnw.targetcollection615f1fcd-40bd-4210-baef-38a1876bcfad
relation.isAuthorOfPublication11ed072b-3933-4356-8cb6-b533a17bcb1b
relation.isAuthorOfPublication9061b5d1-c442-49b7-9e08-2535a52db3db
relation.isAuthorOfPublication.latestForDiscovery11ed072b-3933-4356-8cb6-b533a17bcb1b
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