A two-step regeneration method for carbon-supported Ru catalysts deactivated by coke and sulfur during hydrothermal gasification
| dc.contributor.author | Sun, Songlan | |
| dc.contributor.author | Bjelić, Saša | |
| dc.contributor.author | Hua, Weicheng | |
| dc.contributor.author | Vogel, Frédéric | |
| dc.contributor.author | Baudouin, David | |
| dc.date.accessioned | 2026-06-19T08:24:49Z | |
| dc.date.issued | 2026 | |
| dc.description.abstract | Catalytic 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.doi | 10.1016/j.supflu.2026.106970 | |
| dc.identifier.issn | 0896-8446 | |
| dc.identifier.issn | 1872-8162 | |
| dc.identifier.uri | https://irf.fhnw.ch/handle/11645/57069 | |
| dc.identifier.uri | https://doi.org/10.26041/fhnw-16534 | |
| dc.language.iso | en | |
| dc.publisher | Elsevier | |
| dc.relation.ispartof | The Journal of Supercritical Fluids | |
| dc.rights.uri | https://creativecommons.org/licenses/by/4.0/ | |
| dc.subject.ddc | 660 - Technische Chemie | |
| dc.title | A two-step regeneration method for carbon-supported Ru catalysts deactivated by coke and sulfur during hydrothermal gasification | |
| dc.type | 01A - Beitrag in wissenschaftlicher Zeitschrift | |
| dc.volume | 234 | |
| dspace.entity.type | Publication | |
| fhnw.InventedHere | Yes | |
| fhnw.ReviewType | peer-reviewed | |
| fhnw.affiliation.hochschule | Hochschule für Technik und Umwelt FHNW | de_CH |
| fhnw.affiliation.institut | Institut für Biomasse und Ressourceneffizienz | de_CH |
| fhnw.oastatus.aurora | Version: Accepted *** Embargo: 24 months *** Licence: CC BY-NC-ND *** URL: https://v2.sherpa.ac.uk/id/publication/14185 | |
| fhnw.openAccessCategory | Hybrid | |
| fhnw.pagination | 106970 | |
| fhnw.publicationState | Published | |
| fhnw.targetcollection | 615f1fcd-40bd-4210-baef-38a1876bcfad | |
| relation.isAuthorOfPublication | 11ed072b-3933-4356-8cb6-b533a17bcb1b | |
| relation.isAuthorOfPublication | 9061b5d1-c442-49b7-9e08-2535a52db3db | |
| relation.isAuthorOfPublication.latestForDiscovery | 11ed072b-3933-4356-8cb6-b533a17bcb1b |
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