Jan Moravčík , Luděk Kaluža , Florian Bonnet , Karel Soukup , Martin Sádecký , Jaroslav Kocík
{"title":"Preparation of sulphide catalysts for heteroatom elimination in hydrocarbon refining","authors":"Jan Moravčík , Luděk Kaluža , Florian Bonnet , Karel Soukup , Martin Sádecký , Jaroslav Kocík","doi":"10.1016/j.cherd.2025.03.016","DOIUrl":null,"url":null,"abstract":"<div><div>Sulphide catalysts containing Co, Ni, Mo and/or W catalyse hydrogenolysis of carbon sulphur/nitrogen/oxygen bonds and they are widely used in the hydrodesulphurization (HDS) of petroleum fractions. The HDS process produces H<sub>2</sub>S, which is subsequently partially oxidized to water and elemental sulphur in the Claus process. Nevertheless, this process can be overflowed with H<sub>2</sub>S. Sulphide catalysts are therefore investigated for the direct thermo-catalytic decomposition of H<sub>2</sub>S to form H<sub>2</sub> and elemental sulphur. This work tailors on a novel and straightforward preparation method of the unsupported form of Co/MoS<sub>2</sub>, Ni/MoS<sub>2</sub>, Ni/WS<sub>2</sub> and Ni/MoWS<sub>2</sub> catalysts. The aqueous slurry of CoCO<sub>3</sub>.Co(OH)<sub>2</sub> or 2NiCO<sub>3</sub>.3Ni(OH)<sub>2</sub>·4H<sub>2</sub>O reacts with MoS<sub>2</sub>, WS<sub>2</sub> or MoS<sub>2</sub>+WS<sub>2</sub> during milling in a planetary mill. After drying and re-sulphidation, the catalyst is characterised by its specific surface area (<em>S</em><sub><em>BET</em></sub>), free sulphur vacancies (O<sub>2</sub> up-take), crystalline size of molybdenite and/or tungstenite (<em>D</em><sub><em>XRD</em></sub>), activity in thiophene (Th) and 4,6-dimethyldibenzothiophene (4,6DMDBT) HDS, and activity in thermo-catalytic decomposition of H<sub>2</sub>S. We concluded that the prepared catalysts are active in Th and 4,6DMDBT hydrodesulphurization, and thermo-catalytic decomposition of H<sub>2</sub>S. The Ni/WS<sub>2</sub> is the most active in all reactions and also the most selective to direct desulphurization (DDS) during the 4,6DMDBT HDS. WS<sub>2</sub> best suits the studied preparation method.</div></div>","PeriodicalId":10019,"journal":{"name":"Chemical Engineering Research & Design","volume":"216 ","pages":"Pages 515-522"},"PeriodicalIF":3.7000,"publicationDate":"2025-03-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Research & Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0263876225001248","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Sulphide catalysts containing Co, Ni, Mo and/or W catalyse hydrogenolysis of carbon sulphur/nitrogen/oxygen bonds and they are widely used in the hydrodesulphurization (HDS) of petroleum fractions. The HDS process produces H2S, which is subsequently partially oxidized to water and elemental sulphur in the Claus process. Nevertheless, this process can be overflowed with H2S. Sulphide catalysts are therefore investigated for the direct thermo-catalytic decomposition of H2S to form H2 and elemental sulphur. This work tailors on a novel and straightforward preparation method of the unsupported form of Co/MoS2, Ni/MoS2, Ni/WS2 and Ni/MoWS2 catalysts. The aqueous slurry of CoCO3.Co(OH)2 or 2NiCO3.3Ni(OH)2·4H2O reacts with MoS2, WS2 or MoS2+WS2 during milling in a planetary mill. After drying and re-sulphidation, the catalyst is characterised by its specific surface area (SBET), free sulphur vacancies (O2 up-take), crystalline size of molybdenite and/or tungstenite (DXRD), activity in thiophene (Th) and 4,6-dimethyldibenzothiophene (4,6DMDBT) HDS, and activity in thermo-catalytic decomposition of H2S. We concluded that the prepared catalysts are active in Th and 4,6DMDBT hydrodesulphurization, and thermo-catalytic decomposition of H2S. The Ni/WS2 is the most active in all reactions and also the most selective to direct desulphurization (DDS) during the 4,6DMDBT HDS. WS2 best suits the studied preparation method.
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