Tom Vandevyvere , Maarten K. Sabbe , Pedro S.F. Mendes , Joris W. Thybaut , Jeroen Lauwaert
{"title":"NiCu-based catalysts for the low-temperature hydrodeoxygenation of anisole: Effect of the metal ratio on SiO2 and γ-Al2O3 supports","authors":"Tom Vandevyvere , Maarten K. Sabbe , Pedro S.F. Mendes , Joris W. Thybaut , Jeroen Lauwaert","doi":"10.1016/j.greenca.2023.10.001","DOIUrl":null,"url":null,"abstract":"<div><p>The effects of the metal ratio of NiCu catalysts on the low-temperature hydrodeoxygenation (HDO) of anisole were assessed on a neutral SiO<sub>2</sub> and an acidic γ-Al<sub>2</sub>O<sub>3</sub> support. The activity of SiO<sub>2</sub>-supported catalysts increases with the Ni content in the NiCu phase, related to Ni’s hydrogenation capacity. In contrast, on a γ-Al<sub>2</sub>O<sub>3</sub> support, the activity decreases with the Ni content. Overall, Al<sub>2</sub>O<sub>3</sub>-supported catalysts, exhibiting a smaller NiCu alloy particle size, are more active than SiO<sub>2</sub>-supported ones. In terms of selectivity, SiO<sub>2</sub>-supported catalysts mainly hydrogenate anisole to methoxycyclohexane, while, particularly at higher conversions, γ-Al<sub>2</sub>O<sub>3</sub>-supported catalysts are able to further convert methoxycyclohexane to cyclohexane, demonstrating the importance of acid sites for low-temperature HDO. The Ni/Cu ratio also steers the selectivity, but not the catalyst stability. Deactivation phenomena are only support dependent: while on SiO<sub>2</sub>-supported catalysts, active site sintering occurs, attributed to weak stabilization of metal particles by the support, acid catalyzed coking is the main cause of deactivation on the γ-Al<sub>2</sub>O<sub>3</sub>-supported catalysts.</p></div>","PeriodicalId":100595,"journal":{"name":"Green Carbon","volume":"1 2","pages":"Pages 170-184"},"PeriodicalIF":0.0000,"publicationDate":"2023-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S2950155523000204/pdfft?md5=6a7bb12a71ab448225e06d085f677ca5&pid=1-s2.0-S2950155523000204-main.pdf","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Green Carbon","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2950155523000204","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
The effects of the metal ratio of NiCu catalysts on the low-temperature hydrodeoxygenation (HDO) of anisole were assessed on a neutral SiO2 and an acidic γ-Al2O3 support. The activity of SiO2-supported catalysts increases with the Ni content in the NiCu phase, related to Ni’s hydrogenation capacity. In contrast, on a γ-Al2O3 support, the activity decreases with the Ni content. Overall, Al2O3-supported catalysts, exhibiting a smaller NiCu alloy particle size, are more active than SiO2-supported ones. In terms of selectivity, SiO2-supported catalysts mainly hydrogenate anisole to methoxycyclohexane, while, particularly at higher conversions, γ-Al2O3-supported catalysts are able to further convert methoxycyclohexane to cyclohexane, demonstrating the importance of acid sites for low-temperature HDO. The Ni/Cu ratio also steers the selectivity, but not the catalyst stability. Deactivation phenomena are only support dependent: while on SiO2-supported catalysts, active site sintering occurs, attributed to weak stabilization of metal particles by the support, acid catalyzed coking is the main cause of deactivation on the γ-Al2O3-supported catalysts.