Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts
The elevated oxygen content in lignin-derived oil restricts its direct application as a liquid fuel. Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts are commonly employed to enhance the quality of lignin-derived oil via the hydrodeoxygenation (HDO) process. In this study, we s...
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| author | Wen Huang Chengyan Wen Yanting Su Xinghua Zhang Longlong Ma |
| author_facet | Wen Huang Chengyan Wen Yanting Su Xinghua Zhang Longlong Ma |
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| description | The elevated oxygen content in lignin-derived oil restricts its direct application as a liquid fuel. Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts are commonly employed to enhance the quality of lignin-derived oil via the hydrodeoxygenation (HDO) process. In this study, we successfully synthesized Ni-supported Al<sub>2</sub>O<sub>3</sub> catalysts with diverse mesopore structural parameters of the Al<sub>2</sub>O<sub>3</sub> support. Subsequently, we investigated the impacts of mesoporous size and volume on the HDO of guaiacol, a representative model compound of lignin-derived oil. The results indicate that optimizing the mesoporous size can enhance catalyst stability and significantly boost selectivity for cyclohexane. Moreover, an increase in the mesoporous volume can further improve the selectivity of cycloalkanes in the products. When the Ni/meso-Al<sub>2</sub>O<sub>3</sub>-F-100 catalyst was utilized, the cycloalkane selectivity reached 98.8%. During the upgrading of lignin-derived oil, the Ni/meso-Al<sub>2</sub>O<sub>3</sub>-F-200 catalyst, featuring a mesopore size of 4.07 nm and a mesopore volume of 0.286 cm<sup>3</sup>/g, exhibited outstanding performance. Notably, its selectivity for alkanes reached 65.9%, significantly higher than that of the commercial Ni/c-Al<sub>2</sub>O<sub>3</sub> catalyst, which has a mesopore size of 3.83 nm and a mesopore volume of 0.184 cm<sup>3</sup>/g. This work offers valuable insights into the design of efficient and stable Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts for upgrading lignin-derived oil. |
| format | Article |
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| spelling | doaj-art-4bfdfcef07204ff798c998f7369b54a52025-08-20T03:24:33ZengMDPI AGEnergies1996-10732025-06-011812304410.3390/en18123044Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> CatalystsWen Huang0Chengyan Wen1Yanting Su2Xinghua Zhang3Longlong Ma4School of Energy and Environment, Southeast University, Nanjing 211100, ChinaSchool of Energy and Environment, Southeast University, Nanjing 211100, ChinaSchool of Energy and Environment, Southeast University, Nanjing 211100, ChinaSchool of Energy and Environment, Southeast University, Nanjing 211100, ChinaSchool of Energy and Environment, Southeast University, Nanjing 211100, ChinaThe elevated oxygen content in lignin-derived oil restricts its direct application as a liquid fuel. Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts are commonly employed to enhance the quality of lignin-derived oil via the hydrodeoxygenation (HDO) process. In this study, we successfully synthesized Ni-supported Al<sub>2</sub>O<sub>3</sub> catalysts with diverse mesopore structural parameters of the Al<sub>2</sub>O<sub>3</sub> support. Subsequently, we investigated the impacts of mesoporous size and volume on the HDO of guaiacol, a representative model compound of lignin-derived oil. The results indicate that optimizing the mesoporous size can enhance catalyst stability and significantly boost selectivity for cyclohexane. Moreover, an increase in the mesoporous volume can further improve the selectivity of cycloalkanes in the products. When the Ni/meso-Al<sub>2</sub>O<sub>3</sub>-F-100 catalyst was utilized, the cycloalkane selectivity reached 98.8%. During the upgrading of lignin-derived oil, the Ni/meso-Al<sub>2</sub>O<sub>3</sub>-F-200 catalyst, featuring a mesopore size of 4.07 nm and a mesopore volume of 0.286 cm<sup>3</sup>/g, exhibited outstanding performance. Notably, its selectivity for alkanes reached 65.9%, significantly higher than that of the commercial Ni/c-Al<sub>2</sub>O<sub>3</sub> catalyst, which has a mesopore size of 3.83 nm and a mesopore volume of 0.184 cm<sup>3</sup>/g. This work offers valuable insights into the design of efficient and stable Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts for upgrading lignin-derived oil.https://www.mdpi.com/1996-1073/18/12/3044lignin-derived oilNi-based Al<sub>2</sub>O<sub>3</sub> catalystshydrodeoxygenationmesoporeguaiacolcycloalkanes |
| spellingShingle | Wen Huang Chengyan Wen Yanting Su Xinghua Zhang Longlong Ma Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts Energies lignin-derived oil Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts hydrodeoxygenation mesopore guaiacol cycloalkanes |
| title | Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts |
| title_full | Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts |
| title_fullStr | Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts |
| title_full_unstemmed | Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts |
| title_short | Effect of Mesopore Structural Parameters in Alumina Supports on Catalytic Hydrodeoxygenation of Guaiacol to Cycloalkanes via Ni-Supported Al<sub>2</sub>O<sub>3</sub> Catalysts |
| title_sort | effect of mesopore structural parameters in alumina supports on catalytic hydrodeoxygenation of guaiacol to cycloalkanes via ni supported al sub 2 sub o sub 3 sub catalysts |
| topic | lignin-derived oil Ni-based Al<sub>2</sub>O<sub>3</sub> catalysts hydrodeoxygenation mesopore guaiacol cycloalkanes |
| url | https://www.mdpi.com/1996-1073/18/12/3044 |
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