Effect of catalyst support on dihydroeugenol hydrodeoxygenation on low cost FeNi catalyst to produce renewable alkane fuel
Solventless hydrodeoxygenation of dihydroeugenol was investigated in a continuous reactor at 300 °C under 30 bar over different nickel-iron catalysts, prepared using a two-step impregnation method. The following catalysts were studied: mesoporous FeNi/Al 2 O 3 , FeNi/SiO 2 and FeNi/H-MCM-48 as well as microporous FeNi/H-Beta-300, FeNi/H-Beta-38, FeNi/H-Y-5.1, FeNi/H-MCM-48 and FeNi/USY-30. The catalysts were characterized by SEM coupled with energy dispersive X-ray analysis, Mössbauer and X-ray absorption spectroscopy, hydrogen TPR, X-ray diffraction, TEM, nitrogen physisorption and FTIR pyridine adsorption. DFT calculations were performed to elucidate the role of Fe and Ni. The results revealed that FeNi/Al 2 O 3 was the most active and stable in dihydroeugenol hydrodeoxygenation. Complete conversion of dihydroeugenol was obtained and the yield of the main product propylcyclohexane was varying in the range 84–88 %. FeNi/Al 2 O 3 catalyst exhibited 3.4 nm metal particles and contained FeNi alloy particles with the fcc metallic structure. No deactivation was observed for FeNi/ Al 2 O 3 during 5 hours time-on-stream due to the presence of Ni-rich particles with iron-enriched outer surface confirmed by EXAFS. Fe was shown to be responsible for deoxygenation, while Ni promotes hydrogenation. Catalyst deactivation was observed for all other catalysts except for FeNi/Al 2 O 3 with increasing time-on-stream under the same reaction conditions due to their higher Brønsted to Lewis acid site ratio and larger average metal particle size in comparison to FeNi/Al 2 O 3 . • Several iron- nickel supported catalysts were studied in solventless hydrodeoxygenation of dihydroeugenol. • FeNi/Al 2 O 3 was active and stable in dihydroeugenol hydrodeoxygenation. • Stability due to presence of Ni-rich particles with Fe -enriched outer surface confirmed by EXAFS • Propylcyclohexane yield of 84–88 % at complete conversion.
Authors
- J. Lindén (ORCID: https://orcid.org/0000-0002-6155-3026)
- Matej Huš (ORCID: https://orcid.org/0000-0002-8318-5121)
- Anssi Peuronen (ORCID: https://orcid.org/0000-0002-2504-8196)
- Zuzana Vajglová (ORCID: https://orcid.org/0000-0001-8163-6104)
- Päivi Mäki‐Arvela (ORCID: https://orcid.org/0000-0002-7055-9358)
- Blaž Likozar (ORCID: https://orcid.org/0000-0001-7226-4302)
- Irina L. Simakova (ORCID: https://orcid.org/0000-0002-5138-4847)
- Olha Yevdokimova
- Teija Tirri (ORCID: https://orcid.org/0000-0001-8522-7105)
- Dmitry E. Doronkin (ORCID: https://orcid.org/0000-0003-3930-3204)
- Jessi E. S. van der Hoeven (ORCID: https://orcid.org/0000-0001-9832-289X)
- Dmitry Yu. Murzin (ORCID: https://orcid.org/0000-0003-0788-2643)
- Mika Lastusaari (ORCID: https://orcid.org/0000-0003-1872-0391)
- Mark E. Martínez‐Klimov
- Kari Eränen
Institutions
- Karlsruhe Institute of Technology (DE)
- Åbo Akademi University (FI)
- University of Turku (FI)
- Turku University of Applied Sciences (FI)
- Utrecht University (NL)
- ŠKUC Association (SI)
- National Institute of Chemistry (SI)
Publication Details
- Journal
- Applied Catalysis A General
- Published
- 2025-04-23
- DOI
- https://doi.org/10.1016/j.apcata.2025.120307
- Citations
- 3
- Primary Topic
- Catalysis and Hydrodesulfurization Studies
- Type
- article
- Field-Weighted Citation Impact
- 2.14
Funders
- Javna Agencija za Raziskovalno Dejavnost RS
- Turun Yliopisto
- Biocenter Finland
- Business Finland