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.

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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

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article

Effect of catalyst support on dihydroeugenol hydrodeoxygenation on low cost FeNi catalyst to produce renewable alkane fuel

J. Lindén, Matej Huš, Anssi Peuronen, Zuzana Vajglová et al.
3 citations
Applied Catalysis A General
Catalysis and Hydrodesulfurization Studies
2.14
article

Effect of catalyst support on dihydroeugenol hydrodeoxygenation on low cost FeNi catalyst to produce renewable alkane fuel

J. Lindén, Matej Huš, Anssi Peuronen, Zuzana Vajglová, Päivi Mäki‐Arvela, Blaž Likozar, Irina L. Simakova, Olha Yevdokimova, Teija Tirri, Dmitry E. Doronkin, Jessi E. S. van der Hoeven, Dmitry Yu. Murzin, Mika Lastusaari, Mark E. Martínez‐Klimov, Kari Eränen
article en
3 citations

Abstract

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.

Applied Catalysis A GeneralVol. 701
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)
Javna Agencija za Raziskovalno Dejavnost RS, Turun Yliopisto, Biocenter Finland, Business Finland
Affordable and clean energy
Openalex Percentile: Top 14%
Catalysis and Hydrodesulfurization Studies
2.14
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