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Co-Processing of Fossil Feedstock with Lignin-Derived Model Compound Isoeugenol over Fe-Ni/H-Y-5.1 Catalysts Full article

Journal Journal of Catalysis
ISSN: 0021-9517 , E-ISSN: 1090-2694
Output data Year: 2023, Volume: 421, Pages: 101-116 Pages count : 16 DOI: 10.1016/j.jcat.2023.03.016
Tags Co-processing; Bio-fuel; Lignin-derivative; Fe-Ni catalysts; Hydrodeoxygenation; Isoeugenol; Hexadecane
Authors Vajglová Zuzana 1 , Gauli Bibesh 1 , Mäki-Arvela Päivi 1 , Simakova Irina L. 2 , Kumar Narendra 1 , Eränen Kari 1 , Tirri Teija 1 , Lassfolk Robert 1 , Peurla Markus 3 , Doronkin Dmitry E. 4 , Murzin Dmitry Yu. 1
Affiliations
1 Åbo Akademi University, Johan Gadolin Process Chemistry Centre, Henriksgatan 2, 20500 Turku/Åbo, Finland
2 Boreskov Institute of Catalysis, Novosibirsk, Russia
3 Institute of Biomedicine, University of Turku, Kiinamyllynkatu 10, 20520 Turku, Finland
4 Institute of Chemical Technology and Polymer Chemistry, and Institute of Catalysis Research and Technology, Karlsruhe Institute of Technology, Kaiserstrasse 12, 76131 Karlsruhe, Germany

Funding (2)

1 Ministry of Science and Higher Education of the Russian Federation 0239-2021-0008
2 Business Finland

Abstract: Co-processing of n-hexadecane with lignin derived isoeugenol as a model compound was investigated in this work using low-cost mono- and bimetallic iron and nickel supported on H-Y-5.1 zeolite. Different FeNi metal ratios in the catalyst led to different reaction rates of processes and product distribution. The presence of just 0.26 wt% isoeugenol in the mixture with n-hexadecane made hydroisomerization-hydrocracking of the latter two-fold less active. Catalysts with smaller metal particle sizes, lower than 6 nm were more efficient pointing out on structure sensitivity. Extremely high activity in co-processing was obtained over 2 wt% Fe – 8 wt% Ni/H-Y-5.1 catalysts with the median metal particle size of 4.6 nm and metals-to-acid site ratio of 8.6. Fe catalyst were much less active in isoeugenol hydrodeoxygenation, while high cracking activity of hexadecane was observed in the presence of Ni. Alkylation of n-hexadecane was a feature of 8 wt% Fe – 2 wt% Ni/H-Y-5.1, whereas, over the 5 wt% Fe – 5 wt% Ni/H-Y5.1 bifunctional catalyst no undesired oxygen-containing cyclic products were detected. This catalyst exhibited the highest hydrogen consumption according to temperature programmed desorption, which can serve as a marker for efficient hydrodeoxygenation. The spent catalysts contained ca 40 wt% of coke with predominantly aliphatic species.
Cite: Vajglová Z. , Gauli B. , Mäki-Arvela P. , Simakova I.L. , Kumar N. , Eränen K. , Tirri T. , Lassfolk R. , Peurla M. , Doronkin D.E. , Murzin D.Y.
Co-Processing of Fossil Feedstock with Lignin-Derived Model Compound Isoeugenol over Fe-Ni/H-Y-5.1 Catalysts
Journal of Catalysis. 2023. V.421. P.101-116. DOI: 10.1016/j.jcat.2023.03.016 WOS Scopus РИНЦ AN OpenAlex
Dates:
Submitted: Sep 21, 2022
Accepted: Mar 6, 2023
Published online: Mar 9, 2023
Published print: May 1, 2023
Identifiers:
Web of science: WOS:000955293200001
Scopus: 2-s2.0-85150025632
Elibrary: 54082257
Chemical Abstracts: 2023:523166
OpenAlex: W4323664593
Citing:
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Scopus 12
Web of science 12
Elibrary 8
OpenAlex 11
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