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Highly Efficient Process for Producing a Jet-A1 Biofuel Component Through Hydroprocessing Soybean Oil over Ni and Pt Catalysts

Author

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  • Marek Główka

    (High Pressure Processes Research Group, Lukasiewicz Research Network—Institute of Heavy Organic Synthesis “Blachownia”, Energetykow 9, 47-225 Kedzierzyn-Kozle, Poland
    Faculty of Chemistry, PhD School, Silesian University of Technology, Akademicka 2a, 44-100 Gliwice, Poland)

  • Jan Krzysztof Wójcik

    (High Pressure Processes Research Group, Lukasiewicz Research Network—Institute of Heavy Organic Synthesis “Blachownia”, Energetykow 9, 47-225 Kedzierzyn-Kozle, Poland)

  • Przemysław Boberski

    (High Pressure Processes Research Group, Lukasiewicz Research Network—Institute of Heavy Organic Synthesis “Blachownia”, Energetykow 9, 47-225 Kedzierzyn-Kozle, Poland)

  • Piotr Józef Woszczyński

    (Analytics Research Group, Lukasiewicz Research Network—Institute of Heavy Organic Synthesis “Blachownia”, Energetykow 9, 47-225 Kedzierzyn-Kozle, Poland)

  • Ewa Sabura

    (Analytics Research Group, Lukasiewicz Research Network—Institute of Heavy Organic Synthesis “Blachownia”, Energetykow 9, 47-225 Kedzierzyn-Kozle, Poland)

Abstract

This study presents an efficient process for producing sustainable aviation fuel (SAF) from soybean oil through hydrodeoxygenation (HDO) and hydroisomerization (HI). The research utilized a commercial nickel catalyst for the HDO step, and a newly developed platinum catalyst supported on SAPO-11 zeolite for the hydroisomerization (HI) stage. The process parameters, including temperature and pressure, were optimized to maximize conversion efficiency and meet ASTM D7566 standards. The results indicate that the HDO process using the nickel catalyst achieved a high yield of n-alkanes (97.8% ± 0.4%) with complete conversion of triglycerides. In the subsequent hydroisomerization step, the platinum catalyst demonstrated excellent selectivity for Jet-A1 fuel, yielding a bio-jet fraction of 87.5% ± 1.6% in a 200 h continuous test. This study also highlights the minimal coking phenomena and high catalyst stability throughout the process. This work suggests that soybean oil, as a readily available feedstock, could significantly contribute to the production of SAF and reduce greenhouse gas emissions in the aviation sector. Additionally, the optimization of temperature and pressure conditions is crucial for enhancing the yield and quality of the final bio-jet product.

Suggested Citation

  • Marek Główka & Jan Krzysztof Wójcik & Przemysław Boberski & Piotr Józef Woszczyński & Ewa Sabura, 2024. "Highly Efficient Process for Producing a Jet-A1 Biofuel Component Through Hydroprocessing Soybean Oil over Ni and Pt Catalysts," Energies, MDPI, vol. 17(23), pages 1-21, December.
    • Handle: RePEc:gam:jeners:v:17:y:2024:i:23:p:6195-:d:1539458
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    References listed on IDEAS

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    1. Yoosuk, Boonyawan & Sanggam, Paphawee & Wiengket, Sakdipat & Prasassarakich, Pattarapan, 2019. "Hydrodeoxygenation of oleic acid and palmitic acid to hydrocarbon-like biofuel over unsupported Ni-Mo and Co-Mo sulfide catalysts," Renewable Energy, Elsevier, vol. 139(C), pages 1391-1399.
    2. Morenike Ajike Peters & Carine Tondo Alves & Jude Azubuike Onwudili, 2023. "A Review of Current and Emerging Production Technologies for Biomass-Derived Sustainable Aviation Fuels," Energies, MDPI, vol. 16(16), pages 1-40, August.
    3. Giuseppe Di Vito Nolfi & Katia Gallucci & Leucio Rossi, 2021. "Green Diesel Production by Catalytic Hydrodeoxygenation of Vegetables Oils," IJERPH, MDPI, vol. 18(24), pages 1-28, December.
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