Single-step production of sustainable aviation fuel by deoxygenation and isomerization of palm kernel oil using Pt-, Pd-, or Ru-incorporated Re/SAPO-11 catalysts
2
Issued Date
2025-09-01
Resource Type
ISSN
01652370
Scopus ID
2-s2.0-105003389939
Journal Title
Journal of Analytical and Applied Pyrolysis
Volume
190
Rights Holder(s)
SCOPUS
Bibliographic Citation
Journal of Analytical and Applied Pyrolysis Vol.190 (2025)
Suggested Citation
Praikaew W., Chuseang J., Itthibenchapong V., Ratchahat S., Chaiwat W., Koo-Amornpattana W., Sakdaronnarong C., Eiad-ua A., Assabumrungrat S., Srifa A. Single-step production of sustainable aviation fuel by deoxygenation and isomerization of palm kernel oil using Pt-, Pd-, or Ru-incorporated Re/SAPO-11 catalysts. Journal of Analytical and Applied Pyrolysis Vol.190 (2025). doi:10.1016/j.jaap.2025.107145 Retrieved from: https://repository.li.mahidol.ac.th/handle/123456789/109914
Title
Single-step production of sustainable aviation fuel by deoxygenation and isomerization of palm kernel oil using Pt-, Pd-, or Ru-incorporated Re/SAPO-11 catalysts
Corresponding Author(s)
Other Contributor(s)
Abstract
The production of sustainable aviation fuel (SAF) from agricultural bioresources is recognized as a sustainable biorefinery application that aligns with the United Nations Sustainable Development Goal 7 (Affordable and clean energy). Herein, bimetallic catalysts (Pt-Re, Pd-Re, and Ru-Re) supported on SAPO-11 were synthesized using a conventional impregnation method for single-step production of SAF through the deoxygenation and isomerization of palm kernel oil. These catalysts were compared with monometallic catalysts (Re, Pt, Pd, and Ru) as benchmarks. Interestingly, the incorporation of Pt, Pd, or Ru with Re/SAPO-11 markedly enhanced deoxygenation and isomerization activities, achieving nearly theoretical yields of 70 % for n- and iso-alkanes with 100 % triglycerides (TGs) conversion. Among the tested catalysts, the bimetallic Ru-Re catalyst produced the highest jet fuel yield of 60 % with a high iso-to-n-alkane (i/n) ratio of 1.2 under conditions of 360°C reaction temperature, H2 pressure of 30 bar, weight hourly space velocity of 2 h−1, and an H2/oil ratio of 1000 N(cm3/cm3). Additionally, the bimetallic Ru-Re catalyst demonstrated excellent stability over 60 h of continuous operation, maintaining exceptional compositions of straight-chain and branched alkane products. The unrefined biofuel produced with the Ru-Re catalyst exhibited the lowest freezing point (Tf) at −31.9°C, as determined by differential scanning calorimetry, without the use of additive compounds. Furthermore, when blended with commercial Jet A at 10 % (v/v), the resulting jet fuel blend achieved a Tf of ∼–60.1°C, meeting Jet A standards.