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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
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Metadata
Document 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
Name from Authors Collection
Affiliations
Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand; National Nanotechnology Center (NANOTEC), National Science and Technology Development Agency (NSTDA), Pathum Thani, 12120, Thailand; College of Nanotechnology, King Mongkut's Institute of Technology, Bangkok, 10520, Thailand; Center of Excellence on Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand; Bio-Circular-Green-Economy Technology & Engineering Center, BCGeTEC, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand
Type
Article
Source Title
Journal of Analytical and Applied Pyrolysis
ISSN
1652370
Year
2025
Volume
190
Open Access
All Open Access; Hybrid Gold Open Access
Publisher
Elsevier B.V.
DOI
10.1016/j.jaap.2025.107145
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. © 2025 The Authors
Keyword
Bifunctional catalyst | Deoxygenation | Isomerization | Palm kernel oil | Rhenium catalyst | Sustainable aviation fuel
Industrial Classification
Knowledge Taxonomy Level 1
Knowledge Taxonomy Level 2
Knowledge Taxonomy Level 3
License
CC BY-NC
Rights
Authors
Publication Source
Scopus
Publication Source
Scopus