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

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, H 2 pressure of 30 bar, weight hourly space velocity of 2 h −1 , and an H 2 /oil ratio of 1000 N(cm 3 /cm 3 ). 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 (T f ) 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 T f of ∼–60.1°C, meeting Jet A standards. • Pt, Pd, or Ru-Re/SAPO-11 were developed for SAF production from palm kernel oil. • Single-step production of SAF was gained by simultaneous deoxygenation and isomerization. • Highest jet yield comprising normal and iso alkanes was obtained using the RuRe/SAPO-11. • Bimetallic RuRe/SAPO-11demonstrated the excellent stability for 60 h of time-on-stream. • Tf of the blended jet fuel using RuRe/SAPO-11 was –60.1 °C in the range of Jet A standard.

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Journal
Journal of Analytical and Applied Pyrolysis
Published
2025-04-22
DOI
https://doi.org/10.1016/j.jaap.2025.107145
Citations
3
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
Field-Weighted Citation Impact
2.14
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article

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

Apiluck Eiad‐ua, Wanida Koo-amornpattana, Sakhon Ratchahat, Suttichai Assabumrungrat et al.
3 citations
Journal of Analytical and Applied Pyrolysis
Catalysis and Hydrodesulfurization Studies
2.14
article

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

Apiluck Eiad‐ua, Wanida Koo-amornpattana, Sakhon Ratchahat, Suttichai Assabumrungrat, Chularat Sakdaronnarong, Wanichaya Praikaew, Atthapon Srifa, Jirawat Chuseang, Weerawut Chaiwat, Vorranutch Itthibenchapong
article en
3 citations

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, H 2 pressure of 30 bar, weight hourly space velocity of 2 h −1 , and an H 2 /oil ratio of 1000 N(cm 3 /cm 3 ). 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 (T f ) 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 T f of ∼–60.1°C, meeting Jet A standards. • Pt, Pd, or Ru-Re/SAPO-11 were developed for SAF production from palm kernel oil. • Single-step production of SAF was gained by simultaneous deoxygenation and isomerization. • Highest jet yield comprising normal and iso alkanes was obtained using the RuRe/SAPO-11. • Bimetallic RuRe/SAPO-11demonstrated the excellent stability for 60 h of time-on-stream. • Tf of the blended jet fuel using RuRe/SAPO-11 was –60.1 °C in the range of Jet A standard.

Journal of Analytical and Applied PyrolysisVol. 190
National Science and Technology Development Agency (TH), Chulalongkorn University (TH), Mahidol University (TH), National Nanotechnology Center (TH), King Mongkut's University of Technology North Bangkok (TH), King Mongkut's Institute of Technology Ladkrabang (TH)
Industry, innovation and infrastructure
Openalex Percentile: Top 14%
Catalysis and Hydrodesulfurization Studies
2.14
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