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March 5, 2026Fuel0 citationsOpen Access

Efficient hydrogenolysis of furfural to 1,2-Pentanediol over Ce-Doped Cu-MgO-Al2O3 catalysts

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XLXiaolong LiXWX WANGSLShuheng Lv

Key Points

  • The study aims to enhance the catalytic conversion of furfural to 1,2-pentanediol using Ce-doped catalysts.
  • Developed Ce-doped Cu-based catalysts using a membrane dispersion microreactor.
  • Conducted orthogonal experiments to identify optimal reaction conditions.
  • Analyzed catalyst stability over five cycles of use.
  • Characterized catalysts to assess dispersion and agglomeration of active components.
  • Furfural conversion reached 100% with a selectivity of 44%.
  • Yield of 1,2-pentanediol was 2.2 times higher than that using undoped catalysts.
  • Catalysts showed excellent stability with no activity loss after five cycles.
  • Ce introduction improved dispersion and reduced agglomeration of Cu particles.

Abstract

Application of Ce-Doped Cu-Based Catalysts Prepared by Membrane Dispersion Microreactor in Furfural Hydrogenolysis to 1,2-Pentanediol. • Efficient synthesis of morphologically uniform Ce-doped catalysts using a Membrane dispersion microreactor. • The CuCe/MgO–Al 2 O 3 –500 catalyst enables the efficient hydrogenolysis of furfural to produce 1,2-pentanediol. • Orthogonal experiments elucidated the interrelationships among the various parameters. • Doped Ce creates a synergy with Cu while also tuning the support properties. The conventional production of 1,2-pentanediol (1,2-PeD) from fossil fuels suffers from high energy consumption and significant environmental pressure. Therefore, developing efficient catalysts to enable the hydrolytic hydrogenation of biomass-derived furfural (FF) is an urgent requirement for obtaining a green alternative. In this work, a membrane dispersion microreactor was successfully employed to incorporate Ce into a Cu-based catalyst for the catalytic hydro conversion of FF to 1,2-PeD. The optimum process conditions were determined by orthogonal reaction: 170 ℃, 6 MPa, 5.5 h. Under these conditions, FF was completely converted with the selectivity increased to 44%, resulting in a yield 2.2 times higher than that obtained with the undoped Ce catalyst. Furthermore, the catalyst exhibited excellent stability with no significant activity loss after five cycles of use. The characterization results show that the introduction of Ce significantly improved the dispersion of the active components, effectively suppressed the agglomeration of Cu particles, and increased the specific surface area of the catalysts; the calcination temperature changes the number of basic sites on the surface of the catalyst and affects the mode of adsorption of the intermediate furfuryl alcohol (FFA), thus affecting the catalyst performance.

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Cite This Study

Li et al. (2026) studied this question.

synapsesocial.com/papers/69a91cbed6127c7a504bfa60https://doi.org/10.1016/j.fuel.2026.138957
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