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Open AccessDOI: 10.3724/2097-213X.2025.JFCT.0037Original Research

Selective Hydrogenation Performance of Pd Catalysts Supported on Alumina Microspheres

College of Chemistry and Chemical Engineering, Xiamen University, Xiamen 361005, China

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Selective Hydrogenation Performance of Pd Catalysts Supported on Alumina Microspheres
Graphical Abstract / Figure
Published In
Journal of Fuel Chemistry and Technology
Published:January 15, 2026Edition:Vol. 54, Issue 6 • pp. 100-112Citation:SHANG Bin et al. (2026), Journal of Fuel Chemistry and Technology
Impact FactorPeer-Reviewed Core
Source Journal燃料化学学报

Key Takeaways & Executive Findings

  • • • Pd/Al2O3-M achieved 95.2% isoprene conversion and 98.3% selectivity to semi-hydrogenated isoamylenes at 60 °C and 1 MPa H2, outperforming conventional Pd/Al2O3 and demonstrating superior selectivity control critical for C5 stream purification. • • In anthraquinone hydrogenation, Pd/Al2O3-M delivered a hydrogenation efficiency of 15.8 g/L, a 27.4% increase over the reference catalyst (12.4 g/L), indicating enhanced productivity for H2O2 synthesis. • • The flower-like alumina microspheres, assembled from nanosheets, increased Pd dispersion and metal-support interaction, resulting in a higher surface Pd content and more abundant active sites, as confirmed by characterization. • • The catalyst maintained stable performance over 24 h in isoprene hydrogenation, evidencing good durability under industrially relevant conditions.

Abstract

Alumina microspheres with a lamellar-assembled flower-like morphology were synthesized via a urea-assisted hydrothermal method and used as supports to prepare Pd/Al2O3-M catalysts by incipient wetness impregnation. The catalytic performance was evaluated in the selective hydrogenation of isoprene and the hydrogenation of 2-ethylanthraquinone for hydrogen peroxide production, and compared with a commercial alumina-supported Pd catalyst (Pd/Al2O3). Characterization revealed that the flower-like structure, composed of stacked nanosheets, promoted high Pd dispersion and enhanced metal-support interaction, leading to a higher surface Pd content and more abundant active sites. Under 60 °C and 1 MPa H2, Pd/Al2O3-M achieved 95.2% conversion of isoprene with 98.3% total selectivity to isoamylenes, and exhibited good stability over 24 h. In anthraquinone hydrogenation, it reached a hydrogenation efficiency of 15.8 g/L, a 27.4% improvement over Pd/Al2O3 (12.4 g/L). The study demonstrates that modulating carrier morphology is an effective strategy to simultaneously enhance activity, selectivity, and stability of Pd catalysts, offering a promising approach for designing efficient hydrogenation catalysts.

1. Introduction

The selective hydrogenation of dienes and alkynes is a pivotal process in the petrochemical industry, particularly for upgrading C5 fractions from naphtha cracking. These streams contain reactive diolefins like isoprene that cause polymerization and fouling in downstream units. Palladium-based catalysts are widely used due to their high activity, but they often suffer from over-hydrogenation, reducing selectivity to valuable mono-olefins. Similarly, the anthraquinone route for hydrogen peroxide production relies on efficient Pd catalysts to achieve high hydrogenation efficiency while suppressing side reactions. Conventional alumina-supported Pd catalysts face limitations in dispersion and metal-support interaction, leading to suboptimal performance. This study addresses these bottlenecks by engineering the carrier morphology—specifically, synthesizing flower-like alumina microspheres with a lamellar structure to enhance Pd dispersion and interaction, thereby improving catalytic performance in both reactions.

The experimental protocol employs a urea-assisted hydrothermal method to produce alumina microspheres with a well-defined flower-like morphology composed of stacked nanosheets. This unique structure provides a high surface area and abundant anchoring sites for Pd nanoparticles, leading to stronger metal-support interactions and higher Pd dispersion compared to commercial alumina. The resulting Pd/Al2O3-M catalyst demonstrates significantly improved activity and selectivity in isoprene hydrogenation and anthraquinone hydrogenation, as evidenced by quantitative metrics. This approach offers a practical strategy for designing high-performance hydrogenation catalysts by modulating support morphology, addressing the industrial need for more efficient and selective catalysts.

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Cite This Research Paper
SHANG Bin, SUN Limin, HU Xiaoli, LAI Weikun, FANG Weiping, YI Xiaodong (2026). Selective Hydrogenation Performance of Pd Catalysts Supported on Alumina Microspheres. Journal of Fuel Chemistry and Technology. https://doi.org/10.3724/2097-213X.2025.JFCT.0037
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Frequently Asked Questions

What is the specific improvement in Pd dispersion and metal-support interaction achieved with the flower-like alumina microspheres compared to commercial alumina?

The flower-like alumina microspheres, composed of stacked nanosheets, provided a higher surface area and more anchoring sites, leading to increased Pd dispersion and stronger metal-support interaction. This was confirmed by characterization, which showed a higher surface Pd content and more abundant active sites on Pd/Al2O3-M compared to Pd/Al2O3.

How does the Pd/Al2O3-M catalyst perform under industrially relevant conditions in terms of stability and selectivity?

Under 60 °C and 1 MPa H2, Pd/Al2O3-M achieved 95.2% conversion of isoprene with 98.3% selectivity to semi-hydrogenated isoamylenes, and maintained stable performance over 24 h, indicating good durability. In anthraquinone hydrogenation, it reached a hydrogenation efficiency of 15.8 g/L, a 27.4% improvement over the reference catalyst.

What are the potential scalability challenges for the urea-assisted hydrothermal synthesis of alumina microspheres?

The synthesis method is scalable in principle, but challenges include controlling the uniformity of the flower-like morphology at larger scales and ensuring reproducibility. The use of urea as a precipitating agent and hydrothermal conditions may require optimization of temperature, pressure, and reaction time to achieve consistent quality. Cost considerations include the need for high-purity precursors and energy-intensive hydrothermal processing.

How does the catalytic performance of Pd/Al2O3-M compare to other advanced Pd catalysts reported in literature?

The performance metrics (95.2% conversion, 98.3% selectivity) are competitive with or superior to many reported Pd-based catalysts for isoprene hydrogenation. The 27.4% improvement in anthraquinone hydrogenation efficiency over a commercial catalyst highlights the advantage of the tailored support morphology. However, direct comparison requires standardized testing conditions.

What is the industrial significance of achieving 98.3% selectivity to isoamylenes in isoprene hydrogenation?

High selectivity to semi-hydrogenated products is crucial to preserve the value of mono-olefins in C5 streams. A selectivity of 98.3% minimizes over-hydrogenation to alkanes, reducing feedstock loss and simplifying downstream separation. This directly impacts process economics by improving yield and reducing waste.

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