New bi-functional catalysts for a novel continuous production of propylene oxide with in-situ generated hydrogen peroxide

• Combined DSHP and HPPO in liquid phase at mild conditions. • AuPd nanoparticles preferentially deposited on anatase in commercial TS-1. • Continuous low-temperature operation successfully demonstrated. • AuPd/TS-1 catalysts achieved relatively high propylene oxide selectivity. • Integrated process more efficient than separated reactions. Combined direct synthesis of hydrogen peroxide (DSHP) and epoxidation of propene to propylene oxide with hydrogen peroxide (HPPO) was carried out first time in a continuous laboratory-scale trickle bed reactor operating under mild conditions of 8 bar and 10°C. The reaction was performed with bimetallic gold–palladium catalysts supported on titanium silicalite 1 (TS-1). Three series of catalysts were synthesized from two different lots of TS-1 and different calcination heating rates. The catalysts were extensively examined using XRD, SEM-EDS, TEM-SAED, STEM-EDS, ICP-OES, XPS, UV–vis DRS, nitrogen-physisorption and ammonia-TPD. The metal-modification of TS-1 containing anatase impurities was shown first time, where the preferential deposition site for the bimetallic nanoparticles was on the minor anatase phase, found in different amounts in commercial TS-1 materials. In the first catalyst series, a higher anatase content was found, which led to a decrease of the AuPd nanoparticle size compared to the second and third series. Increasing the heating rate in calcination resulted in an additional reduction of the AuPd nanoparticle size. The propylene oxide selectivity was 55.7 % using catalysts of the third series, while the propylene oxide production rate was 0.17 mol·kg cat -1 ·h −1 with 19.2 % propene conversion. The use of a palladium-poor alloy was found to be crucial for this reaction system to limit the hydrogenation of hydrogen peroxide and propene. The catalyst activity was investigated in the separate processes of DSHP and epoxidation to get a deeper insight into the reaction mechanism. In the switch experiments, DSHP followed by the combined reaction of DSHP and HPPO, the competing side reactions, hydrogenation of propene and hydrogen peroxide were confirmed. In another experiment, the dismutation of hydrogen peroxide was disproved.

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Publication Details

Journal
Journal of Catalysis
Published
2025-12-13
DOI
https://doi.org/10.1016/j.jcat.2025.116637
Citations
1
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
0.54
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article

New bi-functional catalysts for a novel continuous production of propylene oxide with in-situ generated hydrogen peroxide

1 citations
Journal of Catalysis
Zeolite Catalysis and Synthesis
0.54
article

New bi-functional catalysts for a novel continuous production of propylene oxide with in-situ generated hydrogen peroxide

article en
1 citations

Abstract

• Combined DSHP and HPPO in liquid phase at mild conditions. • AuPd nanoparticles preferentially deposited on anatase in commercial TS-1. • Continuous low-temperature operation successfully demonstrated. • AuPd/TS-1 catalysts achieved relatively high propylene oxide selectivity. • Integrated process more efficient than separated reactions. Combined direct synthesis of hydrogen peroxide (DSHP) and epoxidation of propene to propylene oxide with hydrogen peroxide (HPPO) was carried out first time in a continuous laboratory-scale trickle bed reactor operating under mild conditions of 8 bar and 10°C. The reaction was performed with bimetallic gold–palladium catalysts supported on titanium silicalite 1 (TS-1). Three series of catalysts were synthesized from two different lots of TS-1 and different calcination heating rates. The catalysts were extensively examined using XRD, SEM-EDS, TEM-SAED, STEM-EDS, ICP-OES, XPS, UV–vis DRS, nitrogen-physisorption and ammonia-TPD. The metal-modification of TS-1 containing anatase impurities was shown first time, where the preferential deposition site for the bimetallic nanoparticles was on the minor anatase phase, found in different amounts in commercial TS-1 materials. In the first catalyst series, a higher anatase content was found, which led to a decrease of the AuPd nanoparticle size compared to the second and third series. Increasing the heating rate in calcination resulted in an additional reduction of the AuPd nanoparticle size. The propylene oxide selectivity was 55.7 % using catalysts of the third series, while the propylene oxide production rate was 0.17 mol·kg cat -1 ·h −1 with 19.2 % propene conversion. The use of a palladium-poor alloy was found to be crucial for this reaction system to limit the hydrogenation of hydrogen peroxide and propene. The catalyst activity was investigated in the separate processes of DSHP and epoxidation to get a deeper insight into the reaction mechanism. In the switch experiments, DSHP followed by the combined reaction of DSHP and HPPO, the competing side reactions, hydrogenation of propene and hydrogen peroxide were confirmed. In another experiment, the dismutation of hydrogen peroxide was disproved.

Journal of CatalysisVol. 454
Åbo Akademi University (FI), University of Turku (FI), Turku University of Applied Sciences (FI), Istituto Nazionale di Fisica Nucleare, Sezione di Napoli (IT), École des Métiers de l’Environnement (FR), Oulu University of Applied Sciences (FI), University of Naples Federico II (IT), University of Oulu (FI)
Openalex Percentile: Top 27%
Zeolite Catalysis and Synthesis
0.54
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