Catalytic activity of supported ruthenium catalysts in benzene hydrogenation

2025

Closed access Metadata (CSL-JSON)
DOI 10.37878/2708-0080/2025-6.18
Data confidence 70 medium
How this score is calculated

It is built from checkable properties of the record itself: whether the article has a DOI, how many independent sources confirmed its data, whether the required fields are filled in, and how recent the latest confirmation is. Disagreement between sources and a missing identifier lower it. A value of 80 or above means the record was published without further checking; 60 to 79 means it is published at reduced confidence, with a manual check advisable. A record verified by an editor by hand is never pushed below 90 by a recalculation. This scores our data about the article, not the article itself.

Abstract

In this work, Ru/D-type catalysts (Ru = 0.5–1.5%) were investigated using benzene hydrogenation as a model reaction. Structural and morphological characterization was carried out by SEM/EDX, TEM (with particle size distribution in the 1–10 nm range), X-ray diffraction, and nitrogen adsorption. It was found that the porous framework of the support is preserved; upon Ru introduction, the active phase is uniformly dispersed with high dispersion (mainly 3–5 nm particles, with 7–10 nm aggregates appearing at higher loadings). Textural parameters slightly decrease with increasing Ru content (from 60 to 45 m²/g), which is associated with partial pore filling; meanwhile, XRD patterns do not reveal distinct Ru reflections, confirming the high dispersion of the metal. Kinetic measurements (rate–hydrogen uptake) showed a pronounced dependence on both temperature and Ru loading: at 130 °C, the maximum rate for 1.0% Ru/D was ~40·10-1 mol·s-6, and the activation energy was estimated at 40 kJ·mol-1; the activity of 1.5% Ru/D was about twice as high compared to 0.5% Ru/D. These results confirm the efficiency of Ru/D systems in the hydrogenation of aromatic compounds and indicate that a Ru loading of 1.0–1.5% provides an optimal balance between dispersion and catalytic activity.