This is one of the first reports, which is related to hydrogen production through formic acid
decomposition over Pd/ZnO catalysts widely used for methanol steam-reforming. These catalysts
have been investigated in comparison with Pt/ZnO and Pd/Al2O3 catalysts as well as ZnO support.
HAADF/STEM, XRD, XPS and DRIFTS in situ studies of the systems were performed. The
measured catalyst activity corresponds to the following order: Pd/Al2O3≥Pd/ZnO>Pt/ZnO>ZnO.
Among the studied catalysts, Pd/ZnO showed the highest selectivity to hydrogen (up to 99.3%).
This was assigned to the formation of a PdZn alloy during the reductive pre-treatment of the
catalyst. An increase of the pre-treatment temperature from 573 to 773 K led to a significant
increase of the mean PdZn (PtZn) nanoparticle size. However, the catalyst activity did not change,
but the selectivity to hydrogen increased. These features closely remind the behavior of Pd/ZnO
catalysts in methanol steam reforming implying that the mechanism of formic acid decomposition
involves the same key steps and active sites.
History
Publication
Applied Catalysis A: General;561, pp. 96-103
Publisher
Elsevier
Note
peer-reviewed
The full text of this article will not be available in ULIR until the embargo expires on the 24/05/2020
Rights
This is the author’s version of a work that was accepted for publication in Applied Catalysis A: General . Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Applied Catalysis A: General, 2018, 561, pp. 96-103, https://doi.org/10.1016/j.apcata.2018.05.025