3D-printed Pd/AC catalytic impellers for overcoming mass transfer limitations in hydrogen production from formic acid

Integral 3D-printed Pd/AC catalytic impellers were developed for intensified hydrogen production via formic acid (FA) dehydrogenation. Three-bladed structures with different infill densities (35, 50 and 100%) were fabricated by direct ink writing of whey-derived precursors. Pd (5 wt%) was incorporated by wet impregnation, producing catalysts with similar properties (Pd particle size ∼2 nm, dispersion ∼45%, Pd 2+ /Pd 0 ≈ 7). The CAT#35 impeller (35% infill) showed the best performance, with TOF 0 three times higher than the dense CAT#100. This improvement was attributed to the open mesh architecture, which mitigated external mass transfer limitations, while maintaining stable activity over 15 cycles and 140 h of operation. A kinetic model based on a Langmuir-Hinshelwood-Hougen-Watson equation with a first-order dependence on FA concentration and hydrogen inhibition (E a = 34.8 kJ mol −1 ) was proposed. Catalyst deactivation followed a first-order decay model with residual activity, depending on the temperature and initial FA concentration.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2026-09-11
DOI
https://doi.org/10.1016/j.ijhydene.2026.157531
Primary Topic
Carbon dioxide utilization in catalysis
Type
article
Field-Weighted Citation Impact
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article

3D-printed Pd/AC catalytic impellers for overcoming mass transfer limitations in hydrogen production from formic acid

J.Á. Menéndez, Miguel A. Montes‐Morán, David Ortiz, A. Quintanilla et al.
International Journal of Hydrogen Energy
Carbon dioxide utilization in catalysis
article

3D-printed Pd/AC catalytic impellers for overcoming mass transfer limitations in hydrogen production from formic acid

J.Á. Menéndez, Miguel A. Montes‐Morán, David Ortiz, A. Quintanilla, Isabel Sanz‐Abengozar, Raúl Llamas-Unzueta, Jose A. Casas
article en

Abstract

Integral 3D-printed Pd/AC catalytic impellers were developed for intensified hydrogen production via formic acid (FA) dehydrogenation. Three-bladed structures with different infill densities (35, 50 and 100%) were fabricated by direct ink writing of whey-derived precursors. Pd (5 wt%) was incorporated by wet impregnation, producing catalysts with similar properties (Pd particle size ∼2 nm, dispersion ∼45%, Pd 2+ /Pd 0 ≈ 7). The CAT#35 impeller (35% infill) showed the best performance, with TOF 0 three times higher than the dense CAT#100. This improvement was attributed to the open mesh architecture, which mitigated external mass transfer limitations, while maintaining stable activity over 15 cycles and 140 h of operation. A kinetic model based on a Langmuir-Hinshelwood-Hougen-Watson equation with a first-order dependence on FA concentration and hydrogen inhibition (E a = 34.8 kJ mol −1 ) was proposed. Catalyst deactivation followed a first-order decay model with residual activity, depending on the temperature and initial FA concentration.

International Journal of Hydrogen EnergyVol. 275
Instituto Nacional del Carbón (ES), Universidad Autónoma de Madrid (ES)
Gobierno del Principado de Asturias, Ministerio de Ciencia, Innovación y Universidades
Openalex Percentile: Top 25%
Carbon dioxide utilization in catalysis
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