Lattice Hydroxyl‐Assisted Platinum Single Atom Catalyst Toward Hydrogen Production From Methanol Aqueous Reforming

H Hao Meng S Shaoteng Yuan (State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China) Z Zhiming Yin (State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China) T Tianyao Shen (State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China) K Kai Feng (Department of Chemical Engineering) H Haisong Feng (State Key Laboratory of Chemical Resource Engineering, Beijing Engineering Center for Hierarchical Catalysts) L Lei Wang L Lirong Zheng S Song Hong (State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China) Y Yusen Yang (State Key Laboratory of Chemical Resource Engineering) J Jian Zhang X Xin Zhang M Min Wei (Department of Chemistry and Key Laboratory for Preparation and Application of Ordered Structural Materials of Guangdong Province)

Abstract

ABSTRACT Methanol aqueous reforming reaction (APRM) provides a green and clean route towards hydrogen production, in which the structure design and preparation of efficient catalysts remains a challenge. Herein, we report a platinum catalyst supported on the porous hydroxyl lanthanum oxide, which is prepared via glycine combustion method followed by a reduction process. The optimized 0.8%Pt/La catalyst, which is featured by Pt single‐atom dispersed on a La 2 (OH) 2 x O 3‐2 x support, exhibits an extraordinary catalytic performance towards APRM. A H 2 production rate of 7672 µmol H2 g cat −1 min −1 and an average turnover frequency (ATOF) of 11973 h ‒1 are obtained, which is preponderant to the state‐of‐the‐art catalysts. An in‐depth investigation based on kinetic isotope analysis, in situ spectroscopy characterizations and theoretical calculations substantiates that Pt single atom coordinated with adjacent lattice hydroxyl (OH L ) with electron transfer from Pt to support serves as the intrinsic active site, in which the Pt δ + site promotes the dehydrogenation of methoxyl whilst lattice hydroxyl directly participates in the oxidative coupling process (CH 2 O* + OH L → CH 2 OOH*). Furthermore, the Pt δ + −(OH L ) x −La interface sites can remarkably reduce the energy barrier of CH 2 OOH* dehydrogenation (rate‐determining step), and the resulting hydroxyl vacancies can boost H 2 O dissociation to recover consumed OH L , accounting for the exceptional catalytic performance.

Article Details

Volume / Issue Vol. 65, Issue 21
Published May 18, 2026
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (13)

H

Hao Meng

S

Shaoteng Yuan

State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China

Z

Zhiming Yin

State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China

T

Tianyao Shen

State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China

K

Kai Feng

Department of Chemical Engineering

H

Haisong Feng

State Key Laboratory of Chemical Resource Engineering, Beijing Engineering Center for Hierarchical Catalysts

L

Lei Wang

L

Lirong Zheng

S

Song Hong

State Key Laboratory of Chemical Resource Engineering Beijing University of Chemical Technology Beijing P. R. China

Y

Yusen Yang

State Key Laboratory of Chemical Resource Engineering

J

Jian Zhang

X

Xin Zhang

M

Min Wei

Department of Chemistry and Key Laboratory for Preparation and Application of Ordered Structural Materials of Guangdong Province