A Synergistic C <sub>2+</sub> Alcohols/Olefins‐Intermediated Pathway Boosts CO <sub>2</sub> Hydrogenation to Aromatics

X Xinze Bi (College of New Energy, State Key Laboratory of Heavy Oil Processing) Q Qi Li N Na Zhao Z Zhaorui Zhang (School of Environmental Science and Technology) Y Yang Wang K Kaixuan Huo (College of New Energy China University of Petroleum (East China) Qingdao China) X Xudong Yu S Song Li Z Zhongxu Bian (College of New Energy China University of Petroleum (East China) Qingdao China) Y Yuanyuan Han X Xiaojie Liu Y Yifan Yan W Wenhang Wang (Department of Applied Chemistry, School of Engineering, University of Toyama, Gofuku 3190, Toyama 930-8555, Japan) W Wengang Xu (College of New Energy, State Key Laboratory of Heavy Oil Processing) Q Qiang Liu N Noritatsu Tsubaki (Department of Applied Chemistry, Graduate School of Engineering, University of Toyama, 3190 Gofuku, Toyama 930-8555, Japan) M Mingbo Wu (College of New Energy, State Key Laboratory of Heavy Oil Processing)

Abstract

ABSTRACT The rational design of highly efficient catalysts and the development of novel reaction pathways are eternal themes and central challenges in the field of chemical synthesis. Here, we design a dual‐engine catalytic system for CO 2 hydrogenation to aromatics via a synergistic C 2+ alcohols/olefins pathway. The dual‐engine catalytic system initiated by FeCo active sites and CuZnAl promoters guarantees the continuous C 2+ alcohols/olefins supply, delivering a record‐breaking aromatics yield (31.1%) with the aid of aromatization component H‐ZSM‐5. Multiple characterization and theoretical simulations reveal that C 2+ alcohols trigger carbon‐chain growth through oxonium‐mediated rapid carbocation generation via a low‐barrier “protonation‐dehydration” sequence, whereas olefins serve as π‐substrates to propagate carbon‐chain. This synergy accelerates both oligomerization and subsequent aromatization, effectively circumventing both the sluggish initial C─C coupling of methanol‐mediated pathways and the high‐barrier direct protonation step in olefins‐mediated pathways. Techno‐economic analysis (TEA) further demonstrates the superior industrial viability of this novel process. This work establishes a new paradigm for designing efficient catalytic systems and engineering process toward sustainable CO 2 valorization.

Article Details

Volume / Issue Vol. 1, Issue 1
Published July 03, 2026
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (17)

X

Xinze Bi

College of New Energy, State Key Laboratory of Heavy Oil Processing

Q

Qi Li

N

Na Zhao

Z

Zhaorui Zhang

School of Environmental Science and Technology

Y

Yang Wang

K

Kaixuan Huo

College of New Energy China University of Petroleum (East China) Qingdao China

X

Xudong Yu

S

Song Li

Z

Zhongxu Bian

College of New Energy China University of Petroleum (East China) Qingdao China

Y

Yuanyuan Han

X

Xiaojie Liu

Y

Yifan Yan

W

Wenhang Wang

Department of Applied Chemistry, School of Engineering, University of Toyama, Gofuku 3190, Toyama 930-8555, Japan

W

Wengang Xu

College of New Energy, State Key Laboratory of Heavy Oil Processing

Q

Qiang Liu

N

Noritatsu Tsubaki

Department of Applied Chemistry, Graduate School of Engineering, University of Toyama, 3190 Gofuku, Toyama 930-8555, Japan

M

Mingbo Wu

College of New Energy, State Key Laboratory of Heavy Oil Processing