Synergistically catalytic hydrogenation of <scp> CO <sub>2</sub> </scp> and <scp>CO</scp> to methanol over <scp> Ga <sub>2</sub> O <sub>3</sub> </scp> promoted Cu/ <scp>ZnO</scp> / <scp> Al <sub>2</sub> O <sub>3</sub> </scp>

Abstract Efficient conversion of CO 2 and CO is pivotal for CO 2 hydrogenation to methanol given the synthesis loop recycle generally employed in practice. However, competitive adsorption of CO and CO 2 at active sites reduces methanol production. In this study, multi‐functional active sites were constructed over Ga 2 O 3 ‐modified Cu/ZnO/Al 2 O 3 (CuZnAlGa) for synergistic hydrogenation of CO 2 and CO to methanol. Incorporating the Ga 2 O 3 promoter effectively dispersed Cu particles, formulated extra Cu‐Ga sites active for CO 2 adsorption and Ga sites for H 2 dissociation (Ga‐H), enhancing H 2 and CO 2 activation as well as promoting non‐competitive CO 2 /CO adsorption. Under 240°C, 5 MPa, and 6000 mL g cat −1 h −1 , the CuZnAlGa catalyst achieved a methanol space–time yield of 517 g kg cat −1 h −1 with excellent stability, outperforming the commercial methanol synthesis catalysts. The formate pathway, involving formate and methoxy as critical intermediates, is the predominant route for methanol formation. The Ga 2 O 3 promoter accelerates formate formation and further hydrogenation to methoxy.

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Publication Details

Journal
AIChE Journal
Published
2025-11-09
DOI
https://doi.org/10.1002/aic.70140
Primary Topic
Catalysts for Methane Reforming
Type
article
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article

Synergistically catalytic hydrogenation of CO 2 and CO to methanol over Ga 2 O 3 promoted Cu/ ZnO / Al 2 O 3

Jiyi Chen, Shixiong Tang, Wenyan Jia, Maoshuai Li et al.
AIChE Journal
Catalysts for Methane Reforming
article

Synergistically catalytic hydrogenation of CO 2 and CO to methanol over Ga 2 O 3 promoted Cu/ ZnO / Al 2 O 3

Jiyi Chen, Shixiong Tang, Wenyan Jia, Maoshuai Li, Zhenmei Zhang, Mingcan Chen, Ziwen Hao, Yue Wang, Yurou Bai, Xinbin Ma, Shengyu Wang, Pengju Gao, Xiaoyu Han, Zhen Yu
article en

Abstract

Abstract Efficient conversion of CO 2 and CO is pivotal for CO 2 hydrogenation to methanol given the synthesis loop recycle generally employed in practice. However, competitive adsorption of CO and CO 2 at active sites reduces methanol production. In this study, multi‐functional active sites were constructed over Ga 2 O 3 ‐modified Cu/ZnO/Al 2 O 3 (CuZnAlGa) for synergistic hydrogenation of CO 2 and CO to methanol. Incorporating the Ga 2 O 3 promoter effectively dispersed Cu particles, formulated extra Cu‐Ga sites active for CO 2 adsorption and Ga sites for H 2 dissociation (Ga‐H), enhancing H 2 and CO 2 activation as well as promoting non‐competitive CO 2 /CO adsorption. Under 240°C, 5 MPa, and 6000 mL g cat −1 h −1 , the CuZnAlGa catalyst achieved a methanol space–time yield of 517 g kg cat −1 h −1 with excellent stability, outperforming the commercial methanol synthesis catalysts. The formate pathway, involving formate and methoxy as critical intermediates, is the predominant route for methanol formation. The Ga 2 O 3 promoter accelerates formate formation and further hydrogenation to methoxy.

AIChE JournalVol. 72(2)
Tianjin University (CN), National University of Singapore (SG), Collaborative Innovation Center of Chemical Science and Engineering Tianjin (CN), Xinjiang University (CN)
Openalex Percentile: Top 79%
Catalysts for Methane Reforming
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