Lijun Zhang, Teng Li, Wenjie Xiang, Zhiwei Ye, Luyao Wu, Wei Xia, Hao Huang, Zhihao Liu, Xiuyun Jiang, Guangbo Liu, Zhiliang Jin, Weizhe Gao, Hongliang Li, Jie Zeng, Noritatsu Tsubaki
{"title":"Direct Synthesis of <i>para</i>-Xylene from CO<sub>2</sub> Hydrogenation with a Record-High Space-Time Yield.","authors":"Lijun Zhang, Teng Li, Wenjie Xiang, Zhiwei Ye, Luyao Wu, Wei Xia, Hao Huang, Zhihao Liu, Xiuyun Jiang, Guangbo Liu, Zhiliang Jin, Weizhe Gao, Hongliang Li, Jie Zeng, Noritatsu Tsubaki","doi":"10.1021/jacs.5c03380","DOIUrl":null,"url":null,"abstract":"<p><p>The direct synthesis of <i>para</i>-xylene (<i>p</i>-X) from CO<sub>2</sub> hydrogenation with high space-time yield (STY) remains a significant challenge due to two primary limitations: the Anderson-Schulz-Flory distribution, which restricts the C<sub>8</sub> selectivity to ∼6.8 C%, and the thermodynamic equilibrium, which confines the <i>p</i>-X content among xylene isomers to 15-25%. Herein, we report a composite catalyst, K-FeMn/Hollow ZSM-5, that enables the efficient hydrogenation of CO<sub>2</sub> to <i>p</i>-X by integrating two synergistic catalytic functions. The K-FeMn component facilitates the reverse water-gas shift reaction and Fischer-Tropsch synthesis to olefin processes, generating light olefin intermediates. These intermediates are subsequently transformed to <i>p</i>-X within the hollow ZSM-5 zeolite through oligomerization, cyclization, and aromatization. The hollow ZSM-5 features a suitable pore size to facilitate <i>p</i>-X diffusion only, while its passivated external acid sites effectively suppress isomerization and alkylation of <i>p</i>-X outside the zeolite. As a result, the K-FeMn/Hollow ZSM-5 catalyst achieves a <i>p</i>-X STY of 41.7 g kg<sub>cat</sub><sup>-1</sup> h<sup>-1</sup> at a CO<sub>2</sub> conversion of 46.1%, surpassing all previously reported values. This work demonstrates a novel approach to overcome the local thermodynamic equilibria by specific catalyst design and the spatial separation of processes toward CO<sub>2</sub> hydrogenation into <i>p</i>-X.</p>","PeriodicalId":49,"journal":{"name":"Journal of the American Chemical Society","volume":" ","pages":""},"PeriodicalIF":14.4000,"publicationDate":"2025-06-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of the American Chemical Society","FirstCategoryId":"92","ListUrlMain":"https://doi.org/10.1021/jacs.5c03380","RegionNum":1,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
Abstract
The direct synthesis of para-xylene (p-X) from CO2 hydrogenation with high space-time yield (STY) remains a significant challenge due to two primary limitations: the Anderson-Schulz-Flory distribution, which restricts the C8 selectivity to ∼6.8 C%, and the thermodynamic equilibrium, which confines the p-X content among xylene isomers to 15-25%. Herein, we report a composite catalyst, K-FeMn/Hollow ZSM-5, that enables the efficient hydrogenation of CO2 to p-X by integrating two synergistic catalytic functions. The K-FeMn component facilitates the reverse water-gas shift reaction and Fischer-Tropsch synthesis to olefin processes, generating light olefin intermediates. These intermediates are subsequently transformed to p-X within the hollow ZSM-5 zeolite through oligomerization, cyclization, and aromatization. The hollow ZSM-5 features a suitable pore size to facilitate p-X diffusion only, while its passivated external acid sites effectively suppress isomerization and alkylation of p-X outside the zeolite. As a result, the K-FeMn/Hollow ZSM-5 catalyst achieves a p-X STY of 41.7 g kgcat-1 h-1 at a CO2 conversion of 46.1%, surpassing all previously reported values. This work demonstrates a novel approach to overcome the local thermodynamic equilibria by specific catalyst design and the spatial separation of processes toward CO2 hydrogenation into p-X.
期刊介绍:
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