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作 者:Lingzhen Zeng Yongfang Sun Tingting Wang Zeyan Cen Maolin Wang Oriol Angurell Meng Wang Ding Ma
机构地区:[1]Beijing National Laboratory for Molecular Sciences,New Cornerstone Science Laboratory,College of Chemistry and Molecular Engineering,Peking University,Beijing 100871,China [2]Leitat managing technologies,Parc Cientific de Barcelona,Edifici Clúster Ⅱ,Planta 4,Carrer Baldiri Reixac,4-8.08028,Barcelona,Spain
出 处:《Science China Chemistry》2025年第2期513-519,共7页中国科学(化学英文版)
基 金:supported by National Key R&D Program of China(2022YFE0114900);New Cornerstone Science Foundation,it has also received funding from the European Union’s Horizon 2020 research and innovation program under grant agreement No 101022202.D.M.acknowledges support from the Tencent Foundation through the XPLORER PRIZE.Zeng would like to express gratitude to the China Postdoctoral Science Foundation(2021M700209,2024T170015)。
摘 要:Methanol synthesis via CO_(2) hydrogenation stands as a pivotal avenue for CO_(2) conversion and fixation,garnering extensive investigation.Diverse reactor configurations and energy supplies,alongside a spectrum of catalyst formulations,have been developed to enhance reaction metrics including conversion,selectivity,productivity,and stability.Integrating state-of-the-art Cu-based catalysts from thermal catalysis into a photothermal reactor yielded notable results,achieving an overall CO_(2) conversion of 98%and methanol selectivity of 86%.Utilizing the liquid out/gas in concept(LOGIC)reactor,in which only the catalyst bed is irradiated to raise its temperature,facilitated the condensation of products(H_(2)O and CH3OH),due to their low vapor pressure.The lower concentration of products in vapor phases ensured the continuous progress of the reaction.The synergistic integration of reactor design and catalyst fabrication could capitalize on the strengths of both components and lead to enhanced performance in methanol synthesis.
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