Tianjue Ke, Lei Wang, Xiaoming Guo, Jun Yu, Junyu Lang, Yun Hang Hu, Maohong Fan, Dongsen Mao
{"title":"Two types of catalytic sites of In2O3-Co3O4/CeO2 and their synergy for highly selective CO2 hydrogenation to methanol","authors":"Tianjue Ke, Lei Wang, Xiaoming Guo, Jun Yu, Junyu Lang, Yun Hang Hu, Maohong Fan, Dongsen Mao","doi":"10.1016/j.cej.2024.158236","DOIUrl":null,"url":null,"abstract":"The increasing concentration of greenhouse gases, specifically CO<sub>2</sub>, requires innovative mitigation approaches. Catalytic CO<sub>2</sub> reduction shows potential for producing high-value-added products from CO<sub>2</sub>, but the poor catalyst activity and product selectivity remain significant challenges. Oxygen vacancies and the interaction between the support and active components significantly influence the catalytic reactivity of a catalyst. Herein, we demonstrated a novel strategy to design highly efficient catalysts; namely, the reducibility of CeO<sub>2</sub> was exploited to tune the In<sub>2</sub>O<sub>3</sub>-Co<sub>3</sub>O<sub>4</sub> catalyst for CO<sub>2</sub> hydrogenation, creating synergetic double-type active sites that the O<sub>V1</sub> oxygen defects (generated by hydrogen reduction) on CeO<sub>2</sub> surface as active sites for CO<sub>2</sub> adsorption and the In-Co-Ce interfaces as active sites for hydrogenation of the adsorbed CO<sub>2</sub> to methanol via formate intermediates. Consequently, an excellent methanol selectivity of 74 % was achieved for CO<sub>2</sub> hydrogenation, leading to a very high methanol space–time yield of 276.8 mg∙h<sup>−1</sup>∙g<sub>In-Co</sub><sup>−1</sup> under mild reaction conditions (3 MPa, 280 °C, 2400 mL∙g<sub>cat</sub><sup>−1</sup>∙h<sup>−1</sup>), which is 4.8-fold higher than that without CeO<sub>2</sub>. This study highlights the highly synergistic effects of two types of catalytic sites of the CeO<sub>2</sub> supported In<sub>2</sub>O<sub>3</sub>-Co<sub>3</sub>O<sub>4</sub> catalyst and reveals a new pathway for designing new catalysts for more efficient CO<sub>2</sub> hydrogenation to methanol (CHTM)","PeriodicalId":270,"journal":{"name":"Chemical Engineering Journal","volume":"37 1","pages":""},"PeriodicalIF":13.2000,"publicationDate":"2024-12-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Journal","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1016/j.cej.2024.158236","RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
The increasing concentration of greenhouse gases, specifically CO2, requires innovative mitigation approaches. Catalytic CO2 reduction shows potential for producing high-value-added products from CO2, but the poor catalyst activity and product selectivity remain significant challenges. Oxygen vacancies and the interaction between the support and active components significantly influence the catalytic reactivity of a catalyst. Herein, we demonstrated a novel strategy to design highly efficient catalysts; namely, the reducibility of CeO2 was exploited to tune the In2O3-Co3O4 catalyst for CO2 hydrogenation, creating synergetic double-type active sites that the OV1 oxygen defects (generated by hydrogen reduction) on CeO2 surface as active sites for CO2 adsorption and the In-Co-Ce interfaces as active sites for hydrogenation of the adsorbed CO2 to methanol via formate intermediates. Consequently, an excellent methanol selectivity of 74 % was achieved for CO2 hydrogenation, leading to a very high methanol space–time yield of 276.8 mg∙h−1∙gIn-Co−1 under mild reaction conditions (3 MPa, 280 °C, 2400 mL∙gcat−1∙h−1), which is 4.8-fold higher than that without CeO2. This study highlights the highly synergistic effects of two types of catalytic sites of the CeO2 supported In2O3-Co3O4 catalyst and reveals a new pathway for designing new catalysts for more efficient CO2 hydrogenation to methanol (CHTM)
期刊介绍:
The Chemical Engineering Journal is an international research journal that invites contributions of original and novel fundamental research. It aims to provide an international platform for presenting original fundamental research, interpretative reviews, and discussions on new developments in chemical engineering. The journal welcomes papers that describe novel theory and its practical application, as well as those that demonstrate the transfer of techniques from other disciplines. It also welcomes reports on carefully conducted experimental work that is soundly interpreted. The main focus of the journal is on original and rigorous research results that have broad significance. The Catalysis section within the Chemical Engineering Journal focuses specifically on Experimental and Theoretical studies in the fields of heterogeneous catalysis, molecular catalysis, and biocatalysis. These studies have industrial impact on various sectors such as chemicals, energy, materials, foods, healthcare, and environmental protection.