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• W3032912160 abstract "Dry reforming of methane is conducted in a catalyst packed-bed dielectric barrier discharge (DBD) reactor aiming to improve the reaction efficiency. The MgO- and CeO2-promoted Ni/γ-Al2O3 catalyst is tested to carry out the reaction. An interesting observation is that Ni/MgO_Al2O3 integration provides ∼35 and 13% conversion of CH4 and CO2, respectively. The highest syngas ratio of 0.94 is obtained with Ni/MgO_Al2O3, whereas the ratio is only 0.57 with Ni/CeO2_Al2O3 and 0.64 with bare DBD. In addition, Ni/CeO2_Al2O3 offers the highest selectivity (68%) of CO due to the oxygen buffer property of CeO2. Finally, the optimal acid/base property is highly desirable for the dry reforming reaction." @default.
• W3032912160 created "2020-06-12" @default.
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• W3032912160 date "2020-06-04" @default.
• W3032912160 modified "2023-10-12" @default.
• W3032912160 title "Promising Utilization of CO₂ for Syngas Production over Mg²⁺- and Ce²⁺-Promoted Ni/γ-Al₂O₃ Assisted by Nonthermal Plasma" @default.
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• W3032912160 doi "https://doi.org/10.1021/acsomega.0c01442" @default.
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