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Promising Utilization of CO2 for Syngas Production over Mg2+- and Ce2+-Promoted Ni/?-Al2O3 Assisted by Nonthermal Plasma.


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/?-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.

SUBMITTER: Ray D 

PROVIDER: S-EPMC7301564 | biostudies-literature | 2020 Jun

REPOSITORIES: biostudies-literature

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Promising Utilization of CO<sub>2</sub> for Syngas Production over Mg<sup>2+</sup>- and Ce<sup>2+</sup>-Promoted Ni/γ-Al<sub>2</sub>O<sub>3</sub> Assisted by Nonthermal Plasma.

Ray Debjyoti D   Chawdhury Piu P   Subrahmanyam Challapalli C  

ACS omega 20200604 23


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 CeO<sub>2</sub>-promoted Ni/γ-Al<sub>2</sub>O<sub>3</sub> catalyst is tested to carry out the reaction. An interesting observation is that Ni/MgO_Al<sub>2</sub>O<sub>3</sub> integration provides ∼35 and 13% conversion of CH<sub>4</sub> and CO<sub>2</sub>, respectively. The highest syngas ratio of 0.94 is obtained with Ni/MgO_Al<sub>2</s  ...[more]

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