期刊
CHEMPHYSCHEM
卷 18, 期 22, 页码 3253-3259出版社
WILEY-V C H VERLAG GMBH
DOI: 10.1002/cphc.201700752
关键词
non-thermal plasmas; carbon dioxide conversion; plasma treatment of catalysts; plasma chemistry; supported catalysts
资金
- EPSRC SUPERGEN Hydrogen & Fuel Cell (H2FC) Programme [EP/J016454/1]
- ECR Project [EACPR_PS5768]
- EPSRC CO2Chem Grand Challenge Network Seedcorn grant
Direct conversion of CO2 into CO and O-2 is performed in a packed-bed dielectric barrier discharge (DBD) non-thermal plasma reactor at low temperatures and atmospheric pressure. The maximum CO2 conversion of 22.6% is achieved when BaTiO3 pellets are fully packed into the discharge gap. The introduction of g-Al2O3 or 10 wt% Ni/g-Al2O3 catalyst into the BaTiO3 packed DBD reactor increases both CO2 conversion and energy efficiency of the plasma process. Packing g-Al2O3 or 10 wt% Ni/g-Al2O3 upstream of the BaTiO3 bed shows higher CO2 conversion and energy efficiency compared with that of mid-or downstream packing modes because the reverse reaction of CO2 conversion-the recombination of CO and O to form CO2-is more likely to occur in mid-and downstream modes. Compared with the g-Al2O3 support, the coupling of the DBD with the Ni catalyst shows a higher CO2 conversion, which can be attributed to the presence of Ni active species on the catalyst surface. The argon plasma treatment of the reacted Ni catalyst provides extra evidence to confirm the role of Ni active species in the conversion of CO2.
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