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- W2354003764 abstract "The conversion of benzene hydrocarbons, COx selectivity and O3 formation by the non-thermal plasma and the combinations of non-thermal plasma and Pt/Al2O3 or Mn/Al2O3 catalyst were investigated in a link tooth wheel-cylinder plasma reactor. The results showed that the order of benzene hydrocarbons conversion was p-xylenetoluenebenzene under the same reaction conditions. Placing a Pt/Al2O3 or Mn/Al2O3 catalyst bed behind discharge region which induced non-thermal plasma promoted the conversion of benzene hydrocarbons while the applied voltage, corresponding to the same conversion rate, decreased for 1~2 kV. The combination of non-thermal plasma and Pt/Al2O3 or Mn/Al2O3 catalyst also resulted in a higher COx yield and a less O3 emission, the highest COx yield increasing from 80% to 86% (Pt/Al2O3) and 100% (Mn/Al2O3). Similarly, the largest O3 emission decreased from 707 mg·m-3 to 339 mg·m-3 (Pt/Al2O3) and 39 mg·m-3 (Mn/Al2O3). The combination of non-thermal and Mn/Al2O3 catalyst can be expected to become a practical method dealing with low concentration VOCs after further optimizing plasma reactor configuration, catalyst compositions and the combination of non-thermal plasma and catalyst." @default.
- W2354003764 created "2016-06-24" @default.
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- W2354003764 date "2008-01-01" @default.
- W2354003764 modified "2023-09-25" @default.
- W2354003764 title "Combination of non-thermal plasma and heterogeneous catalysis for removal of low concentration benzene hydrocarbons in air" @default.
- W2354003764 hasPublicationYear "2008" @default.
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