Abstract
AbstractIn this work, we report the decomposition of gas-phase benzene using plasma-driven catalyst (PDC) system of a single-stage configuration. The decomposition of benzene was affected by the reactor diameter of the surface discharge type PDC reactor. The smaller the reactor diameter, the higher the decomposition efficiency. Long-term test over 150 h demonstrated the stable operation of the PDC reactor without any deterioration of catalytic activity. The PDC reactor with Ag/TiO
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