2021
DOI: 10.1016/j.jhazmat.2020.123877
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Regeneration of Hopcalite used for the adsorption plasma catalytic removal of toluene by non-thermal plasma

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Cited by 17 publications
(6 citation statements)
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“…The transient productions reach the first maximum (shoulder) value between 1 and 3 min of plasma exposure and the second maximum value between 7 and 9 min of plasma exposure and return to baseline beyond 20 min of plasma treatment. This type of behavior has been previously observed over Hopcalite whether it is by thermal desorption [24] or NTP exposure [23]. Most of the CO 2 produced in the first minutes of NTP exposure is released in the gas phase and some surface sites are thus liberated.…”
Section: Effect Of Toluene Exposure Time On Apc Process Performancessupporting
confidence: 71%
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“…The transient productions reach the first maximum (shoulder) value between 1 and 3 min of plasma exposure and the second maximum value between 7 and 9 min of plasma exposure and return to baseline beyond 20 min of plasma treatment. This type of behavior has been previously observed over Hopcalite whether it is by thermal desorption [24] or NTP exposure [23]. Most of the CO 2 produced in the first minutes of NTP exposure is released in the gas phase and some surface sites are thus liberated.…”
Section: Effect Of Toluene Exposure Time On Apc Process Performancessupporting
confidence: 71%
“…This explains the good catalytic activity and maintained CO 2 selectivity of several sequences performed on Hopcalite. In our previous work, Veerapandian et al [23] proposed a detailed mechanism of toluene abatement. It was suggested that the catalytic oxidation of toluene follows a Mars and Van Krevelen mechanism.…”
Section: Characterization Of Catalystmentioning
confidence: 99%
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“…The presence of the dielectric barrier limits the amount of energy and charge imparted to every microdischarge, resulting in the distribution of microdischarge over the entire electrode, which makes the DBD reactor suitable for applications such as O 3 generation and air cleaning [185] . In the DBD reactor, the catalyst is usually introduced as a packed bed in the form of pellets [186] , powder [187] , granules, or fibers. The presence of packing material in the discharge gap enhances the electric field near their contact points, increases the VOC residence time, and reduces the plasma volume, resulting in better VOC removal efficiency.…”
Section: In-plasma Catalysismentioning
confidence: 99%
“…Therefore, many studies focus on the hybrid technologies of NTP coupled with other technologies [33][34][35][36]. Among these hybrid systems, plasma catalysis technology shows its advantages among the treatments of typically VOCs for its high selectivity and removal rate because the gas-phase reaction and catalyst surface reaction induces a synergistic effect of plasma and catalysts [37][38][39][40][41]. In previous studies, the enhancing effect of various transition metal oxides for the treatment of VOCs by NTP has been confirmed.…”
Section: Introductionmentioning
confidence: 99%