Modification of the classical multipin to plate plasmachemical reactor
for pollutant decomposition is proposed in this paper. In this modified
reactor a mixture of air and pollutant flows through the needles,
contrary to the classical reactor where a mixture of air and pollutant
flows around the pins or through the channel plus through the hollow
needles.
We give the results of comparison of toluene decomposition efficiency for (a) a
reactor with the main stream of a mixture through the channel around the
needles and a small flow rate through the needles and (b) a modified reactor.
It was found that for similar flow rates and similar energy deposition,
the decomposition efficiency of toluene was increased more than six times in
the modified reactor.
This new modified reactor was also experimentally tested for the decomposition
of volatile hydrocarbons from gasoline distillation range. An average
efficiency of VOC decomposition of about 25% was reached. However,
significant differences in the decomposition of various hydrocarbon types were
observed. The best results were obtained for the decomposition of olefins
(reaching 90%) and methyl-tert-butyl ether (about 50%). Moreover, the
number of carbon atoms in the molecule affects the quality of VOC
decomposition.