Selective Catalytic Reduction
of NO<sub><i>x</i></sub> of Ship Diesel Engine Exhaust Gas
with C<sub>3</sub>H<sub>6</sub> over Cu/Y Zeolite
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Abstract
Various
solid Cu-containing catalysts were prepared. Their performance
in the selective catalytic reduction of NO<sub><i>x</i></sub> using propene as reducing agent from 150 to 450 °C in an O<sub>2</sub>-rich model exhaust gas in the presence of water vapor was
investigated. This research aimed at the development of a catalytic
NO<sub><i>x</i></sub> to N<sub>2</sub> (DeNO<sub><i>x</i></sub>) step to be part of a ship diesel exhaust abatement
system in combination with other techniques, such as nonthermal plasma.
Among the catalysts tested, Cu on zeolite Y with an optimized load
of 16 wt % (denoted as 16Cu/Y) displayed excellent DeNO<sub><i>x</i></sub> activity with highest selectivity toward N<sub>2</sub> at 290 °C. The influence of other variables, such as Cu load,
calcination temperature, feed composition, and GHSV on the performance
of 16Cu/Y was studied, as well. The highest N<sub>2</sub> yield of
98% was achieved using 2000 ppm of propene in the gas feed. The presence
of O<sub>2</sub> proved to be a crucial factor for promoting the selective
reduction of NO<sub><i>x</i></sub> with C<sub>3</sub>H<sub>6</sub> over this catalyst. On the other hand, the presence of water
in the feed decreased NO<sub><i>x</i></sub> to N<sub>2</sub> conversion. However, the catalyst showed excellent stability over
120 h, even at high water concentration, and also after repeated heating
from ambient temperature to 450 °C, and it was reusable after
downtimes without remarkable loss in activity. The nature of the Cu
species was studied by XPS, XRD, and TPR experiments