Selective catalytic reduction (SCR) of NO
x
with NH3 is the most efficient technology
for NO
x
emissions control, but the activity
of catalysts
decreases exponentially with the decrease in reaction temperature,
hindering the application of the technology in low-temperature SCR
to treat industrial stack gases. Here, we present an industrially
practicable technology to significantly enhance the SCR activity at
low temperatures (<250 °C). By introducing an appropriate
amount of O3 into the simulated stack gas, we find that
O3 can stoichiometrically oxidize NO to generate NO2, which enables NO reduction to follow the fast SCR mechanism
so as to accelerate SCR at low temperatures, and, in particular, an
increase in SCR rate by more than four times is observed over atom-pair
V1–W1 active sites supported on TiO2(001) at 200 °C. Using operando SCR tests and in situ
diffuse reflectance infrared Fourier transform spectra, we reveal
that the introduction of O3 allows SCR to proceed along
a NH4NO3-mediated Langmuir–Hinshelwood
model, in which the adsorbed nitrate species speed up the re-oxidation
of the catalytic sites that is the rate-limiting step of SCR, thus
leading to the enhancement of activity at low temperatures. This technology
could be applicable in the real stack gas conditions because O3 exclusively oxidizes NO even in the co-presence of SO2 and H2O, which provides a general strategy to
improve low-temperature SCR efficacy from another perspective beyond
designing catalysts.