CO2 hydrogenation
to methanol is a promising process
for CO2 conversion and utilization. Despite a well-developed
route for CO hydrogenation to methanol, the use of CO2 as
a feedstock for methanol synthesis remains underexplored, and one
of its major challenges is high reaction pressure (usually 30–300
atm). In this work, atmospheric pressure and room temperature (∼30
°C) synthesis of methanol from CO2 and H2 has been successfully achieved using a dielectric barrier discharge
(DBD) with and without a catalyst. The methanol production was strongly
dependent on the plasma reactor setup; the DBD reactor with a special
water-electrode design showed the highest reaction performance in
terms of the conversion of CO2 and methanol yield. The
combination of the plasma with Cu/γ-Al2O3 or Pt/γ-Al2O3 catalyst significantly
enhanced the CO2 conversion and methanol yield compared
to the plasma hydrogenation of CO2 without a catalyst.
The maximum methanol yield of 11.3% and methanol selectivity of 53.7%
were achieved over the Cu/γ-Al2O3 catalyst
with a CO2 conversion of 21.2% in the plasma process, while
no reaction occurred at ambient conditions without using plasma. The
possible reaction mechanisms in the plasma CO2 hydrogenation
to CH3OH with and without a catalyst were proposed by combined
means of electrical and optical diagnostics, product analysis, catalyst
characterization, and plasma kinetic modeling. These results have
successfully demonstrated that this unique plasma process offers a
promising solution for lowering the kinetic barrier of catalytic CO2 hydrogenation to methanol instead of using traditional approaches
(e.g., high reaction temperature and high-pressure process), and has
great potential to deliver a step-change in future CO2 conversion
and utilization.