Dimethyl
carbonate (DMC) and propylene glycol (PG) synthesis through
a methanol and propylene carbonate (PC) reaction, also referred to
as a transesterification reaction, is a new and green alternative
to other routes, such as phosgene methanolysis, urea methanolysis,
etc. In this paper, the titanium–praseodymium-based catalyst
prepared via the co-precipitation method has been used to improve
the yield and selectivity of DMC production. Different combinations
of catalysts were synthesized, referred to as Ti0.99Pr0.01, Ti0.97Pr0.03, Ti0.96Pr0.04, and Ti0.95Pr0.05, according
to the molar ratio of Ti with respect to Pr. The catalysts have been
studied and analyzed through various characterization techniques,
such as X-ray diffraction (XRD), field emission scanning electron
microscopy (FESEM), Fourier transform infrared spectroscopy (FTIR),
and X-ray photoelectron spectroscopy (XPS). The Brunauer–Emmett–Teller
(BET) surface area and pore volume diameter have been studied through
N2 adsorption–desorption using BET and Barrett–Joyner–Halenda
(BJH) models, respectively. The basicity was determined through the
carbon dioxide temperature-programmed desorption (CO2-TPD)
for understanding the reaction mechanism. The reaction was carried
out in the batch reactor, keeping the temperature range of 160–180
°C and the molar ratio of methanol/PC in the range of 3–10.
The study has also been made on oxygen vacancy concentrations in the
mixed oxide catalysts as a result of the mixing of Pr with Ti, thereby
affecting the yield and selectivity of DMC. The maximum yield of DMC
was obtained with the Ti0.96Pr0.04 catalyst
at a temperature of 170 °C which resulted in the PC conversion
of 81.7%, turnover frequency (TOF) of 0.120 h–1,
and selectivity of 71.6% for DMC.