“…Urakawa et al reported the continuous DMC synthesis from CO 2 and methanol over CeO 2 + 2-cyanopyridine system, which exhibited outstanding methanol conversion of >95% and >99% selectivity toward dimethyl carbonate with much shorter reaction time in a continuous flow fixed-bed reactor than in batch operation . Later, the continuous synthesis of DMC from CO 2 and methanol with excellent yields in a fixed bed has been widely adopted via optimizing the catalyst composition and morphology, the catalyst amount, CO 2 pressure, reaction temperature, and residence time. ,, Concerning catalyst composition and morphology, it has been reported that the adsorption and activation of CO 2 for the synthesis of DMC is significantly affected by the surface oxygen vacancy sites and acid–base properties of the catalysts. , As a result, several strategies have been adopted to increase the number of surface oxygen vacancy sites and acid–base sites of CeO 2 -based catalysts for the synthesis of DMC via tuning the morphology, structure and composition, such as Ti x Ce 1– x O 2 nanocomposites, , surface modification of CeO 2 by rare earth metal, Zr-doped CeO 2 nanorods, MgO-CeO 2 , CeO 2 nanomaterials with differently exposed planes . For example, Urakawa et al reported that the addition of rare earth metals (La, Gd, and Pr) can effectively enhance the catalyst stability by improving the methoxy species adsorption strength while preventing the adsorption of 2-picolinamide-like species, as shown in Figure c .…”