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    Effect of Support and Promoter on Activity and Selectivity of Gold Nanoparticles in Propanol Synthesis from CO<sub>2</sub>, C<sub>2</sub>H<sub>4</sub>, and H<sub>2</sub>

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    Direct propanol synthesis from CO<sub>2</sub>, H<sub>2</sub>, and C<sub>2</sub>H<sub>4</sub> was investigated over TiO<sub>2</sub>- and SiO<sub>2</sub>-based catalysts doped with K and possessing Au nanoparticles (NPs). The catalysts were characterized by scanning transmission electron microscopy and temperature-programmed reduction of adsorbed CO<sub>2</sub>. Mechanistic aspects of CO<sub>2</sub> and C<sub>2</sub>H<sub>4</sub> interaction with the catalysts were elucidated by means of temporal analysis of products with microsecond time resolution. CO<sub>2</sub>, which is activated on the support, is reduced to CO by hydrogen surface species formed from gas-phase H<sub>2</sub> on Au NPs. C<sub>2</sub>H<sub>4</sub> adsorption also occurs on these sites. In comparison with TiO<sub>2</sub>-based catalysts, the promoter in the K–Au/SiO<sub>2</sub> catalysts was found to increase CO<sub>2</sub> conversion and propanol production, whereas Au-related turnover frequency of C<sub>2</sub>H<sub>4</sub> hydrogenation to C<sub>2</sub>H<sub>6</sub> decreased with rising K loading. The latter reason was linked to the effect of the support on the ability of Au NPs for activation of C<sub>2</sub>H<sub>4</sub> and H<sub>2</sub>. The positive effect of K on CO<sub>2</sub> conversion was explained by partial dissolution of potassium in silica with formation of surface potassium silicate layer thus inhibiting formation of potassium carbonate, which binds CO<sub>2</sub> stronger and therefore hinders its reduction to CO
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