<p>A series of Zn<sub>x</sub>Ce<sub>1-x</sub>O<sub>2</sub> catalysts with different Zn/Ce molar ratios were prepared using the co-precipitation method and used for the synthesis of diethyl carbonate from carbon dioxide and ethanol. The catalysts were characterized by XRD, SEM, N<sub>2</sub> adsorption–desorption, XPS, Py-IR, NH<sub>3</sub>-TPD and CO<sub>2</sub>-TPD. Characterization results revealed that the optimal density of acid–base sites (with Lewis acids as the dominant species) was achieved at a Zn/Ce molar ratio of 0.1. The introduction of ZnO promotes the formation of Ce<sup>3</sup>⁺ and leads to a significant increase in the number of Lewis acid sites. ZnO doping induces lattice distortion in CeO<sub>2</sub> and generates abundant oxygen vacancies, which in turn promotes the reduction of Ce<sup>4+</sup> to Ce<sup>3+</sup> and thus optimizes the distribution of acid–base pairs. Ethanol and CO<sub>2</sub> first form an ethoxycarbonate intermediates at the acid–base sites of the catalyst, which then further reacts to produce DEC. Under conditions of 170&#xa0;°C, 4.5&#xa0;MPa, and 3&#xa0;h, the Zn<sub>0.1</sub>Ce<sub>0.9</sub>O<sub>2</sub> catalyst showed excellent catalytic activity. The yield of DEC was 4.32 mmol<sub>DEC</sub> g<sub>cat</sub><sup>−1</sup>, 32% higher than that of pure CeO<sub>2</sub>. The catalyst offers advantages such as simple preparation process, low cost, and no need for dehydrating agents, which provides support for its large-scale industrial application.</p>

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Enhanced CO2 conversion to diethyl carbonate over Zn-modified CeO2 bifunctional catalysts

  • Hefang Wang,
  • Jingwei Liu,
  • Hui Jiang,
  • Shijiao Hao,
  • Xiaofei Ma,
  • Weiqian Qi,
  • Muhammad Hashim Khan

摘要

A series of ZnxCe1-xO2 catalysts with different Zn/Ce molar ratios were prepared using the co-precipitation method and used for the synthesis of diethyl carbonate from carbon dioxide and ethanol. The catalysts were characterized by XRD, SEM, N2 adsorption–desorption, XPS, Py-IR, NH3-TPD and CO2-TPD. Characterization results revealed that the optimal density of acid–base sites (with Lewis acids as the dominant species) was achieved at a Zn/Ce molar ratio of 0.1. The introduction of ZnO promotes the formation of Ce3⁺ and leads to a significant increase in the number of Lewis acid sites. ZnO doping induces lattice distortion in CeO2 and generates abundant oxygen vacancies, which in turn promotes the reduction of Ce4+ to Ce3+ and thus optimizes the distribution of acid–base pairs. Ethanol and CO2 first form an ethoxycarbonate intermediates at the acid–base sites of the catalyst, which then further reacts to produce DEC. Under conditions of 170 °C, 4.5 MPa, and 3 h, the Zn0.1Ce0.9O2 catalyst showed excellent catalytic activity. The yield of DEC was 4.32 mmolDEC gcat−1, 32% higher than that of pure CeO2. The catalyst offers advantages such as simple preparation process, low cost, and no need for dehydrating agents, which provides support for its large-scale industrial application.