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Enhanced catalytic performance of Zr modified CuO/ZnO/Al2O3 catalyst for methanol and DME synthesis via CO2 hydrogenation

机译:通过CO 2氢化增强ZR改性CuO / ZnO / Al2O3催化剂的Zr改性CuO / ZnO / Al2O3催化剂的催化性能

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Zirconium (Zr) modified CuO/ZnO/Al2O3 (CZA) catalysts with different aluminum (Al) and Zr contents were synthesized by the co-precipitation method. The synthesized CuO/ZnO/ZrO2/Al2O3(CZZA) catalysts were comprehensively characterized and studied for methanol synthesis via CO2 hydrogenation. The CZZA catalyst showed the highest methanol yield of 12.4 % at 220 degrees C and 2.76 MPa with an optimized catalyst composition of Cu/Zn/Zr/Al (atomic ratio) at 4:2:1:0.5. The CZZA catalyst showed better activity than that of the CZA catalyst and a superior stability for methanol synthesis. There was no decrease in the BET surface area and very lithe coke formation for the spent CZZA catalyst, after 300 h of methanol synthesis. Bifunctional catalysts, composed of CZZA and HZSM-5, were investigated for dimethyl ether (DME) synthesis directly from CO2 hydrogenation, and a maximum DME yield of 18.3 % was obtained at a reaction temperature of 240 degrees C and a pressure of 2.76 MPa. The stability of the bifunctional CZZA and HZSM-5 catalyst during the DME synthesis also significantly improved, as compared to that of the CZA and HZSM-5. A significant decrease in the BET surface area and an increase in coking on the spent CZZA catalyst were observed after 100 h of DME synthesis, indicating a detrimental effect on CZZA stability when a HZSM-5 catalyst was present. The changes in structural properties (e.g., BET surface area and crystallinity) and coking for HZSM-5 could be responsible for the deactivation of the bifunctional catalyst.
机译:通过共沉淀法合成具有不同铝(Al)和Zr含量的锆(Zr)改性CuO / ZnO / Al2O3(CZA)催化剂。通过CO 2氢化全面地表征合成的CuO / ZnO / ZrO 2 / Al 2 O 3(COZA)催化剂并研究甲醇合成。 CZZA催化剂在220℃和2.76MPa下显示出最高甲醇产率12.4%,具有4:2:1:0.5的Cu / Zn / Zr / Al(原子比)的优化催化剂组合物。 CZZA催化剂显示出比CZA催化剂的活性更好,以及甲醇合成的优异稳定性。在甲醇合成300小时后,BET表面积和废CZEA催化剂的光谱焦炭形成没有减少。研究了由COZA和HZSM-5组成的双官能催化剂,用于直接来自CO 2氢化的二甲醚(DME)合成,在240℃的反应温度和2.76MPa的压力下获得最大DME产率为18.3%。与CZA和HZSM-5相比,双官能CZZA和HZSM-5催化剂在DME合成期间的稳定性也显着改善。在DME合成100小时后观察到BET表面积的显着降低和在花废CZZA催化剂上的焦化的增加,表明当存在HZSM-5催化剂时对COZA稳定性的不利影响。 HZSM-5的结构性质(例如,BET表面积和结晶度)的变化和焦化可负责双官能催化剂的失活。

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