以直接水热合成和低硅沸石高温水蒸气脱铝两种方法制备了不同Si/Al摩尔比的HZSM-5载体,考察了Ga2O3/HZSM-5催化剂上丙烷脱氢制丙烯的反应性能.结合XRD,N2气吸附,27Al MAS NMR和NH3-TPD等表征方法,讨论了催化剂酸性质和孔性质与性能的关...以直接水热合成和低硅沸石高温水蒸气脱铝两种方法制备了不同Si/Al摩尔比的HZSM-5载体,考察了Ga2O3/HZSM-5催化剂上丙烷脱氢制丙烯的反应性能.结合XRD,N2气吸附,27Al MAS NMR和NH3-TPD等表征方法,讨论了催化剂酸性质和孔性质与性能的关系.实验结果表明,减少催化剂表面的中强酸量可以显著提高反应的稳定性和丙烯的选择性;水蒸气脱铝所增加的介孔有同样的效果,这可能是由于介孔的存在有利于丙烯的脱附和扩散而抑制了寡聚、环化等副反应的发生,减少了表面积炭的可能性.展开更多
A series of composite catalysts were prepared by the wet mixing method, and the mass ratio of CuO-ZnO-Al2O3-ZrO2 component to HZSM-5 zeolite （molar ratio of SiO2 to Al2O3 being 25） was 2：1. The CuO-ZnO-Al2O3-ZrO2 ...A series of composite catalysts were prepared by the wet mixing method, and the mass ratio of CuO-ZnO-Al2O3-ZrO2 component to HZSM-5 zeolite （molar ratio of SiO2 to Al2O3 being 25） was 2：1. The CuO-ZnO-Al2O3-ZrO2 （CuO/ZnO/Al2O3=3/6/1 by weight） component was prepared by a modified ＇two-step＇ co-precipitation method. The effects of ZrO2 on the performance of CuO-ZnO-Al2O3/HZSMo5 catalyst for dimethyl ether synthesis from CO2 hydrogenation were investigated. It was found that ZrO2 improved the properties of CuO-ZnO-Al2O3/HZSM-5 as a structural promoter.展开更多
The optimum Mo/[H^+] ratio per unit cell of the active precursors in Mo/HZSM-5 catalysts for methane dehydro-aromatization, measured by1H MAS NMR, was found to be about 1 when adjusting the acid sites by altering eith...The optimum Mo/[H^+] ratio per unit cell of the active precursors in Mo/HZSM-5 catalysts for methane dehydro-aromatization, measured by1H MAS NMR, was found to be about 1 when adjusting the acid sites by altering either the SiO2/Al2O3 ratios or the Mo loading. This implies that a concerted interaction between the Mo species and the Bronsted acid sites probably features the bifunctionality of the Mo/HZSM-5 catalyst. On the other hand, it was found that the driving force for Mo species to move into the HSZM-5 zeolite channels and the interaction between the Mo species and the Bronsted acid sites are closely and proportionably related with the amount of Bronsted acid sites per unit cell.展开更多
文摘以直接水热合成和低硅沸石高温水蒸气脱铝两种方法制备了不同Si/Al摩尔比的HZSM-5载体,考察了Ga2O3/HZSM-5催化剂上丙烷脱氢制丙烯的反应性能.结合XRD,N2气吸附,27Al MAS NMR和NH3-TPD等表征方法,讨论了催化剂酸性质和孔性质与性能的关系.实验结果表明,减少催化剂表面的中强酸量可以显著提高反应的稳定性和丙烯的选择性;水蒸气脱铝所增加的介孔有同样的效果,这可能是由于介孔的存在有利于丙烯的脱附和扩散而抑制了寡聚、环化等副反应的发生,减少了表面积炭的可能性.
文摘A series of composite catalysts were prepared by the wet mixing method, and the mass ratio of CuO-ZnO-Al2O3-ZrO2 component to HZSM-5 zeolite （molar ratio of SiO2 to Al2O3 being 25） was 2：1. The CuO-ZnO-Al2O3-ZrO2 （CuO/ZnO/Al2O3=3/6/1 by weight） component was prepared by a modified ＇two-step＇ co-precipitation method. The effects of ZrO2 on the performance of CuO-ZnO-Al2O3/HZSMo5 catalyst for dimethyl ether synthesis from CO2 hydrogenation were investigated. It was found that ZrO2 improved the properties of CuO-ZnO-Al2O3/HZSM-5 as a structural promoter.
文摘The optimum Mo/[H^+] ratio per unit cell of the active precursors in Mo/HZSM-5 catalysts for methane dehydro-aromatization, measured by1H MAS NMR, was found to be about 1 when adjusting the acid sites by altering either the SiO2/Al2O3 ratios or the Mo loading. This implies that a concerted interaction between the Mo species and the Bronsted acid sites probably features the bifunctionality of the Mo/HZSM-5 catalyst. On the other hand, it was found that the driving force for Mo species to move into the HSZM-5 zeolite channels and the interaction between the Mo species and the Bronsted acid sites are closely and proportionably related with the amount of Bronsted acid sites per unit cell.
