采用柠檬酸溶胶 凝胶法制备的Ce Zr La O固溶体为载体,制备CuO Ce Zr La O催化剂,用XRD,Raman,TPR等实验技术对Ce Zr La O固溶体及CuO Ce Zr La O的物相、Redox性能进行了表征。实验结果表明,Ce0.7Zr0 3-yLayO固溶体的还原性能与La含量...采用柠檬酸溶胶 凝胶法制备的Ce Zr La O固溶体为载体,制备CuO Ce Zr La O催化剂,用XRD,Raman,TPR等实验技术对Ce Zr La O固溶体及CuO Ce Zr La O的物相、Redox性能进行了表征。实验结果表明,Ce0.7Zr0 3-yLayO固溶体的还原性能与La含量有关,适量的La能促进固溶体的氧化还原。CuO的负载量为6%时,CuO Ce0.7Zr0.15La0.15O的活性最高,高分散且与载体相互作用的CuO是CO氧化活性相。展开更多
In accordance with the cerium-lanthanum ratio of fluorocerium ores in the mineralogy of the Baiyun Ebo process, the (Ce,La)CO<sub>3</sub>F grains were synthesised by hydrothermal method using pure material...In accordance with the cerium-lanthanum ratio of fluorocerium ores in the mineralogy of the Baiyun Ebo process, the (Ce,La)CO<sub>3</sub>F grains were synthesised by hydrothermal method using pure material to simulate bastnaesite minerals, and used as NH<sub>3</sub>-SCR denitrification catalysts. The activity results showed that the synthetic (Ce,La)CO<sub>3</sub>F was roasted at 500<span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">, and the NOx conversion was 27% at 200</span></span></span><span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">. The NH<sub>3</sub></span></span></span><span><span><span style="font-family:;" "="">-</span></span></span><span><span><span style="font-family:;" "="">SCR catalytic activity of the synthesised (Ce,La)CO<sub>3</sub>F was improved by loaded transition metal Mn. The best catalyst was found to be produced by impregnating (Ce,La)CO<sub>3</sub>F with 1 mol/L manganese nitrate solution, with a NOx conversion of 80% at 250</span></span></span><span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">. The loading of Mn resulted in the appearance of numerous well-dispersed MnOx species on the catalyst surface, the dispersion of Ce<sub>7</sub>O<sub>12</sub> species was also greatly enhanced, and the reduction in grain size indicated that Mn<sup>n+</sup> entered into the (Ce,La)CO<sub>3</sub>F lattice causing lattice shrinkage. The number of acidic sites on the catalyst surface and the redox capacity were enhanced. The amount of Ce<sup>3+</sup> in the catalyst was also enhanced by the introduction of Mn<sup>n+</sup>, but the proportion of adsorbed oxygen decreased, which indicated that the introduction of Mn<sup>n+</sup> was detrimental to the increase in the proportion of adsorbed oxygen. The reaction mechanisms of the (Ce,La)CO<sub>3</sub>F and Mn/(Ce,La)CO<sub>3</sub>F catalysts were investigated by <i>in-situ</i> Fourier transform infrared spectroscopy (FTIR). The results showed that catalysts followed the E-R and L-H mechanisms. When loaded with Mn, the main reactive species in the L-H mechanism were the </span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species on the Br<span style="white-space:nowrap;">ø</span>nsted acidic site and the O-Ce<sup>3+</sup>-O-NO, O-Mn<sup>3+</sup>-O-NO species. The main reactive species for the E-R mechanism were NH<sub>3</sub>/</span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species and NO. The </span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species on the Br<span style="white-space:nowrap;">ø</span>nsted acidic sites act as the main reactive NH3</span></span></span><span><span><sub><span style="font-family:;" "=""> </span></sub></span></span><span><span><span style="font-family:;" "="">(g) adsorbing species, bonded to the Ce<sup>4+</sup> in the carrier (Ce,La)CO<sub>3</sub>F to participate in the acid cycle reaction. The introduction of Mn<sup>n+</sup> increases the number of Br<span style="white-space:nowrap;">ø</span>nsted acidic sites on the catalyst surface, and acts as an adsorption site for NO, to react with NO to generate more monodentate nitrate species, to participate in the redox cycle reactions. The above results indicated that Mn<sup>n+</sup> and (Ce,La)CO<sub>3</sub>F have a good mutual promotion effect, which makes the loaded catalyst have excellent performance, which provides a theoretical basis for the high value utilization of bastnaesite</span></span></span><span><span><span style="font-family:;" "="">.</span></span></span>展开更多
文摘采用柠檬酸溶胶 凝胶法制备的Ce Zr La O固溶体为载体,制备CuO Ce Zr La O催化剂,用XRD,Raman,TPR等实验技术对Ce Zr La O固溶体及CuO Ce Zr La O的物相、Redox性能进行了表征。实验结果表明,Ce0.7Zr0 3-yLayO固溶体的还原性能与La含量有关,适量的La能促进固溶体的氧化还原。CuO的负载量为6%时,CuO Ce0.7Zr0.15La0.15O的活性最高,高分散且与载体相互作用的CuO是CO氧化活性相。
文摘In accordance with the cerium-lanthanum ratio of fluorocerium ores in the mineralogy of the Baiyun Ebo process, the (Ce,La)CO<sub>3</sub>F grains were synthesised by hydrothermal method using pure material to simulate bastnaesite minerals, and used as NH<sub>3</sub>-SCR denitrification catalysts. The activity results showed that the synthetic (Ce,La)CO<sub>3</sub>F was roasted at 500<span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">, and the NOx conversion was 27% at 200</span></span></span><span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">. The NH<sub>3</sub></span></span></span><span><span><span style="font-family:;" "="">-</span></span></span><span><span><span style="font-family:;" "="">SCR catalytic activity of the synthesised (Ce,La)CO<sub>3</sub>F was improved by loaded transition metal Mn. The best catalyst was found to be produced by impregnating (Ce,La)CO<sub>3</sub>F with 1 mol/L manganese nitrate solution, with a NOx conversion of 80% at 250</span></span></span><span><span><span style="font-family:;" "=""><span style="white-space:nowrap;">˚</span>C</span></span></span><span><span><span style="font-family:;" "="">. The loading of Mn resulted in the appearance of numerous well-dispersed MnOx species on the catalyst surface, the dispersion of Ce<sub>7</sub>O<sub>12</sub> species was also greatly enhanced, and the reduction in grain size indicated that Mn<sup>n+</sup> entered into the (Ce,La)CO<sub>3</sub>F lattice causing lattice shrinkage. The number of acidic sites on the catalyst surface and the redox capacity were enhanced. The amount of Ce<sup>3+</sup> in the catalyst was also enhanced by the introduction of Mn<sup>n+</sup>, but the proportion of adsorbed oxygen decreased, which indicated that the introduction of Mn<sup>n+</sup> was detrimental to the increase in the proportion of adsorbed oxygen. The reaction mechanisms of the (Ce,La)CO<sub>3</sub>F and Mn/(Ce,La)CO<sub>3</sub>F catalysts were investigated by <i>in-situ</i> Fourier transform infrared spectroscopy (FTIR). The results showed that catalysts followed the E-R and L-H mechanisms. When loaded with Mn, the main reactive species in the L-H mechanism were the </span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species on the Br<span style="white-space:nowrap;">ø</span>nsted acidic site and the O-Ce<sup>3+</sup>-O-NO, O-Mn<sup>3+</sup>-O-NO species. The main reactive species for the E-R mechanism were NH<sub>3</sub>/</span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species and NO. The </span></span></span><span><span><span style="font-family:;" "=""><span></span></span></span></span><span><span><span style="font-family:;" "=""><span> </span>(ad) species on the Br<span style="white-space:nowrap;">ø</span>nsted acidic sites act as the main reactive NH3</span></span></span><span><span><sub><span style="font-family:;" "=""> </span></sub></span></span><span><span><span style="font-family:;" "="">(g) adsorbing species, bonded to the Ce<sup>4+</sup> in the carrier (Ce,La)CO<sub>3</sub>F to participate in the acid cycle reaction. The introduction of Mn<sup>n+</sup> increases the number of Br<span style="white-space:nowrap;">ø</span>nsted acidic sites on the catalyst surface, and acts as an adsorption site for NO, to react with NO to generate more monodentate nitrate species, to participate in the redox cycle reactions. The above results indicated that Mn<sup>n+</sup> and (Ce,La)CO<sub>3</sub>F have a good mutual promotion effect, which makes the loaded catalyst have excellent performance, which provides a theoretical basis for the high value utilization of bastnaesite</span></span></span><span><span><span style="font-family:;" "="">.</span></span></span>