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首页> 外文期刊>Journal of the Japan Petroleum Institute >Catalytic Performance of Noble Metals Supported on Mesoporous Silica MCM-41 for Hydrodesulfurization of Benzothiophene
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Catalytic Performance of Noble Metals Supported on Mesoporous Silica MCM-41 for Hydrodesulfurization of Benzothiophene

机译:MCM-41介孔二氧化硅负载的贵金属对苯并噻吩加氢脱硫的催化性能

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The catalytic performances of noble metals (Pt, Rh, Pd, Ru) supported on mesoporous silica MCM-41 were investigated for the hydrodesulfurization (HDS) of benzothiophene (BT). The order of HDS activities of noble metal/MCM-41 catalysts was Pt>Rh>Pd》Ru. Pt/MCM-41 catalyst showed high HDS activity, which was higher than that of commercial CoMo/Al_2O_3 catalyst. The supported noble metal catalysts were characterized by TEM, XRD, hydrogen adsorption and benzene hydrogenation. The order of dispersion of noble metal on MCM-41 was Rh>Pt>Pd>Ru, which was not the same as that of HDS activities. On the other hand, the order of the activities of noble metal/MCM-41 catalysts for benzene hydrogenation was Pt>Rh>Pd>Ru. The hydrogenation activity of Pt/MCM-41 catalyst was regenerated after H_2S treatment, but the activities of other catalysts were not regenerated. Thus, high hydrogenation activity and sulfur tolerance are important factors to prepare highly active noble metal/MCM-41 catalysts. Pt/MCM-41 catalyst showed remarkably high and stable activity for the HDS of BT, but Pt/SiO_2 catalyst, with similar Pt dispersion on MCM-41, showed low activity which decreased with time on stream. Since MCM-41 showed higher acidity than SiO_2, hydrogenation activity and sulfur tolerance of Pt/MCM-41 catalyst were higher than those of Pt/SiO_2 catalyst. The results of FT-IR analysis indicated that the strength of interaction between BT and MCM-41 was stronger than that of SiO_2, suggesting that both acid sites of MCM-41 and Pt particles in the Pt/MCM-41 catalyst act as active sites for the HDS of BT. Furthermore, FT-IR spectra of BT adsorbed on Pt/MCM-41 revealed that BT interacts with the silanol group on the MCM-41 surface rather than the Pt surface. Therefore, we concluded that the high HDS activity of Pt/ MCM-41 catalyst could be attributed to the high hydrogenation activity of Pt and the acidity of the support.
机译:研究了介孔二氧化硅MCM-41上负载的贵金属(Pt,Rh,Pd,Ru)对苯并噻吩(BT)的加氢脱硫(HDS)的催化性能。贵金属/ MCM-41催化剂的HDS活性顺序为Pt> Rh> Pd》 Ru。 Pt / MCM-41催化剂表现出较高的HDS活性,高于商业CoMo / Al_2O_3催化剂。通过TEM,XRD,氢吸附和苯加氢表征了负载型贵金属催化剂。贵金属在MCM-41上的分散顺序为Rh> Pt> Pd> Ru,与HDS活性不同。另一方面,贵金属/ MCM-41催化剂对苯加氢的活性顺序为Pt> Rh> Pd> Ru。 H_2S处理后,Pt / MCM-41催化剂的氢化活性得以再生,而其他催化剂的活性并未再生。因此,高氢化活性和耐硫性是制备高活性贵金属/ MCM-41催化剂的重要因素。 Pt / MCM-41催化剂对BT的HDS具有很高的稳定性,而Pt / SiO_2催化剂在MCM-41上具有相似的Pt分散度,但活性较低,随生产时间的延长而降低。由于MCM-41的酸度高于SiO_2,因此Pt / MCM-41催化剂的加氢活性和耐硫性均高于Pt / SiO_2催化剂。 FT-IR分析结果表明BT与MCM-41的相互作用强度强于SiO_2,表明Mt-MCM-41催化剂中MCM-41和Pt颗粒的酸性位点均作为活性位点。用于BT的HDS。此外,吸附在Pt / MCM-41上的BT的FT-IR光谱表明,BT与MCM-41表面而不是Pt表面的硅烷醇基相互作用。因此,我们得出结论,Pt / MCM-41催化剂的高HDS活性可以归因于Pt的高氢化活性和载体的酸性。

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