王斐, 钟梅, 李建, 亚力昆江·吐尔逊, 靳立军. 机械球磨法制备NiMo催化剂及其在菲加氢中的应用[J]. 燃料化学学报(中英文), 2023, 51(2): 165-174. DOI: 10.19906/j.cnki.JFCT.2022045
引用本文: 王斐, 钟梅, 李建, 亚力昆江·吐尔逊, 靳立军. 机械球磨法制备NiMo催化剂及其在菲加氢中的应用[J]. 燃料化学学报(中英文), 2023, 51(2): 165-174. DOI: 10.19906/j.cnki.JFCT.2022045
WANG Fei, ZHONG Mei, LI Jian, YALKUN·Tursun, JIN Li-jun. Preparation of mesoporous NiMo catalyst by mechanical ball milling for hydrogenation of phenanthrene[J]. Journal of Fuel Chemistry and Technology, 2023, 51(2): 165-174. DOI: 10.19906/j.cnki.JFCT.2022045
Citation: WANG Fei, ZHONG Mei, LI Jian, YALKUN·Tursun, JIN Li-jun. Preparation of mesoporous NiMo catalyst by mechanical ball milling for hydrogenation of phenanthrene[J]. Journal of Fuel Chemistry and Technology, 2023, 51(2): 165-174. DOI: 10.19906/j.cnki.JFCT.2022045

机械球磨法制备NiMo催化剂及其在菲加氢中的应用

Preparation of mesoporous NiMo catalyst by mechanical ball milling for hydrogenation of phenanthrene

  • 摘要: 采用机械球磨法制备NiMo催化剂,通过XRD、XPS等表征其结构,探究Ni/(Ni+Mo)比对催化剂组成和结构及菲加氢性能的影响。结果表明,该法制备的催化剂活性组分Ni和Mo的分散性好,为孔径集中分布于2−10 nm的介孔催化剂。随Ni/(Ni+Mo)比增加,催化剂的比表面积和MoIV含量呈现出先增加后降低趋势,均于0.33处达到最高。适量Ni促进Mo硫化形成NiMoS活性相,过量的Ni会形成NixSy,覆盖活性位点,降低加氢活性。恒定Ni/(Ni+Mo)比为0.33,催化剂的比表面积随Ni、Mo含量增加明显降低,而MoIV含量增加。增加硫化剂硫代硫酸铵(ATS)的用量,可同时提高催化剂的比表面积和MoIV的含量。Ni/(Ni+Mo)比对菲转化率的影响表现出与催化剂中MoIV含量相一致的变化趋势,当Ni/(Ni+Mo)比为0.33时,菲转化率达最高值74.7%。在该比例下,Ni、Mo含量及S/Mo比分别增至4.8%、16%和4.5时,菲的转化率达96.5%,八氢菲和全氢菲的总选择性和产率分别为83.9%和80.9%,且菲主要从侧环进行深度加氢形成全氢菲。

     

    Abstract: The NiMo catalysts were prepared using the mechanical ball milling method, and their structures were characterized by XRD and XPS to investigate the effects of the Ni/(Ni+Mo) ratio on catalyst composition and structure, as well as the performance of phenanthrene hydrogenation. The results show that the catalysts prepared by this method have good dispersion of active components Ni and Mo, and are mesoporous catalysts with a concentrated pore size distribution in the range of 2−10 nm. The specific surface area and MoIV content of the catalysts increase first and then decrease as the Ni/(Ni+Mo) ratio increases, both reaching maximum values at 0.33. The moderate amount of Ni promotes Mo sulfidation to form the NiMoS active phase, while the excessive amount of Ni forms NixSy, which covers active sites and reduces the hydrogenation activity. When the Ni/(Ni+Mo) ratio maintains at 0.33, the specific surface area of the catalyst decreases as Ni and Mo content increases, while MoIV content shows an increase trend. Raising the amount of sulfurizing agent ammonium thiosulfate (ATS) could increase both the specific surface area and MoIV content of the catalyst. It is observed that the effect of the Ni/(Ni+Mo) ratio on phenanthrene conversion is consistent with the MoIV content of catalyst, and the maximum value of 74.7% is obtained at the Ni/(Ni+Mo) ratio of 0.33. This further rises to 96.5% when the Ni and Mo contents and S/Mo ratio increase to 4.8%, 16% and 4.5, respectively. Meanwhile, the total selectivity and yield of octahydrophenanthrene and perhydrophenanthrene reach 83.9% and 80.9%, respectively. Furthermore, perhydrophenanthrene is mainly formed by hydrogenation of side ring of phenanthrene.

     

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