首页> 外文期刊>Applied Petrochemical Research >Preparation of novel mesoporous Ce-NiSubscript2/SubscriptP/SBA-15 catalysts and their catalytic performance for hydrodesulfurization of dibenzothiophene
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Preparation of novel mesoporous Ce-NiSubscript2/SubscriptP/SBA-15 catalysts and their catalytic performance for hydrodesulfurization of dibenzothiophene

机译:新型介孔Ce-Ni 2 P / SBA-15催化剂的制备及其对二苯并噻吩加氢脱硫的催化性能

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Ni2P/SBA-15 precursors with Ni2P loadings of 25?wt% and initial P/Ni of 0.8 were prepared using nickel nitride as nickel source, diammonium hydrogen phosphide as phosphorus and mesopore molecular sieve SBA-15 as support. Then Ce was introduced into the Ni2P/SBA-15 precursor. The novel mesoporous Ce-Ni2P/SBA-15 catalysts were prepared after temperature-programmed reduction in flowing H2. The structure was characterized by X-ray diffraction, N2 adsorption–desorption isotherms, NH3 temperature-programmed desorption and X-ray photoelectron spectroscopy. The catalytic activities for the hydrodesulfurization (HDS) of dibenzothiophene (DBT) were evaluated. The results showed that only Ni2P phase was formed in Ce-Ni2P/SAB-15 catalysts with Ce loadings of 0–5?wt%. Ni2P and Ni12P5 phases were existed in 7?wt% Ce-Ni2P/SBA-15 catalyst. The surface area and pore volume increased when Ce was added to Ni2P/SBA-15 catalyst. The strength of the acid sites and total acid amount of Ce-Ni2P/SBA-15 catalysts increased with increasing Ce loadings. Ce existed in the form of Ce3+and Ce4+, Ni existed in the form of Ni2+ and Niδ+, and P existed in the form of Pδ? and P5+. The addition of Ce to the Ni2P/SBA-15 catalyst decreased Niδ+ concentration in Ni2P/SBA-15 catalyst. The activity for HDS of DBT over Ni2P/SBA-15 catalysts was affected by the addition of Ce at 300–340?°C. The catalysts exhibited a good catalytic performance of deep hydrodesulfurization of dibenzothiophene and the conversion of DBT can reach 98.9?% at 380?°C. Biphenyl was the main product over Ce-Ni2P/SBA-15 catalysts and cyclohexylbenzene was the main product over Ni2P/SBA-15 catalyst at 380?°C.
机译:使用氮化镍作为镍源,磷化氢二铵作为磷和中孔分子筛SBA-15作为载体,制备了Ni2P含量为25wt%,初始P / Ni为0.8的Ni2P / SBA-15前体。然后将Ce引入Ni2P / SBA-15前驱体中。在程序升温还原流动的氢气后,制备了新型的介孔Ce-Ni2P / SBA-15催化剂。通过X射线衍射,N2吸附-脱附等温线,NH3程序升温脱附和X射线光电子能谱对结构进行了表征。评价了二苯并噻吩(DBT)的加氢脱硫(HDS)的催化活性。结果表明,在Ce-Ni2P / SAB-15催化剂中,只有Ce负载量为0-5wt%时才形成Ni2P相。 Ni2P和Ni12P5相存在于7wt%的Ce-Ni2P / SBA-15催化剂中。当将Ce添加到Ni2P / SBA-15催化剂中时,表面积和孔体积增加。 Ce-Ni2P / SBA-15催化剂的酸点强度和总酸量随Ce含量的增加而增加。 Ce以Ce3 +和Ce4 +的形式存在,Ni以Ni2 +和Niδ+的形式存在,P以Pδα和Pδ的形式存在。和P5 +。在Ni2P / SBA-15催化剂中添加Ce会降低Ni2P / SBA-15催化剂中的Niδ+浓度。在300–340°C下添加Ce会影响DBT在Ni2P / SBA-15催化剂上的HDS活性。该催化剂表现出良好的二苯并噻吩深度加氢脱硫的催化性能,在380℃下DBT的转化率可达到98.9%。在380℃下,联苯是Ce-Ni2P / SBA-15催化剂的主要产物,环己基苯是Ni2P / SBA-15催化剂的主要产物。

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