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首页> 外文期刊>Journal of Catalysis >The active site of nickel phosphide catalysts for the hydrodesulfurization of 4,6-DMDBT
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The active site of nickel phosphide catalysts for the hydrodesulfurization of 4,6-DMDBT

机译:磷化镍催化剂用于4,6-DMDBT加氢脱硫的活性中心

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Ni2P catalysts supported on SiO2 and MCM-41 were prepared by temperature-programmed reduction (TPR), and the effect of the dispersion on catalyst structure and hydroprocessing performance was studied. The surface areas of the samples varied from low (Ni2P/SiO2-L, 88 m(2) g(-1)) to high (Ni2P/SiO2-H, 240 m(2) g(-1)), to very high (Ni2P/MCM-41, 487 m(2) g(-1)), with corresponding Ni2P average crystallite sizes decreasing from 10.1 to 6.5 and 3.8 nm. X-ray diffraction (XRD) and extended X-ray absorption fine structure (EXAFS) studies were used to obtain structural parameters for the supported NO phase. The catalytic activity in hydrodesulfurization (HDS) was measured at 613 K and 3.1 MPa in a three-phase fixed bed reactor using a model liquid feed containing 4,6-dimethyldibenzothiophene (4,6-DMDBT) and quinoline in a tridecane solvent. At standard conditions using 500 ppm S as 4,6-DMDBT, 6000 ppm S as dimethyldisulfide (DMDS), and 500 ppm N as quinoline, the catalytic activity followed the sequence Ni2P/MCM-41 > Ni2P/SiO2-H > Ni2P/SiO2-L, based on equal sites (230 mu mol) loaded in the reactor. In particular, Ni2P/MCM-41 gave an HDS conversion of 90%, which was much higher than that of a commercial Ni-Mo-S/Al2O3 catalyst which gave an HDS conversion of 68%, based on equal number of sites (230 mu mol) loaded in the reactor. The sites were counted by CO chemisorption for the phosphide and by low-temperature O-2 chemisorption for the sulfide. EXAFS analysis of the samples confirmed the presence of two types of sites, tetrahedral Ni(1) sites and square pyramidal Ni(2) sites, with the latter growing in number in the same order as the reactivity Ni2P/MCM-41 > Ni2P/SiO2-H > Ni2P/SiO2-L, as the crystallite size decreased. From the selectivity to the direct desulfurization (DDS) product (dimethylbiphenyl) and the hydrogenation (HYD) products (methylcyclohexyltoluenes and dimethylbicyclohexyls) it is concluded that the Ni(1) sites are responsible for DDS while the Ni(2) are highly active sites for the HYD route. (C) 2008 Elsevier Inc. All rights reserved.
机译:通过程序升温还原(TPR)制备了负载在SiO2和MCM-41上的Ni2P催化剂,研究了分散液对催化剂结构和加氢性能的影响。样品的表面积从低(Ni2P / SiO2-L,88 m(2)g(-1))到高(Ni2P / SiO2-H,240 m(2)g(-1))不等高(Ni2P / MCM-41,487 m(2)g(-1)),相应的Ni2P平均晶粒尺寸从10.1降至6.5和3.8 nm。 X射线衍射(XRD)和扩展的X射线吸收精细结构(EXAFS)研究用于获得负载型NO相的结构参数。在三相固定床反应器中,使用包含在十三烷溶剂中的4,6-二甲基二苯并噻吩(4,6-DMDBT)和喹啉的模型液体进料,在613 K和3.1 MPa下测量了加氢脱硫(HDS)的催化活性。在使用500 ppm S作为4,6-DMDBT,6000 ppm S作为二甲基二硫化物(DMDS)和500 ppm N作为喹啉的标准条件下,催化活性遵循以下顺序Ni2P / MCM-41> Ni2P / SiO2-H> Ni2P / SiO2-L,基于反应器中负载的相等位点(230摩尔)。特别是,Ni2P / MCM-41的HDS转化率为90%,远高于市售Ni-Mo-S / Al2O3催化剂的HDS转化率为68%(基于相同的位点数)(230 (μmol)装入反应器中。通过CO对磷的化学吸附和通过低温O-2对硫化物的化学吸附来计算位点。样品的EXAFS分析证实存在两种类型的位点,四面体Ni(1)位点和方形锥体Ni(2)位点,后者的数量按与反应性Ni2P / MCM-41> Ni2P / SiO2-H> Ni2P / SiO2-L,随着微晶尺寸的减小。从选择性到直接脱硫(DDS)产物(二甲基联苯)和加氢(HYD)产物(甲基环己基甲苯和二甲基双环己基)得出结论,Ni(1)位点负责DDS,而Ni(2)是高活性位点HYD路线。 (C)2008 Elsevier Inc.保留所有权利。

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