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首页> 外文期刊>Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications >Catalytic potential of carbon-supported NiMo-sulfide for ultra-deep hydrodesulfurization of diesel fuel
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Catalytic potential of carbon-supported NiMo-sulfide for ultra-deep hydrodesulfurization of diesel fuel

机译:碳载NiMo-硫化物对柴油超深度加氢脱硫的催化潜力

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摘要

Carbon-supported NiMo-sulfide (NMC) catalysts were prepared using a variety of active carbons,whose surface area ranged from 916 to 3075 m~2 g~(-1),in order to examine the effect of properties of the carbon support on hydrodesulfurization (HDS) activity to 4,6-dimethyldibenzothiophenes (4,6-DMDBT).The HDS activity,measured at 320 deg C using an autoclave,tended to be enhanced with an increase in the surface area of the active carbon.The increase in the surface area enhanced dispersion of the catalytic active component.The active carbon of rich oxygen functional groups was negatively deflected from the tendency mentioned above because of the restricted dispersion of the active component.For this active carbon,reduction of the oxygen surface groups resulted in enhancing the HDS activity.NMC prepared using the best carbon,whose surface area was the largest (3075 m~2 g~(-1)),catalyzed the hydrogenative HDS reaction of the refractory 4,6-DMDBT,as well as DBT,more than the conventional alumina-supported NiMo-sulfide (NMA).In HDS reaction of the real-feedstock using a down-flow tubular reactor with LHSV of 1.5 h~(-1) under H_2 pressure of 5 MPa in volumetric H2/oil ratio of 250 nl l~(-1),the best NMC achieved 10 ppm-S at 337 deg C.For NMA,10 ppm-S was not achieved at even the maximum temperature in the real HDS reaction,350 deg C.The HDS rate constant was ca.four times larger for the best NMC than for NMA.
机译:为了研究碳载体的性能对碳载NiMo硫化物(NMC)催化剂的影响,该活性炭的表面积为916〜3075 m〜2 g〜(-1)。加氢脱硫(HDS)活性变成4,6-二甲基二苯并噻吩(4,6-DMDBT).HDS活性在320℃下用高压釜测量,倾向于随着活性炭表面积的增加而增强。由于活性组分的分散受到限制,富氧官能团的活性炭从上述趋势中发生了负向偏转。对于这种活性炭,氧表面基团的还原用最佳碳制备的NMC,其表面积最大(3075 m〜2 g〜(-1)),催化了难处理的4,6-DMDBT以及DBT的氢化HDS反应。 ,比传统的铝板Na负载的NiMo硫化物(NMA)。在下行进料管式反应器的HDS反应中,LHSV为1.5 h〜(-1),H_2压力为5 MPa,体积H2 /油比为250 nl l〜(-1),最好的NMC在337摄氏度时达到10 ppm-S。对于NMA,即使在实际HDS反应的最高温度350摄氏度下也没有达到10 ppm-S.HDS速率常数为最佳NMC的大小大约是NMA的四倍。

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