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Micro-crystalline molybdenum sulfide prepared by mechanical milling as an unsupported model catalyst for the hydrodesulfurization of diesel fuel

机译:通过机械研磨制备的微晶硫化钼,用作柴油加氢脱硫的无载体模型催化剂

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Micro-crystalline molybdenum sulfide (MoS2) Was prepared by mechanical milling as an unsupported model catalyst for hydrodesulfurization (HDS) of diesel fuel, was prepared by mechanical milling. The catalytic function of the micro-crystallite was analyzed on the basis of the data from XRD measurements, TEM observations, and activity measurements. During the activity measurements, desulfurization of 4,6-dimethyldibenzothiophene (4,6-DMDBT) was carried out at 320 degreesC in an autoclave initially charged with 5 MPa of hydrogen. The desulfurizing kinetics was evaluated for the unsupported MoS2 in comparison with an industrial catalyst, alumina-supported cobalt-molybdenum sulfide. The unsupported MoS2 was more able to enhance the desulfurizing kinetics for 4,6-DMDBT than the industrial catalyst under the equivalent weight of molybdenum, while the unsupported MoS2 was inferior to the industrial catalyst in desulfurizing dibenzothiophene (DBT). Since the major catalyzed reaction was the hydrogenative desulfurization for the unsupported MoS2, it was an appropriate catalyst for 4,6-DMDBT, which was desulfurized under steric hindrance. Catalyst fouling was analyzed on the basis of the data from the real HDS reaction with diesel fuel in a down-flow tubular reactor, at 330-360 degreesC with 1.5-3.0 h(-1) under 5 MPa of hydrogen. The deposited carbon and the nitrogen constituents fouled the unsupported MoS2 more seriously than was the case for the industrial catalyst. (C) 2004 Elsevier B.V. All rights reserved.
机译:通过机械研磨制备微晶硫化钼(MoS2),作为柴油机加氢脱硫(HDS)的无载体模型催化剂,通过机械研磨制备。基于来自XRD测量,TEM观察和活性测量的数据分析了微晶的催化功能。在活性测量期间,在320℃下在初始装有5MPa氢气的高压釜中进行4,6-二甲基二苯并噻吩(4,6-DMDBT)的脱硫。与工业催化剂氧化铝负载的钴-钼钼硫化物相比,评估了无负载的MoS2的脱硫动力学。在钼当量下,未负载的MoS2比工业催化剂更能增强4,6-DMDBT的脱硫动力学,而在二苯并噻吩(DBT)脱硫中,未负载的MoS2不及工业催化剂。由于主要的催化反应是未负载的MoS2的氢化脱硫,因此它是4,6-DMDBT的合适催化剂,该催化剂在空间位阻下被脱硫。根据实际的HDS反应与柴油在下流管式反应器中于330-360摄氏度,1.5-3.0 h(-1)和5 MPa氢气下的数据进行分析。与工业催化剂相比,沉积的碳和氮成分更严重地污染了未负载的MoS2。 (C)2004 Elsevier B.V.保留所有权利。

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