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CATALYTIC PERFORMANCE OF Ni/ZSM-5 CATALYSTS FOR C9 ALKYL-AROMATICS HYDRODEALKYLATION

机译:Ni / ZSM-5催化剂对C9烷基芳烃加氢脱烷基化反应的催化性能

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Aromatics are an important raw material for the production of monomer for polyesters and engineering plastics, detergents, pharmaceuticals, etc. Benzene, toluene, and xylenes (BTX) is produced by naphtha reforming and pyrolysis, in which the proportion of each aromatic is controlled thermodynamically. BTX are the three basic aromatic starting reactants (1). Hydrodealkylation is a common route in the petrochemical industry. Benzene for example is produced from either pyrolysis gasoline or pure alkylaromatic hydrocarbons, mostly toluene, thermally or catalytically reaction (2). As is known, thermal processes require relatively high temperatures (973–998 K) compared to catalytic ones which usually take place at 873–898 K and high temperatures increase the heavy aromatic hydrocarbon content such as naphthalene and decrease the benzene selectivity. Moreover, catalytic processes are of course more economic provided a highly selective catalyst can be found (3). A series of H/ZSM-5 and Ni/ZSM-5 catalysts were chosen to improve catalytic activity, permitting an increase in C9 alkyl-aromatics conversion, increase the selectivity of the process by reducing the final concentration of by-products, increase catalyst life, thus prolonging regeneration cycles. In the work, they were studied to evaluate the role of metallic function and catalyst activity in the process of BTX.
机译:芳族化合物是生产聚酯和工程塑料,洗涤剂,药品等单体的重要原料。苯,甲苯和二甲苯(BTX)是通过石脑油重整和热解生产的,其中每种芳族化合物的比例均通过热力学控制。 BTX是三种基本的芳香族起始反应物(1)。加氢脱烷基化是石化工业中的常见途径。例如,苯是由热解或催化反应(2)由热解汽油或纯净的烷基芳香烃(主要是甲苯)制得的。众所周知,与通常在873-898 K发生的催化过程相比,热过程需要相对较高的温度(973-998 K),并且高温会增加重芳烃的含量,例如萘,并降低苯的选择性。此外,如果可以发现高选择性催化剂,催化过程当然更经济(3)。选择了一系列H / ZSM-5和Ni / ZSM-5催化剂来提高催化活性,从而增加C9烷基芳族化合物的转化率,通过降低副产物的最终浓度来提高工艺的选择性,增加催化剂寿命,从而延长再生周期。在工作中,他们被研究以评估金属功能和催化剂活性在BTX过程中的作用。

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