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Investigation into the effect of the intermediate carbon carrier on the catalytic activity of the HDS catalysts prepared using heteropolycompounds

机译:研究中间碳载体对使用杂多化合物制备的HDS催化剂的催化活性的影响

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摘要

The effect of the intermediate activated carbon covering the alumina carrier on catalytic activity of the supported transition metal sulfides (TMS) prepared from heteropolycompounds (HPCs) in thiophene hydrodesulfurization (HDS), benzene hydrogenation (HYD) and hydrotreating (including HDS of S-containing and HYD of polyaromatic compounds) of diesel oil fractions was investigated. Carbon content on the alumina carrier varied from 0 to 3.8 wt.%. It was found that the structure of carbon coating the alumina surface changes depending on the presence/absence of the active phase on the intermediate activated carbon. Total catalytic activity of the catalysts in HDS and HYD reactions was maximal for carbon content of 1-2 wt.% and fell down for catalysts with 3.8 wt.% of carbon. The specific catalytic activity grew proportionally to the carbon content on the catalyst. The experimental data showed that a rise of the reaction temperature leads to a decrease in the amount of adsorbed hydrogen whose deficiency limits the formation of H2S. It was supposed that the intermediate carbon placed between the alumina carrier and the active phase accumulates hydrogen inside carbon pores. Besides, the intermediate C-carrier of the catalysts synthesized from Co(Ni) salts of heteropolycompounds promotes rising of stacking number in nanoslabs of the active CoMoS phase of the second type.
机译:中间活性炭覆盖氧化铝载体对由杂多化合物(HPC)制备的负载过渡金属硫化物(TMS)在噻吩加氢脱硫(HDS),苯加氢(HYD)和加氢处理(包括含S的HDS)中的催化活性的影响柴油馏分的HYD和HYD)。氧化铝载体上的碳含量为0至3.8重量%。已经发现,覆盖氧化铝表面的碳的结构根据中间活性炭上活性相的存在/不存在而变化。对于HDS和HYD反应,催化剂的总催化活性对于1-2重量%的碳含量是最大的,而对于具有3.8重量%的碳的催化剂而言下降。比催化活性与催化剂上的碳含量成比例地增长。实验数据表明,反应温度的升高导致氢吸附量的减少,而氢的缺乏限制了H2S的形成。据推测,放置在氧化铝载体和活性相之间的中间碳在碳孔内积累了氢。此外,由杂多化合物的Co(Ni)盐合成的催化剂的中间C-载体促进了第二种活性CoMoS相的纳米板中堆积数的增加。

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