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Non-oxidative dehydroaromatization of methane: an effective reaction-regeneration cyclic operation for catalyst life extension

机译:甲烷的非氧化脱氢芳族化:催化剂生命延伸的有效反应再生循环操作

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摘要

Non-oxidative methane aromatization is an attractive direct route for producing higher hydrocarbons. It is highly selective to benzene despite the low conversion due to thermodynamic limitations, and Mo/H-ZSM-5, the first catalyst proposed for this reaction, is still considered as one of the most adequate. The major problem of this process is the severe catalyst deactivation due to the rapid build-up of carbonaceous deposits on the catalysts. Here we present an effective regeneration procedure that extends the life of Mo/ zeolite based catalysts by combining reaction periods of 1.5 h with 0.5 h regeneration steps in a continuous cyclic mode and methane activation after each regeneration stage. Benzene productivity obtained with Mo/ZSM-5 is shown to be almost constant for increasing TOS ranges when applying this new cyclic protocol, and threefold values are achieved for an 18 h on stream period by limiting the reaction steps to the first 1.5 h of maximum benzene selectivity (97 vs. 33 g benzene per kg cat h) compared to a conventional single run.
机译:非氧化甲烷芳香化是产生较高烃的有吸引力的直接途径。尽管由于热力学限制而转化较低,但它对苯具有高度选择性,而对该反应提出的第一个催化剂mo/h-ZSM-5仍然被认为是最适当的催化剂。该过程的主要问题是由于催化剂上碳质沉积物的迅速积聚而导致严重的催化剂失活。在这里,我们提出了一种有效的再生程序,该程序通过将1.5 h的反应周期与0.5 h的再生步骤相结合,以连续的环状模式和甲烷激活在每个再生阶段后延长基于Mo/沸石的催化剂的寿命。使用MO/ZSM-5获得的苯生产率在应用此新的环状方案时显示出TOS范围的增加几乎是恒定的,并且通过将反应步骤限制为最大值的最大值的最大1.5 h,在18小时内达到了三倍的值。与传统的单次运行相比,苯选择性(每公斤cat H苯苯H苯苯H苯h)为33 g苯。

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