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On the impact of co-feeding aromatics and olefins for the methanol-to-olefins reaction on HZSM-5

机译:芳烃和烯烃共进料对甲醇制烯烃反应对HZSM-5的影响

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摘要

The impact of adding various aromatic molecules (benzene, toluene, and xylenes) or olefins (ethene, propene, 1-butene, 1-pentene, and 1-hexene) to methanol over a HZSM-5 catalyst on activity and selectivity was systematically studied. Addition of a low concentration of aromatic molecules (16-32 C%), which are free of diffusion constraints, significantly enhanced the aromatics-based catalytic cycle and greatly suppressed the olefin-based cycle. This led to enhanced methane and ethene formation and methylation of aromatic rings at the expense of propene and C_(4+) higher olefins. The ratio of propene to ethene is controlled by the concentration of the aromatic molecules added. Co-feeding the same molar concentration of benzene, toluene and p-xylene influenced the methanol conversion to a nearly identical extent, as none of them experience transport constraints and the methylation rapidly equilibrates the aromatic molecules retained in the pores. In stark contrast, addition of small concentrations (10-40 C%) of C_(3-6) olefins with 100 C% methanol does not selectively suppress the catalytic cycle based on aromatic molecules. This led to unchanged selectivities to ethene and higher olefins (C_(3+)). Within the C_(3+) fraction, the selectivity to propene decreased and the selectivity to butenes were enhanced with increasing concentration of the co-fed olefin. Because of the relatively fast rates in methylation and cracking of C_(3-6) olefins in the olefin-based cycle, the product distributions at high methanol conversion were identical when co-feeding C_(3-6) olefins with the same carbon concentrations. This work provides further insights into the two distinct catalytic cycles operating for the methanol conversion to produce ethene and propene over HZSM-5 catalysts.
机译:系统地研究了在HZSM-5催化剂上向甲醇中添加各种芳族分子(苯,甲苯和二甲苯)或烯烃(乙烯,丙烯,1-丁烯,1-戊烯和1-己烯)对活性和选择性的影响。 。添加不受扩散限制的低浓度芳族分子(16-32 C%),可显着增强基于芳族化合物的催化循环并大大抑制基于烯烃的循环。这导致甲烷和乙烯的形成增加以及芳环的甲基化,但以丙烯和C_(4+)高级烯烃为代价。丙烯与乙烯的比例由所添加的芳族分子的浓度控制。共进料相同摩尔浓度的苯,甲苯和对二甲苯对甲醇的转化影响程度几乎相同,因为它们都没有遇到运输限制,而甲基化迅速平衡了保留在孔中的芳族分子。与之形成鲜明对比的是,将少量(10-40 C%)的C_(3-6)烯烃与100 C%甲醇一起添加不会选择性地抑制基于芳族分子的催化循环。这导致对乙烯和高级烯烃(C_(3+))的选择性不变。在C_(3+)馏分中,随着共进料烯烃浓度的增加,对丙烯的选择性降低,对丁烯的选择性提高。由于在基于烯烃的循环中C_(3-6)烯烃的甲基化和裂化速度相对较快,因此当共同进料具有相同碳浓度的C_(3-6)烯烃时,高甲醇转化率下的产物分布是相同的。这项工作为HZSM-5催化剂上甲醇转化生成乙烯和丙烯的两个不同催化循环提供了进一步的见解。

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