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Improvements on Selective Conversion of Methanol and/or Dimethylether into Liquefied Petroleum Gas over Zeolite Catalysts

机译:在沸石催化剂上改善甲醇和/或二甲醚将甲醇和/或二甲醚转化成液化石油气中的催化剂

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For the proposed LPG synthesis, ethylene recirculation conversion with methanol or dimethylether was investigated by the simulation tests of using the coupled reaction of ethylene with oxygenates. The process selectivity in converting unit can be enhanced significantly after a fully recirculation of formed C2 components. For the MFI metallosilicate catalysts, the assembled modes of MFI heteroatoms were correlated with performance in methanol conversion to LPG hydrocarbons. Zeolites containing gallium or gallium-aluminum catalyze methanol conversion along with aromatization. The H-FeAlMFI leads to a great restraint towards aromatization and carbon-chain growth; the zeolite that comprises iron and aluminum was confirmed quite effective for improving the LPG fractional selectivity. The DME conversion results concerning H-FeAlMFI-silicate and unmodified H-ZSM-5 confirmed the improvements in catalytic selectivity and active stability.
机译:对于所提出的LPG合成,通过使用乙烯与含氧化合物的偶联反应的模拟试验研究了用甲醇或二甲醚的乙烯再循环转化。在形成的C2组分的完全再循环后,可以显着提高转换单元的过程选择性。对于MFI金属硅酸盐催化剂,MFI杂原子的组装模式与甲醇转化为LPG烃的性能相关。含镓或镓 - 铝催化甲醇转化的沸石以及芳香化。 H-FEALMFI导致富裕的芳香化和碳链增长束缚;包含熨斗和铝的沸石对改善LPG分数选择性非常有效。关于H-FealMFI-硅酸盐和未修饰的H-ZSM-5的DME转化结果证实了催化选择性和活性稳定性的改善。

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