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Dehydrogenation of propane over Ga and Cr modified, 'fresh' and steamed, MFI-type zeolites

机译:Ga和Cr修饰,“新鲜”和蒸,MFI型沸石上的丙烷脱氢。

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In this work we synthesized MFI type zeolites with chromium and gallium. Hydrothermal synthesis was applied using, either aluminum with gallium or chromium sources in 1:1 mole ratios, or impregnation of H-ZSM-5 with the desired metal. The "as synthesized" samples were characterized by XRD, Chemical analysis, SEM-EDS, SSA, ammonia-TPD and subjected to severe steaming, in order to suppress their acidity and consequently decrease the oligomerization capability of the formed catalysts. The catalytic activity of the zeolite samples in propane dehydrogenation was investigated using a fixed-bed continuous-flow glass reactor. The catalytic test results revealed that propylene yield and selectivity over the steamed catalysts increased remarkably (e.g. propylene yield ~11% with selectivity of ~45%, for H-[Ga/Al]ZSM-5), as a consequence of the suppression of their acidity and therefore of the dramatic decrease of their oligomerization capability. The above results suggest that Cr- and Ga-modified steamed zeolites are promising catalysts for the dehydrogenation of propane to propylene.
机译:在这项工作中,我们用铬和镓合成了MFI型沸石。用镓或铬源在1:1摩尔比中使用铝,或用所需金属浸渍H-ZSM-5,施用水热合成。通过XRD,化学分析,SEMEDS,SSA,氨-TPD并进行严重蒸汽,以抑制它们的酸度并因此降低所形成的催化剂的低聚能力,以“合成”样品特征。使用固定床连续流动玻璃反应器研究丙烷脱氢中沸石样品的催化活性。催化试验结果显示,由于抑制,升降催化剂对蒸汽催化剂的选择性显着增加(例如丙烯产率〜11%,选择性为〜45%,选择性〜45%)。它们的酸度,因此对寡聚化能力的显着降低。上述结果表明,Cr-和Ga-改性的蒸沸石是丙烷脱氢丙烷脱氢的催化剂。

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