Abstract
Lower loading of Fe (1 wt%) and higher reaction temperature (450 °C) led to higher and stable selectivity of C3+ olefins by ethanol conversion using Fe/H-ZSM-5 catalysts. Carbon deposition and framework collapse of zeolite support, which may be the cause of change in selectivity of products, was suppressed in some degree.
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Inaba, M., Murata, K. & Takahara, I. Effect of Fe-loading and reaction temperature on the production of olefins from ethanol by Fe/H-ZSM-5 zeolite catalysts. React Kinet Catal Lett 97, 19–26 (2009). https://doi.org/10.1007/s11144-009-0002-8
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DOI: https://doi.org/10.1007/s11144-009-0002-8