Abstract
Addition of Pt and K to Ga2O3/Al2O3 was shown to be beneficial for isobutane dehydrogenation. This catalytic system can be successfully realized in both fluidized and fixed-bed reactors. In contrast to supported catalysts based on CrOx and Pt–Sn, the catalyst performance of the supported Ga–Pt–K catalyst only marginally changed after 3 hours of dehydrogenation.
Original language | English |
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Pages (from-to) | 7719-7723 |
Number of pages | 5 |
Journal | Catalysis Science and Technology |
Volume | 10 |
DOIs | |
Publication status | Published - 2020 |
MoE publication type | A1 Journal article-refereed |