Sammanfattning
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.
Originalspråk | Engelska |
---|---|
Sidor (från-till) | 7719-7723 |
Antal sidor | 5 |
Tidskrift | Catalysis Science and Technology |
Volym | 10 |
DOI | |
Status | Publicerad - 2020 |
MoE-publikationstyp | A1 Tidskriftsartikel-refererad |