作者: M. P. Lobera , C. Téllez , J. Herguido , M. Menéndez
DOI: 10.1021/IE900381P
关键词:
摘要: n-Butane dehydrogenation over a Pt−Sn/MgAl2O4 catalyst has been carried out in two-zone fluidized-bed reactor (TZFBR), where oxidation and reduction of this occurs the same vessel but separate zones. This allows working continuous mode with situ regeneration, unlike traditional systems that require two different reactors or single periodic operation. The effect main TZFBR operating variables was studied its performance compared conventional loaded other + systems. Compared previous work similar another catalyst, selectivity is improved because lower tendency to coke formation catalyst.