May 1-5, 2011
Platinum and tin deposited on mixed support of SAPO-34 and alumina oxide at certain proportion constitute a new catalyst of good catalytic performance. The catalyst was tested in a Gas-Solid-Solid fluidized bed reactor. Cold model experiment was carried on to obtain fluidization curves and characteristic velocities. Reaction results in the GSS-FBR showed that propylene yield was improved by 5 % compared with that in micro fixed bed reactor.
Yue Chu, Tongwei Wu, Yunxin Li, Zeeshan Nawaz, Yao Wang, and Fei Wei, "Studies on Propane Dehydrogenation to Propylene in a Gas-Solid-Sold Fluidized Bed Reactor" in "10th International Conference on Circulating Fluidized Beds and Fluidization Technology - CFB-10", T. Knowlton, PSRI Eds, ECI Symposium Series, (2013). http://dc.engconfintl.org/cfb10/22