Catalytic Fast Pyrolysis of Biomass in a Fluidized Bed with Fresh and Spent Fluidized Catalytic Cracking (FCC) Catalysts

2009 ◽  
Vol 23 (12) ◽  
pp. 6199-6206 ◽  
Author(s):  
Huiyan Zhang ◽  
Rui Xiao ◽  
Denghui Wang ◽  
Zhaoping Zhong ◽  
Min Song ◽  
...  
2015 ◽  
Vol 8 (3) ◽  
pp. 1263-1274 ◽  
Author(s):  
Zhi-bo Zhang ◽  
Qiang Lu ◽  
Xiao-ning Ye ◽  
Ti-peng Wang ◽  
Xian-hua Wang ◽  
...  

2009 ◽  
Vol 52 (3) ◽  
pp. 241-252 ◽  
Author(s):  
Torren R. Carlson ◽  
Geoffrey A. Tompsett ◽  
William C. Conner ◽  
George W. Huber

2020 ◽  
Vol 602 ◽  
pp. 117727 ◽  
Author(s):  
Lei Yu ◽  
Azeem Farinmade ◽  
Oluwole Ajumobi ◽  
Yang Su ◽  
Vijay T. John ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (2) ◽  
pp. 293 ◽  
Author(s):  
Sung Kim ◽  
Chae Yeo ◽  
Do Lee

Effect of fines content (weight % of particles with diameter less than 45 μm) on bed fluidity was determined to get a base for good fluidization quality in the fluid catalytic cracking (FCC) unit. The fines content in equilibrium FCC catalysts (Ecat) from commercial units were controlled by adding or removing the fines to simulate commercial situation. To get the fluidity values (Umb/Umf) of seven different FCC catalysts (2 Ecats and 5 fresh catalysts) and their mixture, minimum fluidization velocity (Umf) and minimum bubbling velocity (Umb) were measured in a fluidized bed reactor (0.05 m ID). The fluidity decreased with loss of fines content and increased with increments of makeup of fresh catalysts or additive with the controlled fines content. The fluidities of catalysts increase with increases of normalized particle diameter variation by the fines addition. The obtained fluidities have been correlated with the fines contents and the catalyst and gas properties. The proposed correlation could guide to keep good catalyst fluidity in the FCC unit.


1992 ◽  
Vol 38 (12) ◽  
pp. 2621-2629 ◽  
Author(s):  
S. Rapagna ◽  
E. Tempesti ◽  
P. U. Foscolo ◽  
E. Parodi

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