The influence of the fluidization velocities on products yield and catalyst residence time in industrial risers

H C Alvarezcastro,E M Matos,Milton Mori,W P Martignoni,R Ocone

Advanced Powder Technology（2015）

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摘要

•The hydrodynamics of the riser of a FCC process is modeled using ANSYS.•The cracking reactions are studied via a discrete lumping kinetics model.•A 12 lump model is used.•The methodology is checked against experimental data from the literature.

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关键词

CFD simulation,Gas particle flow,FCC,Riser,Catalytic cracking reaction,Petroleum refining

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