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|Type:||Artigo de periódico|
|Title:||Evaluation Of The Performance Of The Riser In The Fluid Catalytic Cracking Process|
H. C.; Matos
E. M.; Mori
|Abstract:||In a 3D model simulating in the riser of the fluid catalytic cracking (FCC) was studied feedstock conversion and yield products. Computational fluid dynamics (CFD) and Eulerian-Eulerian approach with a 12-lump model was used to predict the hydrodynamic and kinetic behavior, respectively. All the equations and conditions were solved using a solver Ansys CFX 14.0. The different operation variables and hydrodynamic effects of the riser are evaluated. Predictions from the model are shown and comparison with experimental data is presented; recommendations are drawn to establish the conditions to obtain higher product yields in the industrial process.|
|Subject:||Energy & Fuels|
|Editor:||TAYLOR & FRANCIS INC|
|Citation:||Evaluation Of The Performance Of The Riser In The Fluid Catalytic Cracking Process. Taylor & Francis Inc, v. 33, p. 579-587 2015.|
|Appears in Collections:||Unicamp - Artigos e Outros Documentos|
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