In the fluid catalytic cracking (FCC) process, the riser is the most important equipment where the reaction taken place. In the riser operation, the feedstock is fed through injectors and mixed with catalyst and steam. A good design and localization of the injectors to ensure rapid evaporation of the feedstock and a good contact of the droplets with the catalyst is important to improve the process efficiency due to a better reagent distribution which ensures a good feedstock conversion and product yields. Hydrodynamic modelling, heat transfer and cracking reactions were studied in this paper using Computational Fluid Dynamic (CFD) in order to evaluate the effect of nozzles design and configuration on the homogeneity of the gas-solid distrib...
The hydrodynamic characteristic of the industrial riser used in the fluid catalytic cracking (FCC) p...
Risers are considered vital parts in Fluidized Catalytic Cracking (FCC) conversion units. It is insi...
A three-dimensional and two-phase flow model to predict the dynamic behavior of a fluid catalytic cr...
In the fluid catalytic cracking (FCC) process, the riser is the most important equipment where the r...
A three dimensional gas-solid reactive flow model based on the Eulerian-Eulerian approach was used t...
The feedstock injection zone is a key section for Fluid Catalytic Cracking riser reactor. A 3-D Comp...
The homogeneity of the regenerated catalyst flow upstream of the feed injectors at the bottom of an ...
The fluid catalytic cracking (FCC) process is at the heart of a modern refinery oriented toward maxi...
Design and scale-up of fluid catalytic cracking (FCC) riser is still largely empirical, owing to lim...
Design and scale-up of fluid catalytic cracking (FCC) riser is still largely empirical, owing to lim...
Feedstock conversion and yield products are studied through a 3D model simulating the main reactor o...
Fluid catalytic cracking (FCC) riser reactors have complex hydrodynamics, which depend not only on o...
Essential to today's modern refineries and the gasoline production process are fluidized catalytic c...
Feedstock injection zone is a key section for fluid catalytic cracking (FCC) riser reactor. In conve...
Risers are considered vital parts in Fluidized Catalytic Cracking (FCC) conversion units. It is insi...
The hydrodynamic characteristic of the industrial riser used in the fluid catalytic cracking (FCC) p...
Risers are considered vital parts in Fluidized Catalytic Cracking (FCC) conversion units. It is insi...
A three-dimensional and two-phase flow model to predict the dynamic behavior of a fluid catalytic cr...
In the fluid catalytic cracking (FCC) process, the riser is the most important equipment where the r...
A three dimensional gas-solid reactive flow model based on the Eulerian-Eulerian approach was used t...
The feedstock injection zone is a key section for Fluid Catalytic Cracking riser reactor. A 3-D Comp...
The homogeneity of the regenerated catalyst flow upstream of the feed injectors at the bottom of an ...
The fluid catalytic cracking (FCC) process is at the heart of a modern refinery oriented toward maxi...
Design and scale-up of fluid catalytic cracking (FCC) riser is still largely empirical, owing to lim...
Design and scale-up of fluid catalytic cracking (FCC) riser is still largely empirical, owing to lim...
Feedstock conversion and yield products are studied through a 3D model simulating the main reactor o...
Fluid catalytic cracking (FCC) riser reactors have complex hydrodynamics, which depend not only on o...
Essential to today's modern refineries and the gasoline production process are fluidized catalytic c...
Feedstock injection zone is a key section for fluid catalytic cracking (FCC) riser reactor. In conve...
Risers are considered vital parts in Fluidized Catalytic Cracking (FCC) conversion units. It is insi...
The hydrodynamic characteristic of the industrial riser used in the fluid catalytic cracking (FCC) p...
Risers are considered vital parts in Fluidized Catalytic Cracking (FCC) conversion units. It is insi...
A three-dimensional and two-phase flow model to predict the dynamic behavior of a fluid catalytic cr...