Add to ORKGThis study consists in characterizing the solid phase behavior in the dilute region of a circulating fluidized bed riser (CFB) for the turbulent regime (i.e. for superficial gas velocities U
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cr...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The hydrodynamics of a circulating fluidized bed (CFB) risers is highly complex and is strongly infl...
International audienceThe behavior of the solid phase in the upper zone of a circulating fluidized b...
International audienceThe solid phase behavior is studied in the upper zone of a circulating fluidiz...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
The hydrodynamics behavior of a bench-scale circulating fluidized bed (CFB) system has been analyzed...
Characterization by means of Kolmogorov entropy shows that the dynamics of the bottom bed in small s...
Almost all previous circulating fluidized bed hydrodynamic data reported in the literature have bee...
Many commercial fluidized bed processes (e.g. catalytic and gas-solid reactions, drying) operate in ...
Characterization by means of Kolmogorov entropy shows that the dynamics of the bottom bed in small s...
Simple and rapid dynamic tests were used to evaluate fluid dynamic behavior of granular materials in...
Flow behavior and flow regime transitions were determined in a circulating fluidized bed riser (0.20...
The radial profiles of particle concentration in circulating fluidized bed (CFB) risers experience a...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cr...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The hydrodynamics of a circulating fluidized bed (CFB) risers is highly complex and is strongly infl...
International audienceThe behavior of the solid phase in the upper zone of a circulating fluidized b...
International audienceThe solid phase behavior is studied in the upper zone of a circulating fluidiz...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
The hydrodynamics behavior of a bench-scale circulating fluidized bed (CFB) system has been analyzed...
Characterization by means of Kolmogorov entropy shows that the dynamics of the bottom bed in small s...
Almost all previous circulating fluidized bed hydrodynamic data reported in the literature have bee...
Many commercial fluidized bed processes (e.g. catalytic and gas-solid reactions, drying) operate in ...
Characterization by means of Kolmogorov entropy shows that the dynamics of the bottom bed in small s...
Simple and rapid dynamic tests were used to evaluate fluid dynamic behavior of granular materials in...
Flow behavior and flow regime transitions were determined in a circulating fluidized bed riser (0.20...
The radial profiles of particle concentration in circulating fluidized bed (CFB) risers experience a...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cr...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The hydrodynamics of a circulating fluidized bed (CFB) risers is highly complex and is strongly infl...