Add to ORKGThe characteristic of particle clusters was studied in a 2-D circulating fluidized bed riser by using a digital image system and optical fiber probes. A new parameter, cluster number fraction, was proposed to characterize the clusters. The results indicated the smaller and lighter particles have higher potential to aggregate, while the effects of particle sphericity were less significant than those of particle density and size
Experiments were performed with gas and solids flow in a 2.42m high circulating fluidized bed (CFB)....
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
A multi-fiber optical reflective probe was used to measure particle velocities and solids loading in...
Knowing the instantaneous flow structure is of great importance for the understanding of gas-particl...
The paper presents an analysis of measurement results on cluster properties in a two-dimensional lab...
The flow pattern in a circulating fluidized bed (CFB) is characterized by clusters of particles. The...
A circulating fluidized bed (CFB) built at FIU was used to study particle motion in the riser in ord...
High Density Circulating Fluidized Bed (HDCFB) reactors have found applications in a number of impor...
The fluid and particle mechanics of circulating fluidised beds (CFBs) was studied in a series of th...
The hydrodynamics of a circulating fluidized bed (CFB) risers is highly complex and is strongly infl...
In fluidized bed systems, particle properties (e.g., particle diameter, Reynolds number) are acknowl...
Micrographs in a 10-m high and 90-mm ID fluidized catalytic cracking (FCC) catalyst-air fast fluidiz...
An extensive experimental investigation of radial profiles of concentration -weighted particle veloc...
A common hydrodynamic feature in industrial scale circulating fluidized beds is the presence of clus...
The microscopic flow structure is studied systematically and comprehensively through a visualization...
Experiments were performed with gas and solids flow in a 2.42m high circulating fluidized bed (CFB)....
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
A multi-fiber optical reflective probe was used to measure particle velocities and solids loading in...
Knowing the instantaneous flow structure is of great importance for the understanding of gas-particl...
The paper presents an analysis of measurement results on cluster properties in a two-dimensional lab...
The flow pattern in a circulating fluidized bed (CFB) is characterized by clusters of particles. The...
A circulating fluidized bed (CFB) built at FIU was used to study particle motion in the riser in ord...
High Density Circulating Fluidized Bed (HDCFB) reactors have found applications in a number of impor...
The fluid and particle mechanics of circulating fluidised beds (CFBs) was studied in a series of th...
The hydrodynamics of a circulating fluidized bed (CFB) risers is highly complex and is strongly infl...
In fluidized bed systems, particle properties (e.g., particle diameter, Reynolds number) are acknowl...
Micrographs in a 10-m high and 90-mm ID fluidized catalytic cracking (FCC) catalyst-air fast fluidiz...
An extensive experimental investigation of radial profiles of concentration -weighted particle veloc...
A common hydrodynamic feature in industrial scale circulating fluidized beds is the presence of clus...
The microscopic flow structure is studied systematically and comprehensively through a visualization...
Experiments were performed with gas and solids flow in a 2.42m high circulating fluidized bed (CFB)....
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
A multi-fiber optical reflective probe was used to measure particle velocities and solids loading in...