Add to ORKGThe PEPT study of the riser of a CFB determines (i) the acceleration length and time, (ii) the upwards and downwards velocities; (ii) the population densities; (iii) the flow pattern at the riser bottom; and (iv) the existence of different flow regimes for associated operating conditions of gas flow rate (U) and solids circulation flux (G)
Standpipes are commonly used in circulating fluidised beds (CFB) to gravitationally transport solids...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The fluid and particle mechanics of circulating fluidised beds (CFBs) was studied in a series of th...
The PEPT study of the riser of a CFB determines (i) the acceleration length and time, (ii) the upwar...
The riser is the key-part of a circulating fluidized bed (CFB) and its hydrodynamics are determined ...
Riser operating modes are vital to designing a circulating fluidized bed (CFB) reactor for a require...
The riser of a Circulating Fluidised Bed (CFB) is the key-component where gas-solid or gas-catalytic...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
Gas velocity U-g and solids circulation rate G(s) are still being commonly treated as the only param...
AbstractCirculating Fluidised Beds (CFBs) are widely applied in the process industry, for mostly gas...
Single radioactive particle tracking was used to measure the overall solids residence time (and its ...
This work discusses operational regimes in CFB-furnaces by means of mapping the relation between flu...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
In this investigation a fiber-optic probe and an extraction solids probe are used to measure particl...
Statement of the Problem: Developing and disseminating a general and experimentally validated model ...
Standpipes are commonly used in circulating fluidised beds (CFB) to gravitationally transport solids...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The fluid and particle mechanics of circulating fluidised beds (CFBs) was studied in a series of th...
The PEPT study of the riser of a CFB determines (i) the acceleration length and time, (ii) the upwar...
The riser is the key-part of a circulating fluidized bed (CFB) and its hydrodynamics are determined ...
Riser operating modes are vital to designing a circulating fluidized bed (CFB) reactor for a require...
The riser of a Circulating Fluidised Bed (CFB) is the key-component where gas-solid or gas-catalytic...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
Gas velocity U-g and solids circulation rate G(s) are still being commonly treated as the only param...
AbstractCirculating Fluidised Beds (CFBs) are widely applied in the process industry, for mostly gas...
Single radioactive particle tracking was used to measure the overall solids residence time (and its ...
This work discusses operational regimes in CFB-furnaces by means of mapping the relation between flu...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
In this investigation a fiber-optic probe and an extraction solids probe are used to measure particl...
Statement of the Problem: Developing and disseminating a general and experimentally validated model ...
Standpipes are commonly used in circulating fluidised beds (CFB) to gravitationally transport solids...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
The fluid and particle mechanics of circulating fluidised beds (CFBs) was studied in a series of th...