In this investigation a fiber-optic probe and an extraction solids probe are used to measure particle velocities and solids flux values. These are subsequently used to determine the local solids fractions as a function of radial position in a cold flow circulating fluidized bed (CFCFB) in operation at the National Energy Technology Laboratory (NETL). Measurements were taken under several separate operating conditions ranging from dilute up-flow to core-annular flow to fast fluidization using nominal 800 micron cork particles. The solids properties and test operating conditions were chosen particularly to provide dynamic similitude between the test data and the operation of a high temperature, high pressure gasifier. The data from these cond...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
AbstractCirculating Fluidised Beds (CFBs) are widely applied in the process industry, for mostly gas...
Almost all previous circulating fluidized bed hydrodynamic data reported in the literature have bee...
A multi-fiber optical reflective probe was used to measure particle velocities and solids loading in...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
This work applies optical probe and particle image velocimetry (PIV) measurements for determining th...
This work applies optical probe and particle image velocimetry (PIV) measurements for determining th...
High Density Circulating Fluidized Bed (HDCFB) reactors have found applications in a number of impor...
Experiments were performed with gas and solids flow in a 2.42m high circulating fluidized bed (CFB)....
This paper presents an experimental study with the aim to understand the relation between the flow c...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
An extensive experimental investigation of radial profiles of concentration -weighted particle veloc...
Solids volume fraction and particle velocity profiles were measured with a fiber optical probe in a ...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cr...
The PEPT study of the riser of a CFB determines (i) the acceleration length and time, (ii) the upwar...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
AbstractCirculating Fluidised Beds (CFBs) are widely applied in the process industry, for mostly gas...
Almost all previous circulating fluidized bed hydrodynamic data reported in the literature have bee...
A multi-fiber optical reflective probe was used to measure particle velocities and solids loading in...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cra...
This work applies optical probe and particle image velocimetry (PIV) measurements for determining th...
This work applies optical probe and particle image velocimetry (PIV) measurements for determining th...
High Density Circulating Fluidized Bed (HDCFB) reactors have found applications in a number of impor...
Experiments were performed with gas and solids flow in a 2.42m high circulating fluidized bed (CFB)....
This paper presents an experimental study with the aim to understand the relation between the flow c...
Fluid catalytic cracking risers operate at solids fluxes of 400 to 1400 kg/s.m2 and gas velocities o...
An extensive experimental investigation of radial profiles of concentration -weighted particle veloc...
Solids volume fraction and particle velocity profiles were measured with a fiber optical probe in a ...
This study was directed to the hydrodynamics of vertical risers, such as those used in catalytic cr...
The PEPT study of the riser of a CFB determines (i) the acceleration length and time, (ii) the upwar...
Flow regime study was conducted in a 0.3 m diameter, 15.5 m height circulating fluidized bed (CFB) r...
AbstractCirculating Fluidised Beds (CFBs) are widely applied in the process industry, for mostly gas...
Almost all previous circulating fluidized bed hydrodynamic data reported in the literature have bee...