Magnetic resonance (MR) imaging techniques have been used to study gas phase dynamics during co-current up-flow in a column of inner diameter 43 mm, packed with spherical non-porous elements of diameters of 1.8, 3 and 5 mm. MR measurements of gas hold-up, bubble-size distribution, and bubble-rise velocities were made as a function of flow rate and packing size. Gas and liquid flow rates were studied in the range of 20–250 cm3 s−1 and 0–200 cm3 min−1, respectively. The gas hold-up within the beds was found to increase with gas flow rate, while decreasing with increasing packing size and to a lesser extent with increasing liquid flow rate. The gas hold-up can be separated into a dynamic gas hold-up, only weakly dependent on packing size and a...
Packed bed reactors are one of the central processing units of chemical and petrochemical industries...
Snapshots of particle concentration and velocity fields in bubbling gas–solid fluidized beds were ac...
In this study, the hydrodynamic, i.e. flow regime identification, line average liquid holdup, and th...
Magnetic resonance imaging (MRI) was used to measure directly gas velocity and gas velocity distribu...
Relative flow between granular material and gas can create phenomena in which particles behave like ...
This thesis describes the first application of ultra-fast magnetic resonance imaging (MRI) towards t...
Snapshots of particle concentration and velocity fields in bubbling gas–solid fluidized beds were ac...
© 2017 Elsevier Ltd A narrow column, gas-solid fluidized bed was studied using ultrashort echo time ...
Magnetic resonance imaging is used to generate snapshots of particle concentration and velocity fiel...
Real-time magnetic resonance imaging was used to study the different flow regimes which occur in a f...
Radial variation of the gas hold-up was investigated in 0.385 m ID bubble column using gamma ray tom...
This paper presents an experimental analysis of the influence of the liquid rheology on the gas flow...
We used a permanent-magnet magnetic resonance imaging (MRI) system to estimate the integral, spatial...
The aim of this study was to develop a practically usable model to describe the influence of increas...
Catalytic packed bed reactors are widely used in industrial processes. The particle packing structur...
Packed bed reactors are one of the central processing units of chemical and petrochemical industries...
Snapshots of particle concentration and velocity fields in bubbling gas–solid fluidized beds were ac...
In this study, the hydrodynamic, i.e. flow regime identification, line average liquid holdup, and th...
Magnetic resonance imaging (MRI) was used to measure directly gas velocity and gas velocity distribu...
Relative flow between granular material and gas can create phenomena in which particles behave like ...
This thesis describes the first application of ultra-fast magnetic resonance imaging (MRI) towards t...
Snapshots of particle concentration and velocity fields in bubbling gas–solid fluidized beds were ac...
© 2017 Elsevier Ltd A narrow column, gas-solid fluidized bed was studied using ultrashort echo time ...
Magnetic resonance imaging is used to generate snapshots of particle concentration and velocity fiel...
Real-time magnetic resonance imaging was used to study the different flow regimes which occur in a f...
Radial variation of the gas hold-up was investigated in 0.385 m ID bubble column using gamma ray tom...
This paper presents an experimental analysis of the influence of the liquid rheology on the gas flow...
We used a permanent-magnet magnetic resonance imaging (MRI) system to estimate the integral, spatial...
The aim of this study was to develop a practically usable model to describe the influence of increas...
Catalytic packed bed reactors are widely used in industrial processes. The particle packing structur...
Packed bed reactors are one of the central processing units of chemical and petrochemical industries...
Snapshots of particle concentration and velocity fields in bubbling gas–solid fluidized beds were ac...
In this study, the hydrodynamic, i.e. flow regime identification, line average liquid holdup, and th...