A detailed study of the residence time distribution (RTD) analysis of liquid phase has been performed in an external-loop airlift reactor of 20 L nominal volume, regarded as a global unit and discriminating its different sections (riser, gas–liquid separator and downcomer) using the tracer response technique. The reactor was used as an electrochemical reactor in order to carry out the electrocoagulation/electroflotation (EC/EF). The gas phase created in the riser is the hydrogen produced by water electrolysis.In order to use this reactor for a continuous EC/EF, hydrodynamic studies were carried out to control the operating conditions and to help modelling the electrocoagulation. Current density, position of the electrodes in the riser and t...
© 2016 This paper investigates the impact of surface tension gradient on liquid circulation time in ...
The local hydrodynamic properties in a multi-stage internal loop airlift reactor were investigated i...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
ABSTRACT: Mixing is one of the important unit operations in chemical and allied industries. Airlift ...
[[abstract]]©2003 Elsevier - The local hydrodynamic properties of the gas phase in an internal-loop ...
The present study summarizes the results of macro- and micro-mixing characteristics in an airlift in...
Gas hold-up and liquid circulation velocity measurements were made using a 167 dm3 external loop air...
The experimental and numerical study of two-phase gas–liquid flows in the external-loop airlift reac...
The residence time distribution (RTD) of a pilot plant scale packed bed reactor was studied in the ...
This paper investigates the impact of surface tension gradient on liquid circulation time in a draft...
This paper documents experiments and CFD simulations of the hydrodynamics of our two-phase (water, a...
The e!ect of the distributing plate ori"ce diameter, air#ow rate, solids loading and solids den...
© 2016 This paper investigates the impact of surface tension gradient on liquid circulation time in ...
The local hydrodynamic properties in a multi-stage internal loop airlift reactor were investigated i...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
International audienceA detailed study of the residence time distribution (RTD) analysis of liquid p...
ABSTRACT: Mixing is one of the important unit operations in chemical and allied industries. Airlift ...
[[abstract]]©2003 Elsevier - The local hydrodynamic properties of the gas phase in an internal-loop ...
The present study summarizes the results of macro- and micro-mixing characteristics in an airlift in...
Gas hold-up and liquid circulation velocity measurements were made using a 167 dm3 external loop air...
The experimental and numerical study of two-phase gas–liquid flows in the external-loop airlift reac...
The residence time distribution (RTD) of a pilot plant scale packed bed reactor was studied in the ...
This paper investigates the impact of surface tension gradient on liquid circulation time in a draft...
This paper documents experiments and CFD simulations of the hydrodynamics of our two-phase (water, a...
The e!ect of the distributing plate ori"ce diameter, air#ow rate, solids loading and solids den...
© 2016 This paper investigates the impact of surface tension gradient on liquid circulation time in ...
The local hydrodynamic properties in a multi-stage internal loop airlift reactor were investigated i...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...