Local mass transfer studies have been carried out in an external loop airlift reactor and indi cated the existence of significant non-uniformities in aeration capacity in the various sec tions of the reactor. The traditional assumption of a single well mixed unit with a single kL a value for external loop airlift reactors was found to be poor and cannot represent ade quately the reactor as a whole. The liquid head in the gas/liquid separator was found to have a significant negative effect on the local mass transfer coefficient kL a. Visualization of flow patterns showed the existence of strong vortices in the riser and downcomer which contributed to a reduction in local aeration capacity. Mass transfer experiments in an aerat ed tank showed...
Liquid-side mass-transfer coefficients (kLa) were measured in surface aerators and self-inducing-typ...
Determinations of volumetric mass transfer coefficient were conducted in a three-phase internal-loop...
The effect of superficial gas velocity within the range 0.01-0.164 m/s on gas holdup (overall, riser...
Abstract: Gas hold-up and oxygen transfer have been investigated in two geo metrically similar exter...
In airlift reactors transport phenomena are achieved by pneumatic agitation and circulation occurs i...
Abstract- In airlift reactors transport phenomena are achieved by pneumatic agitation and circulatio...
A pilot external airlift loop reactor (EALR) integrating mixing and separation was first proposed by...
The hydrodynamics and mass transfer characteristics of a 0.7 m3 external loop airlift reactor were e...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
Gas hold-up and liquid circulation velocity measurements were made using a 167 dm3 external loop air...
International audienceOne-dimensional modelling of global hydrodynamics and mass transfer is develop...
Experimental studies on the effects of surface active agents on the hydrodynamics and mass-transfer ...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
Hydrodynamics is an important issue for the design and development of three phase internal air lift...
The gas–liquid hydrodynamics and mass transfer were studied in a concentric tube internal jet-loop a...
Liquid-side mass-transfer coefficients (kLa) were measured in surface aerators and self-inducing-typ...
Determinations of volumetric mass transfer coefficient were conducted in a three-phase internal-loop...
The effect of superficial gas velocity within the range 0.01-0.164 m/s on gas holdup (overall, riser...
Abstract: Gas hold-up and oxygen transfer have been investigated in two geo metrically similar exter...
In airlift reactors transport phenomena are achieved by pneumatic agitation and circulation occurs i...
Abstract- In airlift reactors transport phenomena are achieved by pneumatic agitation and circulatio...
A pilot external airlift loop reactor (EALR) integrating mixing and separation was first proposed by...
The hydrodynamics and mass transfer characteristics of a 0.7 m3 external loop airlift reactor were e...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
Gas hold-up and liquid circulation velocity measurements were made using a 167 dm3 external loop air...
International audienceOne-dimensional modelling of global hydrodynamics and mass transfer is develop...
Experimental studies on the effects of surface active agents on the hydrodynamics and mass-transfer ...
In an internal loop airlift reactor of 55L working volume, the gas-liquid volumetric oxygen mass tra...
Hydrodynamics is an important issue for the design and development of three phase internal air lift...
The gas–liquid hydrodynamics and mass transfer were studied in a concentric tube internal jet-loop a...
Liquid-side mass-transfer coefficients (kLa) were measured in surface aerators and self-inducing-typ...
Determinations of volumetric mass transfer coefficient were conducted in a three-phase internal-loop...
The effect of superficial gas velocity within the range 0.01-0.164 m/s on gas holdup (overall, riser...