In the present work the superficial gas velocities ( u G ) and the oscillatory conditions (frequency and amplitude) effects on the gas–liquid mass transfer process in a novel oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) are experimentally evaluated. The liquid-side mass transfer coefficient, k L , and the specific interfacial area, a, are studied individually. The specific interfacial area is obtained using the new automatic image analysis technique developed by Ferreira et al. (2012). The experimental results of volumetric liquid side mass transfer coefficient ( k L a ), Sauter mean diameter ( d 32 ) and gas holdup ( ε G ), and the calculated values of a and k L , are correlated with the superficial gas ve...
Gas–liquid mass transfer was investigated around Taylor bubbles flowing in a long, in-plane, spirals...
Process intensification demands the development of innovative and more sustainable process design a...
The present paper reports an original, predominantly experimental study of the mass transfer efficie...
n the present work, it is studied for the first time the use of an oscillatory flow reactor provided...
The mass transfer performance has been tested for gas-liquid flow in a new tubular reactor system, t...
The experimental study of gas dispersion in a vertical periodically, constricted, oscillatory meso-t...
In this paper, we present an experimental study on mass transfer of oxygen into water in an oscillat...
An extensive use in chemistry, biological and pharmaceutical laboratories is envisaged for a novel c...
In bioprocesses, the microorganisms growth is ruled by physical, chemical, and biological conditions...
This work aims at characterizing bubble size distribution and its control in a small-scale, constric...
In this paper attempts are made to address how bubble behaviour in a batch oscillatory ba'ed column ...
Hydrodynamics and mass transfer of gas–liquid flow are explored under ambient conditions in an Advan...
Hydrodynamics and mass transfer of gas–liquid flow are explored under ambient conditions in an Advan...
A novel continuous small-scale reactor based on the oscillatory flow technology (Harvey et al 2001)...
Oxygen gas-liquid mass transfer coefficient was measured in a gas-induced pulsating flow bubble colu...
Gas–liquid mass transfer was investigated around Taylor bubbles flowing in a long, in-plane, spirals...
Process intensification demands the development of innovative and more sustainable process design a...
The present paper reports an original, predominantly experimental study of the mass transfer efficie...
n the present work, it is studied for the first time the use of an oscillatory flow reactor provided...
The mass transfer performance has been tested for gas-liquid flow in a new tubular reactor system, t...
The experimental study of gas dispersion in a vertical periodically, constricted, oscillatory meso-t...
In this paper, we present an experimental study on mass transfer of oxygen into water in an oscillat...
An extensive use in chemistry, biological and pharmaceutical laboratories is envisaged for a novel c...
In bioprocesses, the microorganisms growth is ruled by physical, chemical, and biological conditions...
This work aims at characterizing bubble size distribution and its control in a small-scale, constric...
In this paper attempts are made to address how bubble behaviour in a batch oscillatory ba'ed column ...
Hydrodynamics and mass transfer of gas–liquid flow are explored under ambient conditions in an Advan...
Hydrodynamics and mass transfer of gas–liquid flow are explored under ambient conditions in an Advan...
A novel continuous small-scale reactor based on the oscillatory flow technology (Harvey et al 2001)...
Oxygen gas-liquid mass transfer coefficient was measured in a gas-induced pulsating flow bubble colu...
Gas–liquid mass transfer was investigated around Taylor bubbles flowing in a long, in-plane, spirals...
Process intensification demands the development of innovative and more sustainable process design a...
The present paper reports an original, predominantly experimental study of the mass transfer efficie...