87 - 95 |
Power consumption, mixing time and homogenisation energy in dual-impeller agitated gas-liquid reactors Bouaifi M, Roustan M |
97 - 111 |
A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas-liquid reactors and bubble columns Bouaifi M, Hebrard G, Bastoul D, Roustan M |
113 - 119 |
Prediction of liquid velocity and gas hold-up in rectangular air-lift reactors of different scales Couvert A, Bastoul D, Roustan M, Line A, Chatellier P |
121 - 128 |
A hydrodynamic model for air-lift reactors Camarasa E, Carvalho E, Meleiro LAC, Maciel R, Domingues A, Wild G, Poncin S, Midoux N, Bouillard J |
129 - 133 |
Gas-liquid mass transfer in an airlift reactor - analytical solution and experimental confirmation Dhaouadi H, Poncin S, Midoux N, Wild G |
135 - 151 |
A simple method for regime identification and flow characterisation in bubble columns and airlift reactors Vial C, Poncin S, Wild G, Midoux N |
153 - 158 |
Comparative study of two cocurrent downflow three phase catalytic fixed bed reactors: application to the sulphur dioxide catalytic oxidation on active carbon particles Medeiros EBM, Petrissans M, Wehrer A, Zoulalian A |
159 - 166 |
Identification of axial dispersion coefficients by model method in gas/liquid/solid fluidised beds Giojelli B, Verdier C, Hihn JY, Beteau JF, Rozzi A |
167 - 174 |
Mass transfer in a 'droplets column' in presence of solid particles Muller N, Benadda B, Otterbein M |
175 - 185 |
Wet air oxidation solid catalysis analysis of fixed and sparged three-phase reactors Iliuta I, Larachi F |
187 - 194 |
Global and local mass transfer coefficients in waste water treatment process by computational fluid dynamics Cockx A, Do-Quang Z, Audic JM, Line A, Roustan M |