3155 - 3156 |
Special Issue - Jean-Claude Charpentier - Festschrift Curien H, Sanchez V, Wild G |
3157 - 3183 |
Coherent flow structures in bubble column reactors Joshi JB, Vitankar VS, Kulkarni AA, Dhotre MT, Ekambara K |
3185 - 3215 |
Measuring techniques in gas-liquid and gas-liquid-solid reactors Boyer C, Duquenne AM, Wild G |
3217 - 3223 |
The generalized Leveque equation and its practical use for the prediction of heat and mass transfer rates from pressure drop Martin H |
3225 - 3234 |
Non-Newtonian fluidisation of spherical particles Ciceron D, Comiti J, Chhabra RP, Renaud M |
3235 - 3250 |
A low Reynolds number k-epsilon model for the prediction of flow pattern and pressure drop in bubble column reactors Vitankar VS, Dhotre MT, Joshi JB |
3251 - 3267 |
A model for turbulent binary breakup of dispersed fluid particles Hagesaether L, Jakobsen HA, Svendsen HF |
3269 - 3281 |
On the second-order moment turbulence model for simulating a bubble column Zhou LX, Yang M, Lian CY, Fan LS, Lee DJ |
3283 - 3297 |
Effect of bubble deformation on stability and mixing in bubble columns Leon-Becerril E, Cockx A, Line A |
3299 - 3306 |
Hydrodynamics and volumetric gas-liquid mass transfer coefficient of a stirred vessel equipped with a gas-inducing impeller Poncin S, Nguyen C, Midoux N, Breysse J |
3307 - 3324 |
Mass transfer characteristics in a large-scale slurry bubble column reactor with organic liquid mixtures Behkish A, Men ZW, Inga JR, Morsi BI |
3325 - 3333 |
Hydrodynamics and mass transfer in gas-liquid flow through static mixers Heyouni A, Roustan M, Do-Quang Z |
3335 - 3345 |
Transient state techniques for mass transfer characterization of a gas-liquid packed column Perrin S, Chaudourne S, Jallut C, Lieto J |
3347 - 3358 |
Bubble flow mechanisms in trickle beds - an experimental study using image processing Benkrid K, Rode S, Pons MN, Pitiot P, Midoux N |
3359 - 3371 |
New mechanistic film model for pressure drop and liquid holdup in trickle flow reactors Iliuta I, Grandjean BPA, Larachi F |
3373 - 3385 |
Challenges for the periodic operation of trickle-bed catalytic reactors Silveston PL, Hanika J |
3387 - 3399 |
Liquid-induced pulsing flow in trickle-bed reactors Boelhouwer JG, Piepers HW, Drinkenburg AAH |
3401 - 3405 |
Partial wetting in porous catalysts: wettability and wetting efficiency Khanna R, Nigam KDP |
3407 - 3413 |
Influence of hydrodynamic parameters on performance of a multiphase fixed-bed reactor under phase transition Cheng ZM, Yuan WK |
3415 - 3426 |
Degassing of molten polymers Gestring I, Mewes D |
3427 - 3438 |
A systemic approach for the characterization of ion exchange in the altered layer of a non-radioactive nuclear glass Blet V, Rudloff D, Berne P, Jollivet P, Schweich D |
3439 - 3451 |
Modelling the catalytic steam reforming of methane: discrimination between kinetic expressions using sequentially designed experiments Jarosch K, El Solh T, de Lasa HI |
3453 - 3460 |
Palladium supported on filamentous active carbon as effective catalyst for liquid-phase hydrogenation of 2-butyne-1,4-diol to 2-butene-1, 4-diol Joannet E, Horny C, Kiwi-Minsker L, Renken A |
3461 - 3477 |
Polymerization of liquid propylene with a 4th generation Ziegler-Natta catalyst - influence of temperature, hydrogen and monomer concentration and prepolymerization method on polymerization kinetics Pater JTM, Weickert G, van Swaaij WPM |
3479 - 3484 |
Mass transfer with chemical reaction: the slow reaction regime revisited Roizard C, Wild G |