2099 - 2099 |
Innovative studies in industrial mixing processes Tanguy PA, Bertrand J, Xuereb C |
2101 - 2113 |
Emulsion processing - from single-drop deformation to design of complex processes and products Windhab EJ, Dressler M, Feigl K, Fischer P, Megias-Alguacil D |
2115 - 2125 |
Scale-up effects in coalescing dispersions - comparison of liquid-liquid systems differing in interface mobility Podgorska W |
2127 - 2134 |
More efficient preparation of parenteral emulsions or how to improve a pharmaceutical recipe by formulation engineering Cuellar I, Bullon J, Forgarini AM, Cardenas A, Briceno MI |
2135 - 2153 |
Model reduction for prediction of silver halide precipitation Kresta S, Anthieren G, Parsiegla K |
2155 - 2165 |
Effects of convection, feed-separation and macro-mixing on particle size distributions for double-jet semi-batch precipitation in a stirred vessel Kagoshima M, Mann R |
2167 - 2178 |
Effects of fluid motion and mixing on particle agglomeration and coating during precipitation Baldyga J, Jasinska M |
2179 - 2192 |
Flocculation related to local hydrodynamics in a Taylor-Couette reactor and in a jar Coufort C, Bouyer D, Line A |
2193 - 2201 |
Particle formation by turbulent mixing with supercritical antisolvent Henczka M, Baldyga J, Shekunov BY |
2203 - 2214 |
Numerical modelling of gas-liquid flow in stirred tanks Lane GL, Schwarz MP, Evans GM |
2215 - 2229 |
Gas-liquid flow generated by a Rushton turbine in stirred vessel: CARPT/CT measurements and CFD simulations Khopkar AR, Rammohan AR, Ranade VV, Dudukovic MP |
2231 - 2238 |
Inverted hollow spinning cone as a device for controlling foam and hold-up in pilot scale gassed agitated fermentation vessels Stocks SM, Cooke M, Heggs PJ |
2239 - 2252 |
A phenomenological model for the gas phase flow in high-aspect-ratio stirred vessels: the role of small bubbles in non-coalescent and moderately viscous liquids Pinelli D |
2253 - 2272 |
Comparison of mixing in two industrial gas-liquid reactors using CFD simulations Gentric C, Mignon D, Bousquet J, Tanguy PA |
2273 - 2282 |
Mixing characteristics of industrial flotation equipment Yianatos JB, Bergh LG, Diaz F, Rodriguez J |
2283 - 2292 |
Suspension of buoyant particles in a three phase stirred tank Bao YY, Hao ZG, Gao ZM, Shi LT, Smith JM |
2293 - 2302 |
Determination of mixing time and degree of homogeneity in stirred vessels with large eddy simulation Yeoh SL, Papadakis G, Yianneskis M |
2303 - 2316 |
Large-eddy simulation of turbulent flow in an unbaffled stirred tank driven by a Rushton turbine Alcamo R, Micale G, Grisafi F, Brucato A, Ciofalo M |
2317 - 2331 |
Observations on the significance of instabilities turbulence and intermittent motions on fluid mixing processes in stirred reactors Galletti C, Paglianti A, Yianneskis M |
2333 - 2339 |
Intensifying micromixing in a semi-batch reactor using a Rushton turbine Assirelli M, Bujalski W, Eaglesham A, Nienow AW |
2341 - 2354 |
Hydrodynamic effects on mixing and competitive reactions in laboratory reactors Akiti O, Yeboah A, Bai G, Armenante PM |
2355 - 2368 |
Comparative study of different mixing strategies in small high throughput experimentation reactors Hall JE, Barigou A, Simmons MJH, Stitt EH |
2369 - 2380 |
Stirring of a liquid in a stirred tank with an eccentrically located impeller Karcz J, Cudak M, Szoplik J |
2381 - 2398 |
Study of mixing and chemical reaction in RIM Santos RJ, Teixeira AM, Lopes JCB |
2399 - 2408 |
Suspension yield stress and the dynamic response of agitated pulp chests Ein-Mozaffari F, Bennington CPJ, Dumont GA |
2409 - 2418 |
Mixing rheometry for studying the manufacture of lubricating greases Franco JM, Delgado MA, Valencia C, Sanchez MC, Gallegos C |
2419 - 2426 |
Radical polymerization in supercritical carbon dioxide - use of supercritical carbon dioxide as a mixing assistant Nishi K, Morikawa Y, Misumi R, Kaminoyama M |
2427 - 2437 |
CFD simulations and experimental validation of homogenisation curves and mixing time in stirred Newtonian and pseudoplastic liquids Montante G, Mostek M, Jahoda M, Magelli F |
2439 - 2448 |
Heat transfer and power consumption for ribbon impellers. Mixing efficiency Niedzielska A, Kuncewicz C |
2449 - 2457 |
Experimental visualization of mixing pathologies in laminar stirred tank bioreactors Alvarez MM, Guzman A, Elias M |
2459 - 2467 |
In situ assembly using a continuous chaotic advection blending process of electrically conducting networks in carbon black-thermoplastic extrusions Chougule VA, Zumbrunnen DA |
2469 - 2478 |
LIF measurements of blending in static mixers in the turbulent and transitional flow regimes Wadley R, Dawson MK |
2479 - 2501 |
Micromixers - a review on passive and active mixing principles Hessel V, Lowe H, Schonfeld F |
2503 - 2516 |
Design of micromixers using CFD modelling Aubin J, Fletcher DF, Xuereb C |
2517 - 2531 |
DEM-based models for the mixing of granular materials Bertrand F, Leclaire LA, Levecque G |