2071 - 2072 |
14th European Conference on Mixing Baldyga J, Pohorecki R |
2073 - 2083 |
On POD analysis of PIV measurements applied to mixing in a stirred vessel with a shear thinning fluid Line A, Gabelle JC, Morchain J, Anne-Archard D, Augier F |
2084 - 2097 |
Mixing time and kinetic energy measurements in a shaken cylindrical bioreactor Rodriguez G, Weheliye W, Anderlei T, Micheletti M, Yianneskis M, Ducci A |
2098 - 2105 |
Development of method for estimating drop diameter in the manufacturing process of functional O/W microcapsules Kanaya K, Akao S, Misumi R, Nishi K, Kaminoyama M |
2106 - 2113 |
Development of positron emission particle tracking for studying laminar mixing in Kenics static mixer Rafiee M, Simmons MJH, Ingram A, Stitt EH |
2114 - 2121 |
Numerical simulation of liquid-liquid turbulent flow in a stirred tank with an explicit algebraic stress model Feng X, Li XY, Cheng JC, Yang C, Mao ZS |
2122 - 2133 |
Dispersion of water into oil in a rotor-stator mixer. Part 1: Drop breakup in dilute systems Rueger PE, Calabrese RV |
2134 - 2141 |
Dispersion of water into oil in a rotor-stator mixer. Part 2: Effect of phase fraction Rueger PE, Calabrese RV |
2142 - 2155 |
Drop breakage and coalescence in the toluene/water dispersions with dissolved surface active polymers PVA 88% and 98% Bak A, Podgorska W |
2156 - 2168 |
The effect of scale and interfacial tension on liquid-liquid dispersion in in-line SiIverson rotor-stator mixers Hall S, Pacek AW, Kowalski AJ, Cooke M, Rothman D |
2169 - 2178 |
Investigations of mass transfer with chemical reactions in two-phase liquid-liquid systems Jasinska M, Baldyga J, Cooke M, Kowalski A |
2179 - 2189 |
Investigation of turbulence modulation in solid-liquid suspensions using parallel competing reactions as probes for micro-mixing efficiency Unadkat H, Nagy ZK, Rielly CD |
2190 - 2197 |
Advanced impeller design: Anti-ragging impeller, ARI2 Higbee RW, Giacomelli JJ, Wyczalkowski WR |
2198 - 2208 |
Fluid-dynamics characteristics of a vortex-ingesting stirred tank for biohydrogen production Montante G, Magelli F, Paglianti A |
2209 - 2224 |
The confined impeller stirred tank (CIST): A bench scale testing device for specification of local mixing conditions required in large scale vessels Machado MB, Kresta SM |
2225 - 2234 |
Mixing and recirculation characteristics of gas-liquid Taylor flow in microreactors Abadie T, Xuereb C, Legendre D, Aubin J |
2235 - 2242 |
Liquid-liquid mixing using micro-fluidised beds Doroodchi E, Sathe M, Evans G, Moghtaderi B |
2243 - 2249 |
Incorporation of nanoparticle clusters into a liquid using a proprietary design mixer, Ytron Y Jet Ozcan-Taskin NG |
2250 - 2258 |
The NETmix reactor: Pressure drop measurements and 3D CFD modeling Fonte CM, Leblebici ME, Dias MM, Lopes JCB |
2259 - 2264 |
Process intensification of continuous starch hydrolysis with a Couette-Taylor flow reactor Masuda H, Horie T, Hubacz R, Ohmura N |
2265 - 2274 |
Scale-down studies for assessing the impact of different stress parameters on growth and product quality during animal cell culture Nienow AW, Scott WH, Hewitt CJ, Thomas CR, Lewis G, Amanullah A, Kiss R, Meier SJ |
2275 - 2290 |
Identification of nucleation rate parameters with MD and validation of the CFD model for polymer particle precipitation Di Pasquale N, Marchisio DL, Carbone P, Barresi AA |