| 545 - 545 |
Prefact to the special issue on mixing
Kresta S, Tanguy PA |
| 546 - 557 |
Laminar mixing in eccentric stirred tank systems
Alvarez MM, Arratia PE, Muzzio FJ |
| 558 - 565 |
Unconventional configuration studies to improve mixing times in stirred tanks
Ascanio G, Brito-Bazan M, Brito-De La Fuente E, Carreau PJ, Tanguy PA |
| 566 - 579 |
Experimental analysis of hydrodynamics induced by a Moritz HAS impeller in laminar and turbulent regimes
Escudie R, Line A, Kiener P |
| 580 - 590 |
Tracer dispersion in stirred tank reactors: Asymptotic properties and mixing characterization
Giona M, Paglianti A, Cerbelli S, Pintus S, Adrover A |
| 591 - 600 |
Investigation of flow patterns in continuous-flow stirred vessels by laser Doppler velocimetry
Mavros P, Xuereb C, Fort I, Bertrand J |
| 601 - 603 |
Power consumption in the turbulent regime for a coaxial mixer
Tanguy PA, Thibault F |
| 604 - 613 |
Morphology development in kenics static mixers (application of the extended mapping method)
Galaktionov OS, Anderson PD, Peters GWM, Meijer HEH |
| 614 - 621 |
The influence of viscosity ratio on mixing effectiveness in a two-fluid laminar motionless mixer
Ventresca AL, Cao Q, Prasad AK |
| 622 - 631 |
Using a new interfacial area transport equation to predict interfacial area in co-current jet mixers
Yarbro SL, Long RL |
| 632 - 637 |
On the applicability of the Grace curve in practical mixing operations
Stegeman YW, van de Vosse FN, Meijer HEH |
| 638 - 652 |
Flow generated by an aerated Rushton impeller: Two-phase PIV experiments and numerical simulations
Deen NG, Solberg T, Hjertager BH |
| 653 - 659 |
Operational characteristics of a new energy-saving impeller for gas-liquid mixing
Vlaev SD, Mavros P, Seichter P, Mann R |
| 660 - 664 |
Simple model to evaluate loading/flooding transition in aerated vessels stirred by Rushton disc turbines
Paglianti A |
| 665 - 673 |
Diagnosis of solid distribution in vessels stirred with multiple PBTs and comparison of two modelling approaches
Montante G, Pinelli D, Magelli F |
| 674 - 681 |
Concept for scale-up of solids suspension in stirred tanks
Kraume M, Zehner P |
| 682 - 687 |
Critical impeller speed for suspending solids in aerated agitation tanks
Zhu YG, Wu J |
| 688 - 694 |
Measuring volumetric phase fractions in a gas-solid-liquid stirred tank reactor using an impedance probe
Brunazzi E, Di Festa U, Galletti C, Merello C, Paglianti A, Pintus S |
| 695 - 709 |
CFD simulations of three-dimensional wall jets in a stirred tank
Bhattacharya S, Kresta SM |
| 710 - 720 |
On the comparison between probability density function models for CFD applications
Fissore D, Marchisio DL, Barresi AA |
| 721 - 726 |
CFD simulation of solids suspension in mixing vessels
Kee NCS, Tan RBH |
| 727 - 733 |
Pressure drop and mass transfer study in static mixers with gas continuous phase
Couvert A, Peculier MF, Laplanche A |
| 734 - 740 |
Flocculation monitoring: Focused beam reflectance measurement as a measurement tool
Blanco A, Fuente E, Negro C, Tijero J |
| 741 - 752 |
An aqueous phase equilibrium calculation algorithm
Makkuni A, Phoenix AV, Rohani S |
| 753 - 763 |
Determination of the optimum conditions for zinc extraction from ore containing sphalerite by HCl solutions
Ata ON, Yesilyurt M, Colak S, Bese AV |
| 764 - 768 |
The effect of adding phosphate on the size of extremely fine needle-like lepidocrocite particles prepared by oxidizing an aqueous suspension of ferrous hydroxide
Mihara N, Kawasaki H, Kumazawa H, Choi WS, Kwak JS, Choi HK |
| 769 - 773 |
Effect of technological factors on electrochemical hydrogenation of lignin
Zhang HN, Zhang XY, Xie DM, Liu DH, Li ZH |
| 774 - 779 |
Dynamic process modelling using a PCA-based output integrated recurrent neural network
Qian Y, Cheng HN, Li XX, Jiang YB |
| 780 - 781 |
Mona Lisa's gaze and smile - Myth or reality?
Tamir A |
