| 1 |
Bubble size distribution in aerated stirred tanks: Quantifying the effect of impeller-stator design
Mesa D, Brito-Parada PR
Chemical Engineering Research & Design, 160, 356, 2020 |
| 2 |
Influence of Spacing of Multiple Impellers on Power Input in an Industrial-Scale Aerated Stirred Tank Reactor
Fitschen J, Maly M, Rosseburg A, Wutz J, Wucherpfennig T, Schluter M
Chemie Ingenieur Technik, 91(12), 1794, 2019 |
| 3 |
Multiphase Stirred Tank Bioreactors - New Geometrical Concepts and Scale-up Approaches
Bohm L, Hohl L, Bliatsiou C, Kraume M
Chemie Ingenieur Technik, 91(12), 1724, 2019 |
| 4 |
A Coupled Population Balance Model and CFD Approach for the Simulation of Mixing Issues in Lab-Scale and Industrial Bioreactors
Morchain J, Gabelle JC, Cockx A
AIChE Journal, 60(1), 27, 2014 |
| 5 |
A consistent dimensional analysis of gas-liquid mass transfer in an aerated stirred tank containing purely viscous fluids with shear-thinning properties
Hassan R, Loubiere K, Legrand J, Delaplace G
Chemical Engineering Journal, 184, 42, 2012 |
| 6 |
Onset of gas induction and power consumption in an agitated tank having shortened narrower baffles
Hsu YC, Huang CJ, Yen WH, Peng RY
Journal of Chemical Technology and Biotechnology, 71(3), 187, 1998 |
| 7 |
Effects of Geometrical Factors on Liquid-Mixing in a Gas-Induced Agitated Tank
Hsu YC, Huang KF
Journal of Chemical Technology and Biotechnology, 68(2), 222, 1997 |
| 8 |
Onset of Gas Self-Induction and Power-Consumption After Gas Induction in an Agitated Tank
Hsu YC, Chang HC
Journal of Chemical Technology and Biotechnology, 64(2), 137, 1995 |
