1 |
Kinetic Energy Transfer between First Proper Orthogonal Decomposition Modes in a Mixing Tank Gabelle JC, Morchain J, Line A Chemical Engineering & Technology, 40(5), 927, 2017 |
2 |
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 |
3 |
Coupling of Biokinetic and Population Balance Models to Account for Biological Heterogeneity in Bioreactors Morchain J, Gabelle JC, Cockx A AIChE Journal, 59(2), 369, 2013 |
4 |
Experimental determination of the shear rate in a stirred tank with a non-newtonian fluid: Carbopol Gabelle JC, Morchain J, Anne-Archard D, Augier F, Line A AIChE Journal, 59(6), 2251, 2013 |
5 |
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 Chemical Engineering Research & Design, 91(11), 2073, 2013 |
6 |
Impact of rheology on the mass transfer coefficient during the growth phase of Trichoderma reesei in stirred bioreactors Gabelle JC, Jourdier E, Licht RB, Ben Chaabane F, Henaut I, Morchain J, Augier F Chemical Engineering Science, 75, 408, 2012 |
7 |
EFFECT OF TANK SIZE ON k(L)a AND MIXING TIME IN AERATED STIRRED REACTORS WITH NON-NEWTONIAN FLUIDS Gabelle JC, Augier F, Carvalho A, Rousset R, Morchain J Canadian Journal of Chemical Engineering, 89(5), 1139, 2011 |