Dominique Bastoul

A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas–liquid reactors and bubble columns

Mounir Bouaifi, Gilles Hébrard, Dominique Bastoul et al. · Chemical Engineering and Processing - Process Intensification · 2001 · 363 citations

Stirred Gas–liquid Reactors, Bubble Dynamic, Engineering +8

Attempts, Successes, and Failures of Distance Learning in the Time of COVID-19

Nicolas Dietrich, Kalyani Kentheswaran, Aras Ahmadi et al. · Journal of Chemical Education · 2020 · 271 citations · Full text

Hydrodynamics of a three-phase fluidized bed—the inverse turbulent bed

M.P. Comte, Dominique Bastoul, Gilles Hébrard et al. · Chemical Engineering Science · 1997 · 66 citations

Engineering, Fluid Mechanics, Hydrodynamics +4

Bubble size and velocity measurement in gas—liquid systems: Application of fiber optic technique to pilot plant scale

Sh. Saberi, K. Shakourzadeh, Dominique Bastoul et al. · The Canadian Journal of Chemical Engineering · 1995 · 48 citations

Engineering, Measurement, Mm Plastic Fiber +16

Effect of solid characteristics on hydrodynamic and mass transfer in a fixed bed reactor operating in co-current gas–liquid up flow

J.G. Garcia Maldonado, Dominique Bastoul, S. Baig et al. · Chemical Engineering and Processing - Process Intensification · 2007 · 40 citations

Solid Characteristics, Fixed Bed Reactor, Fluid Mechanics +2