Serveur d'exploration sur le LRGP - Exploration (Accueil)

Index « Teeft.i » - entrée « Flow regime »
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List of bibliographic references indexed by Flow regime

Number of relevant bibliographic references: 23.
[0-20] [0 - 20][0 - 23][20-22][20-40]
Ident.Authors (with country if any)Title
000B44 (2011) Gabriel Wild [France] ; Souhila Poncin [France] ; Huai-Zhi Li [France] ; Eric Olmos [France]Some Aspects of the Hydrodynamics of Bubble Columns
001907 (2001) Horst-Michael Prasser ; Jochen Zschau ; Dieter Peters ; Gerd Pietzsch ; Wolfgang Taubert ; Manuel TrepteFast Wire‐Mesh Sensor for Two‐Phase Flow Visualisation with 10 000 Frames per Second
001930 (2001) Dolores Kukanja [Slovénie] ; Matjaž Krajnc [Slovénie] ; Janvit Golob [Slovénie]Comparison between Acrylic‐Polyurethane Hybrid Emulsions and Physical Blends
002183 (1997) M. A. Latifi [France] ; A. Naderifar [France] ; Noël Midoux [France]Experimental investigation of the liquid/solid mass transfer at the wall of a trickle-bed reactor—influence of Schmidt number
002421 (1996) A. S. Lamine [France] ; L. Gerth [France] ; H. Le Gall [France] ; G. Wild [France]Heat transfer in a packed bed reactor with cocurrent downflow of a gas and a liquid
002550 (1995) M. A. Latifi [France] ; A. Naderifar [France] ; Noël Midoux [France]Stochastic analysis of the local velocity gradient in a trickle-bed reactor
002698 (1994) J. Mercadier [France] ; M. Pignon [France] ; F. Calabuig [France] ; J. Lédé [France] ; Jacques Villermaux [France]Kinetics of isocyanuric acid pyrolysis
002782 (1994) S. Rode [France] ; Noël Midoux [France] ; M. A. Latifi [France] ; A. Storck [France]Hydrodynamics and liquid—solid mass transfer mechanisms in packed beds operating in cocurrent gas—liquid downflow: An experimental study using electrochemical shear rate sensors
002788 (1994) M. A. Latifi [France] ; A. Naderifar [France] ; Noël Midoux [France] ; A. Le Méhauté [France]Fractal behaviour of local liquid—solid mass transfer fluctuations at the wall of a trickle-bed reactor
002904 (1993) M. Hlavacek [France] ; F. Bouchet [France]Constant flowrate blocking laws and an example of their application to dead-end microfiltration of protein solutions
002A48 (1992) A. S. Lamine [France] ; M. T. Colli Serrano [France] ; G. Wild [France]Hydrodynamics and heat transfer in packed beds with liquid upflow
002A87 (1992) M. A. Latifi [France] ; S. Rode [France] ; Noël Midoux [France] ; A. Storck [France]The use of microelectrodes for the determination of flow regimes in a trickle-bed reactor
002B00 (1992) Faïçal Larachi [France] ; André Laurent [France] ; Gabriel Wild [France] ; Noël Midoux [France]Pressure effects on gas-liquid interfacial areas in cocurrent trickle-flow reactors
002B04 (1992) A. Lara Marquez [France] ; F. Larachi [France] ; G. Wild [France] ; A. Laurent [France]Mass transfer characteristics of fixed beds with cocurrent upflow and downflow. A special refence to the effect of pressure.
002B09 (1992) A. S. Lamine [France] ; M. T. Colli Serrano [France] ; G. Wild [France]Hydrodynamics and heat transfer in packed bed with cocurrent upflow
002B10 (1992) M. A. Latifi [France] ; S. Rode [France] ; Noël Midoux [France] ; A. Storck [France]Hydrodynamic study of a trickle-bed reactor by means of microelectrodes: analysis of the probability densities
002C57 (1991) Faïcal Larachi [France] ; André Laurent [France] ; Noël Midoux [France] ; Gabriel Wild [France]Liquid saturation data in trickle beds operating under elevated pressure
002E69 (1989) Mohamad Saberian-Broudjenni [France] ; Gabriel Wild [France] ; Sang Done Kim [France]Liquid axial dispersion in gas—liquid—solid fluidized beds
002E90 (1989) M. A. Latifi [France] ; Noël Midoux [France] ; A. Storck [France] ; J. N. Gence [France]The use of micro-electrodes in the study of the flow regimes in a packed bed reactor with single phase liquid flow
002E97 (1989) R. M. Nicoud ; D. SchweichSolute transport in porous media with solid‐liquid mass transfer limitations: Application to ion exchange
002F48 (1988) M. A. Latifi [France] ; A. Laurent [France] ; A. Storck [France]Liquid—solid mass transfer in a packed bed with downward cocurrent gas—liquid flow: An organic liquid phase with high Schmidt number

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