Milli-channel with metal foams under an applied gas–liquid periodic flow: Flow patterns, residence time distribution and pulsing properties
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Claude de Bellefon | Régis Philippe | R. Philippe | C. Bellefon | J. Tourvieille | Jean-Noël Tourvieille
[1] J. Moulijn,et al. Scaling down trickle bed reactors , 2005 .
[2] G. Groppi,et al. Mass-Transfer Characterization of Metallic Foams as Supports for Structured Catalysts , 2005 .
[3] J. Moulijn,et al. Dispersion and Holdup in Multiphase Packed Bed Microreactors , 2008 .
[4] Peter J.T. Verheijen,et al. Scaling-up Multiphase Monolith Reactors: Linking Residence Time Distribution and Feed Maldistribution , 2005 .
[5] Bettina Kraushaar-Czarnetzki,et al. Mass transfer and pressure drop in ceramic foams: A description for different pore sizes and porosities , 2008 .
[6] Wernher Brevis,et al. Integrating cross-correlation and relaxation algorithms for particle tracking velocimetry , 2011 .
[7] Masahiro Kawaji,et al. The effect of channel diameter on adiabatic two-phase flow characteristics in microchannels ☆ , 2004 .
[8] Chin Pan,et al. Gas-liquid two-phase flow in micro-channels , 2002 .
[9] David Edouard,et al. Pressure drop measurements and modeling on SiC foams , 2007 .
[10] M. Ashby,et al. Cellular solids: Structure & properties , 1988 .
[11] B. Kuster,et al. Gas–liquid mass transfer and axial dispersion in solid foam packings , 2007 .
[12] N. A. Tsochatzidis,et al. Properties of pulsing flow in a trickle bed , 1995 .
[13] C. Stemmet,et al. Gas-Liquid Solid Foam Reactors: Hydrodynamics and Mass Transfer , 2005 .
[14] Freek Kapteijn,et al. Gas–liquid mass transfer of aqueous Taylor flow in monoliths , 2001 .
[15] S. Kuhn,et al. Scalar transport in a milli-scale metal foam reactor , 2010 .
[16] Said I. Abdel-Khalik,et al. Gas–liquid two-phase flow in microchannels: Part II: void fraction and pressure drop , 1999 .
[17] Adeniyi Lawal,et al. Numerical study on gas and liquid slugs for Taylor flow in a T-junction microchannel , 2006 .
[18] M. S. Ananth,et al. Hydrodynamics of two-phase cocurrent downflow through packed beds. Part I. Macroscopic model , 1983 .
[19] Asterios Gavriilidis,et al. Gas-liquid and gas-liquid-solid microstructured reactors : contacting principles and applications , 2005 .
[20] Klavs F. Jensen,et al. Microfabricated multiphase packed-bed reactors : Characterization of mass transfer and reactions , 2001 .
[21] Jc Jaap Schouten,et al. Gas-liquid mass transfer in rotating solid foam reactors , 2010 .
[22] H. A. Becker,et al. Mixing between a round jet and a transverse turbulent pipe flow , 1983 .
[23] Klavs F. Jensen,et al. Measurement of residence time distribution in microfluidic systems , 2005 .
[24] Faïçal Larachi,et al. Experimental study of a trickle-bed reactor operating at high pressure: two-phase pressure drop and liquid saturation , 1991 .
[25] Jerome Vicente,et al. Open Celled Material Structural Properties Measurement : From Morphology To Transport Properties , 2006 .
[26] N. Midoux,et al. FLOW PATTERN, PRESSURE LOSS AND LIQUID HOLDUP DATA IN GAS-LIQUID DOWNFLOW PACKED BEDS WITH FOAMING AND NONFOAMING HYDROCARBONS , 1976 .
[27] Muhammad Akbar,et al. On gas–liquid two-phase flow regimes in microchannels , 2003 .
[28] Feike J. Leij,et al. Modeling the Nonequilibrium Transport of Linearly Interacting Solutes in Porous Media: A Review , 1991 .
[29] van der J John Schaaf,et al. Hydrodynamics of gas¿liquid counter-current flow in solid foam packings , 2005 .
[30] Götz Veser,et al. Experimental and theoretical investigation of H2 oxidation in a high-temperature catalytic microreactor , 2001 .
[31] Y. W. Kwon,et al. Representative unit-cell models for open-cell metal foams with or without elastic filler , 2003 .
[32] Faïçal Larachi,et al. Hydrodynamics of gas–liquid micro-fixed beds – Measurement approaches and technical challenges , 2013 .
[33] C. Pham‐Huu,et al. Residence time distribution, axial liquid dispersion and dynamic–static liquid mass transfer in trickle flow reactor containing β-SiC open-cell foams , 2012 .
[34] Vito Specchia,et al. Pressure drop and liquid holdup for two-phase concurrent flow in packed beds , 1977 .
[35] Charlotte Pham,et al. Experimental measurements and multiphase flow models in solid SiC foam beds , 2008 .
[36] A. Burghardt,et al. Hydrodynamics of Pulsing Flow in Three-Phase Fixed-Bed Reactor Operating at an Elevated Pressure , 2004 .
[37] J. van der Schaaf,et al. Gas–liquid dynamics at low Reynolds numbers in pillared rectangular micro channels , 2010 .
[38] M. Kreutzer. Hydrodynamics of Taylor Flow in Capillaries and Monolith Reactors , 2003 .
[39] Adrian Zenklusen,et al. Axial dispersion in metal foams and streamwise-periodic porous media , 2011 .
[40] Srinivas Garimella,et al. Characterization of two-phase flow patterns in small diameter round and rectangular tubes , 1999 .
[41] Ruben G. Carbonell,et al. hydrodynamic parameters for gas-liquid cocurrent flow in packed beds , 1985 .
[42] V. G. Rao,et al. Pressure drop and hydrodynamic properties of pulses in two‐phase gas‐liquid downflow through packed columns , 1983 .
[43] Markus Schubert,et al. Hydrodynamic multiplicity in a tubular reactor with solid foam packings , 2013 .
[44] Ioannis G. Kevrekidis,et al. Dynamics of pulsing flow in trickle beds , 1990 .
[45] R. M. Sullivan,et al. A general tetrakaidecahedron model for open-celled foams , 2008 .
[46] Cesar Zarcone,et al. Numerical models and experiments on immiscible displacements in porous media , 1988, Journal of Fluid Mechanics.
[47] A. Attou,et al. Revue des aspects hydrodynamiques des réacteurs catalytiques gaz-liquide-solide à lit fixe arrosé , 1999 .
[48] J. E. Myers,et al. Fluid‐flow characteristics of concurrent gas‐liquid flow in packed beds , 1964 .
[49] Sang Yong Lee,et al. Pressure drop of two-phase plug flow in round mini-channels: Influence of surface wettability , 2008 .
[50] A. Drinkenburg,et al. Hydrodynamic properties of pulses in two-phase downflow operated packed columns , 1982 .
[51] J. Boelhouwer. Nonsteady operation of trickle-bed reactors : hydrodynamics, mass and heat transfer , 2001 .
[52] Hui Liu,et al. Hydrodynamics of Taylor Flow in Vertical Capillaries: Flow Regimes, Bubble Rise Velocity, Liquid Slug Length, and Pressure Drop , 2005 .