| 1 |
Gas and solid behaviours during defluidisation of Geldart-A particles
Santos ET, Hemati M, Andreux R, Ferschneider G
Powder Technology, 211(1), 156, 2011 |
| 2 |
Reduced model for characterization of solid wall effects for transient thermal dispersion in granular porous media
Fiers B, Ferschneider G, Maillet D
International Journal of Heat and Mass Transfer, 53(25-26), 5962, 2010 |
| 3 |
Experimental study of a fast gas-particle separator
Andreux R, Ferschneider G, Hemati M, Simonin O
Chemical Engineering Research & Design, 85(A6), 808, 2007 |
| 4 |
Hydrodynamics of trickle bed reactors at high pressure: Two-phase flow model for pressure drop and liquid holdup, formulation and experimental validation
Boyer C, Volpi C, Ferschneider G
Chemical Engineering Science, 62(24), 7026, 2007 |
| 5 |
Experimental validation of a two-phase flow model for pressure drop and liquid hold-up in downflow packed bed bubble reactors
Boyer C, Ferschneider G
Canadian Journal of Chemical Engineering, 81(3-4), 808, 2003 |
| 6 |
Dilute gas-solid flow in a riser
Ferschneider G, Mege P
Chemical Engineering Journal, 87(1), 41, 2002 |
| 7 |
Flow distribution studies applied to deep hydro-desulfurization
Harter I, Boyer C, Raynal L, Ferschneider G, Gauthier T
Industrial & Engineering Chemistry Research, 40(23), 5262, 2001 |
| 8 |
A two-fluid hydrodynamic model for the transition between trickle and pulse flow in a cocurrent gas-liquid packed-bed reactor
Attou A, Ferschneider G
Chemical Engineering Science, 55(3), 491, 2000 |
| 9 |
Modelling of the hydrodynamics of the cocurrent gas-liquid trickle flow through a trickle-bed reactor
Attou A, Boyer C, Ferschneider G
Chemical Engineering Science, 54(6), 785, 1999 |
| 10 |
A two-fluid model for flow regime transition in gas-liquid trickle-bed reactors
Attou A, Ferschneider G
Chemical Engineering Science, 54(21), 5031, 1999 |
