Liquid back-mixing in packed-bubble column reactors: A state-of-the-art correlation
The extent of liquid back-mixing in gas-liquid concurrent upflow packed-bubble column reactors is quantified in terms of an axial dispersion coefficient or its corresponding dimensionless Peclet number. Effects of reactor operating conditions on the axial dispersion coefficient are not properly acco...
Guardado en:
Autores principales: | Belfares, L., Cassanello, M., Grandjean, B.P.A., Larachi, F. |
---|---|
Formato: | JOUR |
Materias: | |
Acceso en línea: | http://hdl.handle.net/20.500.12110/paper_09205861_v64_n3-4_p321_Belfares |
Aporte de: |
Ejemplares similares
-
Liquid back-mixing in packed-bubble column reactors: A state-of-the-art correlation
Publicado: (2001) -
Mass transfer to the wall of a packed and unpacked bubble column operating with Newtonian and non-Newtonian liquids
Publicado: (2006) -
Mass transfer to the wall of a packed and unpacked bubble column operating with Newtonian and non-Newtonian liquids
por: Khamadieva, R., et al. -
Influence of structured packing on gas holdup in a three-phase bubble column
Publicado: (2007) -
Influence of structured packing on gas holdup in a three-phase bubble column
por: Monsalvo, M., et al.