Influence of channel geometry on hydrodynamics and mass transfer in the monolith film flow reactor
- 15 September 2001
- journal article
- Published by Elsevier in Catalysis Today
- Vol. 69 (1-4), 153-163
- https://doi.org/10.1016/s0920-5861(01)00391-1
Abstract
No abstract availableThis publication has 4 references indexed in Scilit:
- Gas–liquid mass transfer in an internally finned monolith operated countercurrently in the film flow regimeChemical Engineering Science, 1999
- Hydrodynamics and mass transfer issues in a countercurrent gas-liquid internally finned monolith reactorChemical Engineering Science, 1999
- Counter-current operation of structured catalytically packed distillation columns: pressure drop, holdup and mixingChemical Engineering Science, 1999
- Effect of Entrance and Exit Geometry on Pressure Drop and Flooding Limits in a Single Channel of an Internally Finned MonolithIndustrial & Engineering Chemistry Research, 1998