Tc. Thulasidas et al., THE MONOLITH FROTH REACTOR - RESIDENCE TIME MODELING AND ANALYSIS, Chemical engineering research & design, 73(A3), 1995, pp. 314-319
A mathematical model describing the residence time for a liquid compon
ent in a gas-liquid-solid monolith reactor has been developed. When tr
avelling in a slug flow pattern, the liquid exhibits alternating regio
ns of upflow in well mixed liquid slugs and downflow along the walls o
f the monolith channel. The model was developed for flow in a single s
quare capillary and indicates a mixing pattern that resembles well-mix
ed behaviour. Theoretical calculations are compared with experimental
results. The model can be extended to the monolith froth reactor by a
statistical analysis of flow within the channels of the monolith. Beca
use the monolith reactor represents a distribution of flow patterns, i
t exhibits greater axial mixing and higher average residence times tha
n would be expected based on the single channel analysis.