Liquid distribution plays a crucial role in the performance
of
the trickle bed reactor (TBR). Therefore, understanding the flow behavior
of a droplet impacting a spherical catalyst particle in the TBR is
essential for the design and operation of the reactor. In this study,
the volume of fluid (VOF) model was used to investigate this phenomenon.
The simulation results revealed two distinctive flow patterns: a uniform
liquid film flow pattern and a droplet flow pattern. To quantitatively
evaluate the two flow patterns, a postprocessing method was proposed
based on the Fibonacci sequence. The results indicate that the uniform
liquid film flow pattern can maintain larger total gas–liquid
interfacial area and specific interfacial area (thinner liquid film)
for a longer residence time compared to the droplet flow pattern,
demonstrating that the uniform liquid film flow pattern is a promising
way to optimize the TBR performance. To facilitate the formation of
a uniform liquid film on the particle, using liquids with smaller
contact angles, lower surface tension, and adjusting the droplet/particle
size ratio to a suitable range can be suggested.