Abstract
In the modeling of gas-liquid separation processes in structured packings, fluid dynamics is often reduced to a uniform liquid film flow over the packing surface. However, previous experiments with X-ray tomography indicate that this assumption is not valid when the liquid-phase viscosity is significantly higher than 1 mPa s. In order to improve existing modeling approaches for viscous systems, a better understanding of the influence of the liquid viscosity on the liquid flow inside the structured packing is necessary. In this work, X-ray tomography is used to investigate the flow morphology of liquid systems with low surface tension and a viscosity up to 50 mPa s. An empirical correlation that describes the hold-up fraction of the existing flow patterns is given and a modelling approach is proposed that allows to consider the influence of the different flow patterns on mass transfer.
Sign-in/Register to access full text options 
Free) 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a call
