Micro-scale CFD modeling of reactive mass transfer in falling liquid films within structured packing materials

Abstract

Post-combustion carbon capture in structured packing columns is considered as a promising technology to reduce greenhouse gas (GHG) emissions because of its maturity and the possibility of being retrofitted to existing power plants. CFD plays an important role in the optimization of this technology. However, due to the current computational capacity limitations, the simulations need to be divided into three scales (i.e. micro-, meso- and macro-scale) depending on the flow characteristics to be analyzed. This study presents a 3D micro-scale approach to describe the hydrodynamics and reactive mass transfer of the CO2-MEA chemical system within structured packing materials. Higbie's penetration theory is used to describe the mass transfer characteristics whereas enhancement factors are implemented to represent the gain in the absorption rate attributable to the chemical reaction. The results show a detrimental effect of the liquid load on the absorption rate via a decrease in the enhancement factor. The evolution of the wetted area for MEA solutions is compared to the case of pure water highlighting the differences in the transient behavior. The CO2 concentration profiles are examined showing the capability of the model to reproduce the depletion of the solute within the bulk liquid ascribed to the high value of the Hatta number. Also, several approaches on the reaction mechanism such as reversibility and instantaneous behavior are assessed. The results from micro-scale are to be used in meso-scale analysis in future studies to optimize the reactive absorption characteristics of structured packing materials

Liquid‐bridge flow in the channel of helical string and its application to gas–liquid contacting process

“…For enhancing the heat and mass transfer efficiency in the gas–liquid contacting process, the thickness of the liquid film should be as thin as possible, to reduce the transfer resistance and to improve the renewal rate of the gas–liquid interface . The mean film thickness ( ), calculated by Eq.…”

Modelling of CO2 absorption in a rotating packed bed using an Eulerian porous media approach

“…Hikita et al (1977), Verstege et al (1996) and Horng and Li (2002). Many simulations on CO 2 absorption by MEA solutions have used the Hikita reaction rate constant (Pham et al, 2015;Sebastia-Saez et al, 2015;Niegodajew and Asendrych, 2016). Actually, these obtained reaction rate constants for the CO 2 absorption by the MEA are very similar.…”

A mesoscale 3D CFD analysis of the liquid flow in a rotating packed bed

“…which has been used to calculate the gas-liquid interfacial area in the VOF models (Sebastia-Saez et al, 2015b;Xu et al, 2009).…”