(172c) Computational Fluid Dynamic (CFD) Simulations of Multiphase Flow through Representative Elementary Units (REU) of Structured Packing
AIChE Spring Meeting and Global Congress on Process Safety
2018
2018 Spring Meeting and 14th Global Congress on Process Safety
Distillation Symposium
Advances in Distillation Technology I
Wednesday, April 25, 2018 - 9:42am to 10:17am
Trien (Mikey) Phan and R. Bruce Eldridge
James R. Fair Process Science and Technology Center
The University of Texas at Austin
Current model predictions of the hydraulic behavior and separation performance of structured packings rely on semi-empirical correlations whose ranges of viability are limited to the packings and operating conditions used during correlation development. A more fundamental understanding of the momentum transfer inside structured packings is crucial for improving model predictions of the hydraulic properties of structured packing, which in turn can lead to optimized designs of mass transfer column internals. To this end, we utilized Computational Fluid Dynamics (CFD) to simulate gas-liquid flows inside simplified Representative Elementary Units (REU) of structured packing. Using Siemensâ STAR-CCM+ CFD software, we investigated the impact of packing geometry, such as corrugation angle and flow channel dimensions, as well as fluid properties, such as surface tension and contact angle, on the hydraulic performance of an REU. The modeling results yielded an optimum geometry for the hydraulic performance of structured packing.