CO2 abatement in oscillating packed-bed scrubbers: Hydrodynamics and reaction performances for marine applications

被引:24
|
作者
Iliuta, Ion [1 ]
Larachi, Faical [1 ]
机构
[1] Univ Laval, Dept Chem Engn, 1065 Ave Med, Quebec City, PQ G1V 0A6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
oscillating packed bed scrubbers; gas-liquid countercurrent flow; CO2-MEA absorption process; FPSO; on-board marine CO2 scrubber; 3-D model; reactor performance; LIQUID COCURRENT DOWNFLOW; CARBON-DIOXIDE; 2-PHASE FLOW; PULSE FLOW; MONOETHANOLAMINE; ABSORPTION; SIMULATION; MODEL; HEAT; DISPERSION;
D O I
10.1002/aic.15450
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas-liquid flow dynamics and CO2-monoethanolamine absorption performances of an oscillating countercurrent packed bed were analyzed by means of a transient 3D nonisothermal two-fluid flow model with a goal to understand the behavior of scrubbing units on-board floating production, storage and offloading platforms. Gas-liquid flow deviation from axial symmetry was significant at larger vessel inclinations prompting noticeable liquid accumulation in the column lowermost area. Conversely, in static vertical and slightly inclined columns only a reduced fraction of the liquid was subject to transverse segregation. Externally-generated column oscillations brought about complex secondary flows in radial and tangential directions resulting in oscillatory patterns with amplitude and propagation frequency affected by the packed bed oscillations. CO2 abatement in inclined and asymmetrically oscillating columns suffered perceptible deviations with respect to vertical configuration while symmetrically oscillating columns gave rise to CO2 performances oscillating around the steady-state solutions of the vertical column. (c) 2016 American Institute of Chemical Engineers AIChE J, 63: 1064-1076, 2017
引用
收藏
页码:1064 / 1076
页数:13
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