Hydrodynamics of gas-liquid cocurrent upflow in oscillating packed beds for offshore marine applications

被引:19
|
作者
Dashliborun, Amir Motamed [1 ]
Larachi, Feical [1 ]
Schubert, Markus [2 ]
机构
[1] Univ Laval, Dept Chem Engn, Quebec City, PQ G1V 0A6, Canada
[2] Helmholtz Zentrum Dresden Rossendorf, Bautzner Landstr 400, D-01328 Dresden, Germany
基金
加拿大自然科学与工程研究理事会;
关键词
Cocurrent upflow packed bed; Oscillation; Wire mesh sensor; Hexapod motion simulator; Maldistribution; Hydrodynamics; TRICKLE-BED; PRESSURE-DROP; REACTOR PERFORMANCE; TUBULAR REACTOR; 2-PHASE FLOWS; FOAM PACKINGS; UP-FLOW; DOWNFLOW; IDENTIFICATION; SIMULATIONS;
D O I
10.1016/j.ces.2016.12.056
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, the hydrodynamic behavior of inclined stationary and oscillating packed beds with gas liquid cocurrent upflow mode of operation was investigated. Comprehensive hydrodynamic experiments were carried out using embedded low-intrusive Wire-Mesh Sensors (WMSs) and a hexapod ship motion simulator in order to properly understand the effect of column inclination and movements on gas-liquid flow distribution in the bed cross-section, overall pressure drop, liquid saturation, and pulsing flow inception. Furthermore, liquid residence time and Peclet number estimated by a stimulus-response technique and a macro-mixing model were presented and discussed with respect to the prevailing flow regimes. The results revealed that the column deviation from the vertical posture and tilting motions significantly alter the hydrodynamics prevailing in the packed bed operating in a concurrent upflow mode. Development of gas-liquid disengagement zones, oscillations in the pressure drop and uniformity factor time series, departure from liquid plug flow character, and delay in the inception of pulsing flow regime were observed as a result of bed inclination and oscillations. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:583 / 596
页数:14
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