Dynamics of liquid dispersion in a rotating packed bed with single-layer wire mesh

被引:8
作者
Chen, Wen-Cong [1 ]
Liu, Zhi-Hao [1 ]
Chu, Guang-Wen [1 ,2 ]
Zhang, Liang-Liang [1 ]
Chen, Jian-Feng [1 ,2 ]
机构
[1] Beijing Univ Chem Technol, Minist Educ High Grav Engn & Technol, Res Ctr, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, State Key Lab Organ Inorgan Composites, Beijing, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
breakup; dispersion dynamics; liquid ligament; numerical simulation; RPB; LIGAMENT FORMATION DYNAMICS; PROCESS INTENSIFICATION; MASS-TRANSFER; FLOW; FILM; DISINTEGRATION; PACKING;
D O I
10.1002/aic.18106
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The improvement of liquid dispersion by rotating wire mesh is one of the major causes for the mass transfer and micromixing intensification in rotating packed beds (RPBs). In particular, the initial dispersion region has been proved to have the greatest mass transfer and micromixing efficiency. However, the dispersion mechanism has not been revealed. This study investigated the dynamics of liquid dispersion in an RPB with single-layer wire mesh. The liquid dispersion behaviors were obtained by high-speed photography and numerical simulation. The liquid was found to stretch into ligaments and break into the main droplet and several satellite droplets. A new theoretical model was established to reveal the dispersion mechanism of these two stages. The stretching stage depends on the liquid initial momentum and acquired impulse, while the breakup stage was determined by the competition of ligaments recoil and pinch-off behaviors. The model was validated in good agreement with the experimental and simulation results of the dispersion characteristics.
引用
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页数:13
相关论文
共 39 条
[1]   Process Intensification in HiGee Absorption and Distillation: Design Procedure and Applications [J].
Agarwal, Lava ;
Pavani, V. ;
Rao, D. P. ;
Kaistha, N. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (20) :10046-10058
[2]   Influence of spinning cup and disk atomizer configurations on droplet size and velocity characteristics [J].
Ahmed, Mahmoud ;
Youssef, M. S. .
CHEMICAL ENGINEERING SCIENCE, 2014, 107 :149-157
[3]   LIQUID HOLDUP IN ROTATING PACKED-BEDS - EXAMINATION OF THE FILM FLOW ASSUMPTION [J].
BASIC, A ;
DUDUKOVIC, MP .
AICHE JOURNAL, 1995, 41 (02) :301-316
[4]   Experimental investigation of liquid disintegration by twin spinning wheel atomizer [J].
Bizjan, Benjamin ;
Sirok, Brane ;
Blagojevic, Marko .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2021, 165 :230-241
[5]   Liquid ligament formation dynamics on a spinning wheel [J].
Bizjan, Benjamin ;
Sirok, Brane ;
Hocevar, Marko ;
Orbanic, Alen .
CHEMICAL ENGINEERING SCIENCE, 2014, 119 :187-198
[6]   Process intensification: Visual study of liquid maldistribution in rotating packed beds [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (08) :1347-1352
[7]   Process intensification: operating characteristics of rotating packed beds - determination of liquid hold-up for a high-voidage structured packing [J].
Burns, JR ;
Jamil, JN ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (13) :2401-2415
[8]  
Chen J.F., 2002, High Gravity Technology and Application
[9]   Synthesis of nano-fibers of aluminum hydroxide in novel rotating packed bed reactor [J].
Chen, JF ;
Shao, L ;
Guo, F ;
Wang, XM .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (3-6) :569-575
[10]   Hydrodynamics of gas flow in a rotating packed bed under floating motions: Experimental and simulation study [J].
Chen, Wen-Cong ;
Meng, Wen-Hao ;
Liu, Zhi-Hao ;
Chu, Guang-Wen ;
Zhang, Liang-Liang ;
Chen, Jian-Feng .
CHEMICAL ENGINEERING JOURNAL, 2022, 442