Flow patterns, liquid holdup, and wetting behavior of viscous liquids in a disk-distributor rotating packed bed

被引:20
作者
Li, Yan-Bin [1 ,2 ]
Wen, Zhang-Nan [1 ,2 ]
Sun, Bao-Chang [1 ,2 ]
Luo, Yong [1 ,2 ]
Gao, Ke-Jing [3 ]
Chu, Guang-Wen [1 ,2 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Organ Inorgan Composites, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Minist Educ High Grav Engn & Technol, Res Ctr, Beijing 100029, Peoples R China
[3] China Natl Petr Corp, Petrochem Res Inst, Beijing 102206, Peoples R China
关键词
Flow patterns; Liquid holdup; High viscosity; Computational fluid dynamics; Rotating packed bed; COMPUTATIONAL FLUID-DYNAMICS; PROCESS INTENSIFICATION; MASS-TRANSFER; SPINNING DISK; CO2; CAPTURE; WASTE-WATER; FILM FLOW; GAS; REACTOR; SIMULATION;
D O I
10.1016/j.ces.2021.117256
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel disk-distributor rotating packed bed (DRPB) was developed in this study to promote the application of RPBs for high-viscosity processes. A rotating disk was used as a liquid distributor in the inner cavity of the DRPB to distribute a high-viscosity liquid, and the porous packing was anchored radially outside the disk to additionally disperse the incoming liquid. Three-dimensional Eulerian multiphase simulations were implemented to examine the liquid flow characteristics in the packing after experimental validation. With increasing viscosity (l) from 11 mPa.s to 59372 mPa.s, flow patterns were transformed from dispersive into continuous modes. Liquid holdup, which ranged from 0.0006 to 0.25, was proportional to mu(0.61). Wetting efficiency and wetting height varied in ranges of 0.0012-0.416 and 3.03-14.57 mm, respectively. At a viscosity of 3331 mPa.s, approaches involving the use of multistage DRPB and the installation of redistribution blades improved the axial utilization efficiency of the packing from 20% to 80% and 20% to 92%, respectively.(c) 2021 Elsevier Ltd. All rights reserved.
引用
收藏
页数:16
相关论文
共 43 条
[1]  
[Anonymous], 2011, ISO11331
[2]  
[Anonymous], 2017, Theory guide toFluent 18.2
[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]   Process intensification: spinning disc reactor for condensation polymerisation [J].
Boodhoo, KVK ;
Jachuck, RJ .
GREEN CHEMISTRY, 2000, 2 (05) :235-244
[5]   Process intensification: spinning disk reactor for styrene polymerisation [J].
Boodhoo, KVK ;
Jachuck, RJ .
APPLIED THERMAL ENGINEERING, 2000, 20 (12) :1127-1146
[6]   MELT FLOW INDEX VALUES AND MOLECULAR-WEIGHT DISTRIBUTIONS OF COMMERCIAL THERMOPLASTICS [J].
BREMNER, T ;
RUDIN, A ;
COOK, DG .
JOURNAL OF APPLIED POLYMER SCIENCE, 1990, 41 (7-8) :1617-1627
[7]   Process intensification: Visual study of liquid maldistribution in rotating packed beds [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (08) :1347-1352
[8]   Measurement of liquid film thickness and the determination of spin-up radius on a rotating disc using an electrical resistance technique [J].
Burns, JR ;
Ramshaw, C ;
Jachuck, RJ .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (11) :2245-2253
[9]   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
[10]   Mass Transfer Study of Dehydration by Triethylene Glycol in Rotating Packed Bed for Natural Gas Processing [J].
Cao, Shaobo ;
Liu, Ping ;
Zhang, Lianglian ;
Sun, Baochang ;
Zou, Haikui ;
Chu, Guangwen ;
Luo, Yong ;
Ghen, Jianfeng .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (15) :5394-5400