Prediction of effective area and liquid hold-up in structured packings by CFD

被引:87
作者
Haroun, Y. [1 ]
Raynal, L. [1 ]
Alix, P. [1 ]
机构
[1] IFP Energies Nouvelles, F-69360 Solaize, France
关键词
Structured packing; Effective mass transfer area; CFD; Volume of fluid method; CO2; capture; Gas treatment; DIRECT NUMERICAL-SIMULATION; MASS-TRANSFER; GAS-LIQUID; PRESSURE-DROP; DISTILLATION; ABSORPTION; VOLUME; MODEL; FLOW; EFFICIENCY;
D O I
10.1016/j.cherd.2013.12.029
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Interfacial effective area and liquid hold-up in structured packing geometries are investigated using the volume of fluid method. Three-dimensional numerical simulations of gas-liquid flow on inclined plane plate and in a structured packing are performed. The VOF method is used to capture the gas-liquid interface motion. After a first validation case on the wetting phenomena prediction on an inclined plane plate, the effective interfacial area, the liquid holdup and the degree of wetting of packing are studied as function of liquid flow rate and wall surface characteristic (adherence contact angle). Results show that the liquid flow-rate and the contact angle play a significant role. It is found that the interfacial effective area and the degree of wetting of packing increase as the liquid flow rate increases and as the contact angle decreases. Moreover, under the influence of the contact angle, different liquid film shapes are observed. The simulations results are compared to experimental data available in literature. This work shows that the CFD is a powerful tool to investigate performance characteristics of structured packings. Moreover, this work shows how CFD can be used as an effective tool to provide information on fluid flow behavior and determination of interfacial area, liquid hold-up and minimum flow-rate to ensure complete wetting. These parameters could be further used in process simulation at larger scale for the development and the design of efficient packings. (C) 2014 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:2247 / 2254
页数:8
相关论文
共 50 条
[1]   Mass transfer and liquid hold-up determination in structured packing by CFD [J].
Haroun, Y. ;
Raynal, L. ;
Legendre, D. .
CHEMICAL ENGINEERING SCIENCE, 2012, 75 :342-348
[2]   Influence of the viscosity on the liquid hold-up in trickle-bed reactors with structured packings [J].
Sidi-Boumedine, R ;
Raynal, L .
CATALYSIS TODAY, 2005, 105 (3-4) :673-679
[3]   Improving design and scale-up of columns with structured packings by means of CFD [J].
Xia, Marc ;
Neumann, Maximilian ;
Rehfeldt, Sebastian ;
Klein, Harald .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2023, 193 :54-64
[4]   Meso-scale CFD study of the pressure drop, liquid hold-up, interfacial area and mass transfer in structured packing materials [J].
Sebastia-Saez, Daniel ;
Gu, Sai ;
Ranganathan, Panneerselvam ;
Papadikis, Konstantinos .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2015, 42 :388-399
[5]   Determination of liquid hold-up and flow distribution inside modular catalytic structured packings [J].
Viva, Aurora ;
Aferka, Said ;
Toye, Dominique ;
Marchot, Pierre ;
Crine, Michel ;
Brunazzi, Elisabetta .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (8A) :1414-1426
[6]   Liquid distribution and liquid hold-up in modern high capacity packings [J].
Alix, Pascal ;
Raynal, Ludovic .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2008, 86 (6A) :585-591
[7]   Tomographic measurement of liquid hold up and effective interfacial area distributions in a column packed with high performance structured packings [J].
Aferka, S. ;
Viva, A. ;
Brunazzi, E. ;
Marchot, P. ;
Crine, M. ;
Toye, D. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (14) :3413-3422
[8]   Investigation of dynamic liquid distribution and hold-up in structured packings using ultrafast electron beam X-ray tomography [J].
Janzen, A. ;
Schubert, M. ;
Barthel, F. ;
Hampel, U. ;
Kenig, E. Y. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 66 :20-26
[9]   CFD Simulation of hold-up and liquid circulation velocity in a membrane airlift reactor [J].
Moraveji, M. K. ;
Sajjadi, B. ;
Davarnejad, R. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2012, 46 (03) :266-273
[10]   Prediction of the Effective Area in Structured Packings by Computational Fluid Dynamics [J].
Shojaee, Saeed ;
Hosseini, Seyyed Hossein ;
Rafati, Arash ;
Ahmadi, Goodarz .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (18) :10833-10842