Numerical studies on effects of geometrical parameters of internals on bubble column hydrodynamics

被引:3
作者
Gaurav, Tuntun K. [1 ]
Prakash, Anand [1 ]
Zhang, Chao [2 ]
机构
[1] Univ Western Ontario, Chem & Biochem Engn, London, ON, Canada
[2] Univ Western Ontario, Mech & Mat Engn, London, ON, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Concentric tube internals; Eulerian-Eulerian CFD model; Hydrodynamics; Bubbles population balance; Internals geometry; FISCHER-TROPSCH SYNTHESIS; CFD SIMULATION; GAS HOLDUP; POPULATION BALANCE; TURBULENCE MODELS; INTERFACIAL FORCES; INTERPHASE FORCES; LIQUID DISPERSION; MEMBRANE REACTOR; BREAK-UP;
D O I
10.1016/j.cep.2022.109179
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Internals are an important part of bubble column design for applications in different industrial processes. A properly designed and configured internal can significantly improve the performance of the reactor. In this work, the Eulerian-Eulerian (E-E) Computational Fluid Dynamics (CFD) model using the discrete bubble population balance model (PBM) has been used to investigate effects of two important geometrical parameters for concentric tube bundle internal. These are tube-to-tube spacing and elevation of the tube bundle from column bottom. The simulations are conducted in 2D space by suitably accounting for vertical perforations in the concentric tube bundle. The results obtained compare well with trends of experimental simulation results from literature studies. It is determined that tube-to-tube spacing and the elevation of the bundle clearly alter mixing patterns in the column, requiring careful evaluations for a given application. The proposed simulation method based on 2D modeling can be a quick means to compare alternative configurations of internals.
引用
收藏
页数:18
相关论文
共 50 条
[31]   Investigations of flow structure and liquid mixing in bubble column equipped with selected internals [J].
George, Keller J. H. ;
Jhawar, Anil K. ;
Prakash, Anand .
CHEMICAL ENGINEERING SCIENCE, 2017, 170 :297-305
[32]   CFD simulations of a bubble column with and without internals by using OpenFOAM [J].
Bhusare, V. H. ;
Dhiman, M. K. ;
Kalaga, D. V. ;
Roy, S. ;
Joshi, J. B. .
CHEMICAL ENGINEERING JOURNAL, 2017, 317 :157-174
[33]   Impact of Internals on the Heat-Transfer Coefficient in a Bubble Column [J].
Abdulmohsin, Rahman S. ;
A-Dahhan, Muthanna H. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (07) :2874-2881
[34]   Effects of internals on fluid dynamics and reactions in pilot-scale slurry bubble column reactors: A CFD study for Fischer-Tropsch synthesis [J].
An, Min ;
Guan, Xiaoping ;
Yang, Ning ;
Bu, Yifeng ;
Xu, Ming ;
Men, Zhuowu .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2018, 132 :194-207
[35]   Impact of heat exchanging internals configurations on the gas holdup and bubble properties in a bubble column [J].
Jasim, Ahmed A. ;
Sultan, Abbas J. ;
Al-Dahhan, Muthanna H. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2019, 112 :63-82
[36]   Solid-liquid mass transfer in a bubble column reactor with tube bank internals [J].
Sedahmed, Gomaa ;
Nosier, S. A. ;
Abdel-Aziz, M. H. ;
El-Naggar, M. A. .
EXPERIMENTAL HEAT TRANSFER, 2021, 34 (05) :461-473
[37]   Influence of Gas Density on Hydrodynamics in a Bubble Column [J].
Tang Xiaojin ;
Hou Shuandi ;
Zhang Zhanzhu .
CHINA PETROLEUM PROCESSING & PETROCHEMICAL TECHNOLOGY, 2014, 16 (01) :66-70
[38]   The dual effect of viscosity on bubble column hydrodynamics [J].
Besagni, Giorgio ;
Inzoli, Fabio ;
De Guido, Giorgia ;
Pellegrini, Laura Annamaria .
CHEMICAL ENGINEERING SCIENCE, 2017, 158 :516-545
[39]   Hydrodynamics of a bubble column under elevated pressure [J].
Pohorecki, R ;
Moniuk, W ;
Zdrójkowski, A .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) :5187-5193
[40]   Hydrodynamics in a small size pressurized bubble column [J].
Ishiyama, H ;
Isokawa, Y ;
Sawai, J ;
Kojima, H .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) :6273-6278