Experimental and Numerical Study on the Residence Time Distribution in a Stirred Membrane Reactor

被引:5
作者
Hui, Yuanyuan [1 ,2 ]
Feng, Xin [1 ,2 ]
Duan, Xiaoxia [1 ]
Mao, Zai-Sha [1 ]
Yang, Chao [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, CAS Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
FLOW; OPTIMIZATION; SIMULATION; PREDICTION; PARAMETERS; IMPELLER;
D O I
10.1021/acs.iecr.3c00182
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The residence time distribution (RTD) of a reactor is a key factor related to the actual reaction time of reactants, by which the mixing in a reactor can be judged indirectly. Though many efforts have been made to study RTD in stirred tank reactors (STs) or membrane modules, research on RTD in a stirred membrane reactor (SMR) is still lacking. For this purpose, we investigated the influence of operating conditions on mixing in the SMR through experiments, obtained non-ideal mixing region by mathematical model fitting, and analyzed the flow field combined with CFD simulation. The critical value of the ratio of the discharge of impeller to the flow rate is 13.13 designed to reach ideal mixing in the SMR and that of the ratio of the mean residence time to the mixing time is 10 correspondingly. In addition, the RTD is independent of membrane permeability resistance.
引用
收藏
页码:6486 / 6499
页数:14
相关论文
共 37 条
[1]   Simulation and optimization of enzymatic hydrogen peroxide production in a continuous stirred tank reactor using CFD-RSM combined method [J].
Aghbolaghy, Mostafa ;
Karimi, Afzal .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2014, 45 (01) :101-107
[2]   Investigating the effect of sparger configuration on the hydrodynamics of a full-scale membrane bioreactor using computational fluid dynamics [J].
Amini, Ershad ;
Mehrnia, Mohammad Reza ;
Mousavi, Seyyed Mohammad ;
Azami, Hamed ;
Mostoufi, Navid .
RSC ADVANCES, 2015, 5 (127) :105218-105226
[3]   Modeling flow and residence time distribution in an industrial-scale reactor with a plunging jet inlet and optional agitation [J].
Bai, Hua ;
Stephenson, Amber ;
Jimenez, Jorge ;
Jewell, Dennis ;
Gillis, Paul .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2008, 86 (12A) :1462-1476
[4]   Development of a multiscale model for the design and scale-up of gas/liquid stirred tank reactors [J].
Bashiri, Hamed ;
Bertrand, Francois ;
Chaouki, Jamal .
CHEMICAL ENGINEERING JOURNAL, 2016, 297 :277-294
[5]   Time-dependent flow structures and Lagrangian mixing in Rushton-impeller baffled-tank reactor [J].
Campolo, M ;
Sbrizzai, F ;
Soldati, A .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (08) :1615-1629
[6]  
CARRENOLOPEZ F, 2023, EUR PHYS J C, V451, P1
[7]   In situ product recovery: Submerged membranes vs. external loop membranes [J].
Carstensen, Frederike ;
Apel, Andreas ;
Wessling, Matthias .
JOURNAL OF MEMBRANE SCIENCE, 2012, 394 :1-36
[8]   VELOCITY PROFILES AND PUMPING CAPACITIES FOR TURBINE TYPE IMPELLERS [J].
COOPER, RG ;
WOLF, D .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1968, 46 (02) :94-&
[9]   CFD optimization of continuous stirred-tank (CSTR) reactor for biohydrogen production [J].
Ding, Jie ;
Wang, Xu ;
Zhou, Xue-Fei ;
Ren, Nan-Qi ;
Guo, Wan-Qian .
BIORESOURCE TECHNOLOGY, 2010, 101 (18) :7005-7013
[10]   Extending potential flow modelling of flat-sheet geometries as applied in membrane-based systems [J].
Dirkse, M. H. ;
van Loon, W. K. P. ;
Stigter, J. D. ;
Post, J. W. ;
Veerman, J. ;
Bot, G. P. A. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 325 (02) :537-545