Hydrodynamics of gas-liquid micro-fixed beds - Measurement approaches and technical challenges

被引:30
作者
Faridkhou, Ali [1 ]
Hamidipour, Mohsen [1 ]
Larachi, Faical [1 ]
机构
[1] Univ Laval, Dept Chem Engn, Quebec City, PQ G1V 0A6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Hydrodynamics; Micro-fixed bed reactors; Residence time distribution (RTD); Visualization; Pressure drop; Liquid holdup; MASS-TRANSFER; PACKED-BEDS; FLOW; TEMPERATURE; REACTORS; MICROREACTORS; DISPERSION; POROSITY;
D O I
10.1016/j.cej.2013.03.014
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Despite many areas that are open to investigation in the hydrodynamic study of micro-fixed bed reactors, conducting research in this field is mostly hampered by a number of experimental challenges that have made many attempts ineffectual. This work provides a summary of the technical challenges, problems and misconstrues one might encounter in performing hydrodynamic experiments on micro-fixed bed reactors. Some of these issues will be pointed out upon comparing classical residence time distribution (RTD) measurements through electrical conductivity probes at micro-fixed bed scale with near-wall RTD obtained via visualizations of dye-tracer elution and monitoring the changes in gray level intensity of the images. Laterally-averaged gray level intensity at both upstream and downstream extremities of the wall regions of interest acted as inlet and outlet curves for the Aris method. The major outcome of this work was experimental confirmation of theoretically predicted maximum liquid velocity in the high porosity zone close to the wall. Finally, the experimental results on pressure drop and liquid holdup obtained upon following the right experimental protocols are presented. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:425 / 435
页数:11
相关论文
共 25 条
[1]   Microfabricated cross-flow chemical reactor for catalyst testing [J].
Ajmera, SK ;
Delattre, C ;
Schmidt, MA ;
Jensen, KF .
SENSORS AND ACTUATORS B-CHEMICAL, 2002, 82 (2-3) :297-306
[2]   Numbered-up gas-liquid micro/milli channels reactor with modular flow distributor [J].
Al-Rawashdeh, M. ;
Yu, F. ;
Nijhuis, T. A. ;
Rebrov, E. V. ;
Hessel, V. ;
Schouten, J. C. .
CHEMICAL ENGINEERING JOURNAL, 2012, 207 :645-655
[3]   High-pressure trickle-bed reactors: A review [J].
AlDahhan, MH ;
Larachi, F ;
Dudukovic, MP ;
Laurent, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (08) :3292-3314
[4]   Trickle bed hydrodynamics and flow regime transition at elevated temperature for a Newtonian and a non-Newtonian liquid [J].
Aydin, B ;
Larachi, F .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (23) :6687-6701
[5]   Microfabricated multiphase reactors for the selective direct fluorination of aromatics [J].
de Mas, N ;
Günther, A ;
Schmidt, MA ;
Jensen, KF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (04) :698-710
[6]   Heterogeneously catalyzed synthesis of performic acid in a microstructured reactor [J].
Ebrahimi, Fatemeh ;
Kolehmainen, Eero ;
Turunen, Ilkka .
CHEMICAL ENGINEERING JOURNAL, 2012, 179 :312-317
[7]  
Ehrfeld W., 2000, MICROREACTORS
[8]   Hydrodynamics of Gas-Liquid Cocurrent Flows in Micropacked Beds-Wall Visualization Study [J].
Faridkhou, Ali ;
Larachi, Faical .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (50) :16495-16504
[9]   Visualisation of flow processes in packed beds with NMR imaging:: determination of the local porosity, velocity vector and local dispersion coefficients [J].
Götz, J ;
Zick, K ;
Heinen, C ;
König, T .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2002, 41 (07) :611-629
[10]   Assessment of micro-structured fixed-bed reactors for highly exothermic gas-phase reactions [J].
Guettel, Robert ;
Turek, Thomas .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (05) :1644-1654