On the droplet formation in hollow-fiber emulsification

被引:12
作者
Breisig, Hans [1 ,2 ]
Hoppe, Jens [1 ]
Melin, Thomas [1 ]
Wessling, Matthias [1 ,2 ]
机构
[1] Rhein Westfal TH Aachen, D-52064 Aachen, Germany
[2] DWI Leibniz Inst Interact Mat Res, D-52074 Aachen, Germany
关键词
Hollow-fiber emulsification; Membrane emulsification; Thread breakup; Droplet formation; Computational fluid dynamics; COMPUTATIONAL FLUID-DYNAMICS; MEMBRANE EMULSIFICATION; MICROFLUIDIC DEVICE; DOUBLE EMULSIONS; VOLUME; MICROCHANNELS; MODEL;
D O I
10.1016/j.memsci.2014.05.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hollow-fiber emulsification is a recent development that allows a continuous production of narrow-dispersed droplets with tunable diameter using hollow-fiber membranes. The to-be-dispersed phase is fed on one end through the lumen side while the continuous phase permeates through the membrane wall. After droplet formation, a droplet train leaves the hollow fiber on the other end. Droplet break-up has been assumed to occur inside a hollow-fiber membrane originating from Rayleigh-like instabilities; however proof has been missing yet due to missing visualization techniques inside the hollow fiber. Here we proof for the first time experimentally the droplet break-up mechanism and support these findings using computational fluid dynamics (CFD) simulations. Results of the CFD simulations are compared with experiments carried out using a glycerol-water solution as droplet phase and paraffin oil as continuous phase. The oil turns the porous hollow-fiber membrane transparent thus allowing direct observation of the droplet formation process inside the membrane. Comparisons were carried out by variation of the volume flow rate of the disperse phase and its viscosity as relevant influencing parameters and for the target parameters droplet size and droplet break-up length. Simulations capture the governing trends of the process such as the presence of a size maximum and allow the prediction of the required membrane lengths for droplet break-up. The droplet size maximum is explained using the understanding of droplet detachment in co-flowing streams. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:109 / 115
页数:7
相关论文
共 36 条
[1]   Process fundamentals of membrane emulsification: Simulation with CFD [J].
Abrahamse, AJ ;
van der Padt, A ;
Boom, RM ;
de Heij, WBC .
AICHE JOURNAL, 2001, 47 (06) :1285-1291
[2]   Formation of dispersions using "flow focusing" in microchannels [J].
Anna, SL ;
Bontoux, N ;
Stone, HA .
APPLIED PHYSICS LETTERS, 2003, 82 (03) :364-366
[3]   Polyreactions in miniemulsions [J].
Antonietti, M ;
Landfester, K .
PROGRESS IN POLYMER SCIENCE, 2002, 27 (04) :689-757
[4]   A CONTINUUM METHOD FOR MODELING SURFACE-TENSION [J].
BRACKBILL, JU ;
KOTHE, DB ;
ZEMACH, C .
JOURNAL OF COMPUTATIONAL PHYSICS, 1992, 100 (02) :335-354
[5]  
Brauer H.:., 1971, Grundlagen der Einphasen- und Mehrphasenstromungen
[6]   Formula for the viscosity of a glycerol-water mixture [J].
Cheng, Nian-Sheng .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (09) :3285-3288
[7]   Drop formation in a co-flowing ambient fluid [J].
Cramer, C ;
Fischer, P ;
Windhab, EJ .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (15) :3045-3058
[8]   Porous microfluidic devices - Fabrication and applications [J].
de Jong, Jorrit ;
Geerken, Maik J. ;
Lammertink, Rob G. H. ;
Wessling, Matthias .
CHEMICAL ENGINEERING & TECHNOLOGY, 2007, 30 (03) :309-315
[9]   Computational fluid dynamics model of viscous droplet breakup [J].
Dietsche, L. J. ;
Neubauer, A. C. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (22) :4543-4552
[10]   Tailoring surface properties for controlling droplet formation at microsieve membranes [J].
Geerken, M. J. ;
Lammertink, R. G. H. ;
Wessling, M. .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2007, 292 (2-3) :224-235