High resolution experimental measurement of turbulent flow field in a high pressure homogenizer model and its implications on turbulent drop fragmentation

被引:67
作者
Hakansson, Andreas [1 ]
Fuchs, Laszlo [2 ]
Innings, Fredrik [3 ]
Revstedt, Johan [2 ]
Tragardh, Christian [1 ]
Bergenstahl, Bjorn [1 ]
机构
[1] Lund Univ, Dept Food Technol Engn & Nutr, SE-22100 Lund, Sweden
[2] Lund Univ, Dept Energy Sci, SE-22100 Lund, Sweden
[3] Tetra Pak Proc Syst, Ruben Rausings Gata, SE-22186 Lund, Sweden
基金
瑞典研究理事会;
关键词
Homogenization; Turbulence; Hydrodynamics; Emulsion; Particle image velocimetry; Fragmentation; BREAK-UP; DEFORMATION; EMULSIFICATION; VISUALIZATION;
D O I
10.1016/j.ces.2011.01.026
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Particle image velocimetry is performed on a model of a high pressure homogenizer, scaled for qualitative similarity of the one phase turbulent flow field in a production scale homogenizer. Flow fields in gap entrance, gap and gap outlet chamber are obtained with high resolution. The measurements show gap flow development and formation of a turbulent wall adherent jet when exiting into the outlet chamber. Turbulent kinetic energy spectra show how the turbulent energy available for fragmentation is transported over distance along the jet centre axis. The high resolution images are also used together with a Kolmogorov-Hinze theory framework for discussing drop fragmentation together with a direct evaluation of disruptive stresses from measurements. For the turbulent inertial mechanism large drops experience high fragmenting force close to eight gap heights downstream of the gap exit where as this occurs closer to 20 gap heights for smaller drops. The turbulent viscous mechanism is most efficient at a downstream distance of eight gap heights into the outlet chamber for all drops sizes. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1790 / 1801
页数:12
相关论文
共 28 条
[1]
Budde C, 2002, CHEM ENG TECHNOL, V25, P1164, DOI 10.1002/1521-4125(20021210)25:12<1164::AID-CEAT1164>3.0.CO
[2]
2-E
[3]
A numerical procedure for predicting the performance of high pressure homogenizing valves [J].
Casoli, Paolo ;
Vacca, Andrea ;
Berta, Gian L. .
SIMULATION MODELLING PRACTICE AND THEORY, 2010, 18 (02) :125-138
[4]
[5]
Analysis of a new type of high pressure homogeniser. A study of the flow pattern [J].
Floury, J ;
Bellettre, J ;
Legrand, J ;
Desrumaux, A .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (04) :843-853
[6]
GRACE HP, 1980, CHEM ENG COMMUN, V14, P225
[7]
Visual observations and acoustic measurements of cavitation in an experimental model of a high-pressure homogenizer [J].
Hakansson, Andreas ;
Fuchs, Laszlo ;
Innings, Fredrik ;
Revstedt, Johan ;
Bergenstahl, Bjorn ;
Tragardh, Christian .
JOURNAL OF FOOD ENGINEERING, 2010, 100 (03) :504-513
[8]
Dynamic simulation of emulsion formation in a high pressure homogenizer [J].
Hakansson, Andreas ;
Tragardh, Christian ;
Bergenstahl, Bjorn .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (12) :2915-2925
[9]
[10]
Visualization of the drop deformation and break-up process in a high pressure homogenizer [J].
Innings, F ;
Trägårdh, C .
CHEMICAL ENGINEERING & TECHNOLOGY, 2005, 28 (08) :882-891