A method for estimating effective coalescence rates during emulsification from oil transfer experiments

被引:10
作者
Hakansson, Andreas [1 ]
Tragardh, Christian [1 ]
Bergenstahl, Bjorn [1 ]
机构
[1] Lund Univ, Dept Food Technol Engn & Nutr, SE-22100 Lund, Sweden
基金
瑞典研究理事会;
关键词
Coalescence; Emulsification; Population Balance Equations; High-pressure homogenization; HIGH-PRESSURE HOMOGENIZER; POPULATION BALANCE-EQUATIONS; LIQUID-LIQUID DISPERSIONS; DEVELOPED TURBULENT-FLOW; EMULSION DROPLETS; BREAK-UP; DROPS; DISCRETIZATION; COAGULATION; FREQUENCIES;
D O I
10.1016/j.jcis.2011.12.079
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The Oil Transfer Technique (OTT) was developed by Taisne et al. [1] to measure coalescence during emulsification and has been applied since in several studies. One of the main drawbacks of this technique is that it only gives a qualitative measure of coalescence. This paper proposes a new evaluation method of OTT experimental results for estimating qualitative coalescence rates, e.g. for investigating the scaling of coalescence with emulsification parameters (such as homogenizing pressure, and emulsifier concentration). The method is based on comparison with simulated OTT experiments using bivariate Population Balance Equation models. Simulations have been performed under a wide variety of conditions in order to investigate the influence of assumptions on coalescence and fragmentation kernels. These investigations show that the scaling of coalescence rates could be determined accurately when the scaling of efficient residence time of drops in the active region of homogenization is known. The proposed evaluation method is also exemplified by analyzing OTT data from two previously published studies. (C) 2012 Elsevier Inc. All rights reserved.
引用
收藏
页码:25 / 33
页数:9
相关论文
共 33 条
[1]   A new framework for solution of multidimensional population balance equations [J].
Chakraborty, Jayanta ;
Kumar, Sanjeev .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (15) :4112-4125
[2]   On the solution and applicability of bivariate population balance equations for mixing in particle phase [J].
Chauhan, Shivendra Singh ;
Chakraborty, Jayanta ;
Kumar, Sanjeev .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (13) :3914-3927
[3]   DESCRIPTION OF INTERACTION PROCESSES IN AGITATED LIQUID-LIQUID DISPERSIONS [J].
COULALOGLOU, CA ;
TAVLARIDES, LL .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (11) :1289-1297
[4]   COAGULATION IN TURBULENT-FLOW - THEORY AND EXPERIMENT [J].
DELICHATSIOS, MA ;
PROBSTEIN, RF .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1975, 51 (03) :394-405
[5]   Analysis of a new type of high pressure homogeniser. Part B. Study of droplet break-up and recoalescence phenomena [J].
Floury, J ;
Legrand, J ;
Desrumaux, A .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (06) :1285-1294
[6]   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
[7]   High resolution experimental measurement of turbulent flow field in a high pressure homogenizer model and its implications on turbulent drop fragmentation [J].
Hakansson, Andreas ;
Fuchs, Laszlo ;
Innings, Fredrik ;
Revstedt, Johan ;
Tragardh, Christian ;
Bergenstahl, Bjorn .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (08) :1790-1801
[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]   FUNDAMENTALS OF THE HYDRODYNAMIC MECHANISM OF SPLITTING IN DISPERSION PROCESSES [J].
HINZE, JO .
AICHE JOURNAL, 1955, 1 (03) :289-295
[10]   MEASUREMENT OF COALESCENCE FREQUENCY IN AN AGITATED TANK [J].
HOWARTH, WJ .
AICHE JOURNAL, 1967, 13 (05) :1007-&