Formation and charaterization of submicrometer oil-in-water (O/W) emulsions, using high-energy emulsification

被引:56
作者
Seekkuarachchi, IN
Tanaka, K
Kumazawa, H [1 ]
机构
[1] Toyama Univ, Dept Chem Proc Engn, Toyama 9308555, Japan
[2] Sugino Machine Ltd, Plant Equipment Dept, Toyama 9368577, Japan
关键词
D O I
10.1021/ie050323+
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Submicrometer emulsions were generated by a high-pressure wet-type jet mill and a motionless mixer called the Ramond Supermixer. Kerosene and liquid paraffin were used as the dispersed phase, aqueous sucrose and poly(ethylene glycol) solutions of PEG 400 to PEG 20000 were used as the continuous phase, and sodium dodecyl sulfate was used as a surfactant. The droplet size distribution, the Sauter mean diameter (d(32)), and the geometric standard deviation of the droplet size distribution (sigma(g)) were investigated under various combinations of the operating variables. The analysis of time-scale parameters contributed to an understanding of droplet deformation and possible re-coalescence. The relationship between the maximum droplet diameter and d(32) was determined to be a function of the ratio of the viscosity of the dispersed phase to the viscosity of the continuous phase (K). Empirical correlations were constructed for d(32) and sigma(g), and a larger similarity was determined to exist within the correlations, irrespective of the emulsifier that was used. Mechanistic models were developed to describe the droplet formation in view of droplet breakage phenomena with negligible re-coalescence. Separate models were proposed for both the turbulent inertia sub-range and the viscous subrange. For the viscous sub-range, a plot of the critical Weber number versus K revealed a rapid increase of droplet diameter at K < 0.05, regardless of the emulsifier.
引用
收藏
页码:372 / 390
页数:19
相关论文
共 38 条
[1]  
ALTAWEEL AM, 1983, CAN J CHEM ENG, V61, P527
[2]   ORTHOKINETIC COLLISIONS OF HARD SPHERES IN SIMPLE SHEAR-FLOW [J].
ARP, PA ;
MASON, SG .
CANADIAN JOURNAL OF CHEMISTRY-REVUE CANADIENNE DE CHIMIE, 1976, 54 (23) :3769-3774
[3]   Influence of continuous phase viscosity on emulsification by ultrasound [J].
Behrend, O ;
Ax, K ;
Schubert, H .
ULTRASONICS SONOCHEMISTRY, 2000, 7 (02) :77-85
[4]   DISPERSION OF VISCOUS-LIQUIDS BY TURBULENT-FLOW IN A STATIC MIXER [J].
BERKMAN, PD ;
CALABRESE, RV .
AICHE JOURNAL, 1988, 34 (04) :602-608
[5]   DROP BREAKUP IN THE VISCOUS SUBRANGE - A SOURCE OF POSSIBLE CONFUSION [J].
BOURNE, JR ;
BALDYGA, J .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (07) :1077-1078
[6]   DROP BREAKUP IN TURBULENT STIRRED-TANK CONTACTORS .1. EFFECT OF DISPERSED-PHASE VISCOSITY [J].
CALABRESE, RV ;
CHANG, TPK ;
DANG, PT .
AICHE JOURNAL, 1986, 32 (04) :657-666
[7]  
CHESTERS AK, 1991, CHEM ENG RES DES, V69, P259
[8]   DESCRIPTION OF INTERACTION PROCESSES IN AGITATED LIQUID-LIQUID DISPERSIONS [J].
COULALOGLOU, CA ;
TAVLARIDES, LL .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (11) :1289-1297
[10]   EFFECT OF HOLD-UP ON DROP SIZES IN LIQUID-LIQUID DISPERSIONS [J].
DOULAH, MS .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1975, 14 (02) :137-138