Simulation of the population balances for liquid-liquid systems in a nonideal stirred tank. Part 1 Description and qualitative validation of the model

被引:149
作者
Alopaeus, V
Koskinen, J
Keskinen, KI
机构
[1] Helsinki Univ Technol, Dept Chem Technol, Helsinki 02015, Finland
[2] Neste Oyj Engn, Porvoo, Finland
关键词
population balances; liquid-liquid dispersions; inhomogenity; computer simulations; multiblock stirred tank model;
D O I
10.1016/S0009-2509(99)00170-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A simulation model has been developed to model drop populations in a stirred tank. A multiblock stirred tank model has been used with the drop population balance equations developed in the literature. The stirred tank is modeled separately so that local turbulent energy dissipation values and fluid flows are used in the drop breakage and coalescence functions. This model has several attractive features, e.g. it can predict the inhomogenity of dispersions and some scale-up phenomena. Because local conditions can be used in the drop rate functions needed in the population balances, it is possible to take these fundamental processes into closer examination. It seems that the parameter values in the drop breakage and coalescence models depend on flow and turbulence averaging for the vessel. This proposes that for "intrinsic" drop breakage and coalescence rates, a multiblock model for the stirred tank is needed in parameter estimation as well. The stirred tank flow model may be obtained from measurements or from computational fluid dynamics simulations in a straightforward manner. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:5887 / 5899
页数:13
相关论文
共 31 条
[1]  
[Anonymous], 1988, TRANSPORT PHENOMENA
[2]   MASS-TRANSFER IN A LIQUID-LIQUID CFSTR [J].
BAPAT, PM ;
TAVLARIDES, LL .
AICHE JOURNAL, 1985, 31 (04) :659-666
[3]   MONTE-CARLO SIMULATION OF MASS-TRANSFER IN LIQUID-LIQUID DISPERSIONS [J].
BAPAT, PM ;
TAVLARIDES, LL ;
SMITH, GW .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (12) :2003-2013
[4]   INVESTIGATION OF MICROMIXING IN STIRRED-TANK REACTORS USING PARALLEL REACTIONS [J].
BOURNE, JR ;
YU, SY .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (01) :41-55
[5]   STEADY-STATE DROP-SIZE DISTRIBUTIONS IN HIGH HOLDUP FRACTION DISPERSION-SYSTEMS [J].
CHATZI, EG ;
KIPARISSIDES, C .
AICHE JOURNAL, 1995, 41 (07) :1640-1652
[6]  
Clift R, 1978, Bubbles, drops, and particles, DOI 10.1080/07373939308916817
[7]   DESCRIPTION OF INTERACTION PROCESSES IN AGITATED LIQUID-LIQUID DISPERSIONS [J].
COULALOGLOU, CA ;
TAVLARIDES, LL .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (11) :1289-1297
[8]  
Coulson J. M., 1991, CHEM ENG, V2
[9]   EFFECT OF HOLD-UP ON DROP SIZES IN LIQUID-LIQUID DISPERSIONS [J].
DOULAH, MS .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1975, 14 (02) :137-138
[10]  
Haase R., 1969, Thermodynamics of Irreversible Processes