Reynolds number effects on laminar mixing in the Kenics static mixer

被引:77
作者
Hobbs, DM [1 ]
Muzzio, FJ [1 ]
机构
[1] Rutgers State Univ, Dept Chem & Biochem Engn, Piscataway, NJ 08855 USA
关键词
Kenics static mixer; Reynolds numbers; Poincare sections; laminar flow; mixing performance;
D O I
10.1016/S0923-0467(98)00065-7
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The Kenics static mixer was investigated numerically using Lagrangian methods to characterize mixer performance in laminar flow. Techniques from dynamical systems analysis (Poincare sections, tracking of fluid tracers, and the development of stretching histories for tracer elements) as well as a more traditional mixing measure (the variation coefficient) were used to compare mixing performance at various Reynolds numbers. For creeping flow conditions (Re less than or equal to 10), the Kenics flow is globally chaotic and mixing performance is independent of Re. For Re = 100, significant islands of regular motion develop. These islands do not exchange material with the remainder of the flow and act as a barrier to uniform mixing. For Re = 1000, the Row is predominantly chaotic again, but small islands remain, leading to less effective mixing than under creeping flow conditions. (C) 1998 Elsevier Science S.A. All rights reserved.
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页码:93 / 104
页数:12
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