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转子导程及偏心率对面团混合器混合流场及效率影响分析
引用本文:朱向哲,高鹤,刘俭.转子导程及偏心率对面团混合器混合流场及效率影响分析[J].农业工程学报,2018,34(20):305-314.
作者姓名:朱向哲  高鹤  刘俭
作者单位:辽宁石油化工大学机械工程学院,抚顺 113001,辽宁石油化工大学机械工程学院,抚顺 113001,辽宁石油化工大学机械工程学院,抚顺 113001
基金项目:国家自然科学基金项目(51473073; 50903042);辽宁省高等学校创新人才支持计划项目(LR2016022)
摘    要:为了探究偏心螺旋转子扰动下面团混合器的混沌混合机制,明确偏心转子系统的关键几何参数对混沌混合机制的影响,从三维Lagrangian的新视角,利用有限时间Lyapunov指数(finite-time lyapunov exponent, FTLE)和拉格朗日拟序结构(lagrangian coherent structure, LCS),结合经典Poincaré截面,对面团混合器的流体输运和混合机理进行了深入研究。利用LCS的准边界特性,分析了混合器的混沌和非混沌区域分布规律;研究了转子偏心率对混沌尺度和非混沌区粒子运动特性的影响规律。利用剪切速率、对数拉伸、瞬时混合效率和平均时间混合效率等,分析了转子导程和偏心率对混合器混合效率的影响。结果表明,双曲LCS将混合器流域划分为两个不同动力学特性的区域:内回转区和外螺旋区。随着转子偏心率逐渐增大,外螺旋区流体的混沌混合强度增大,内回转区混合强度逐渐较低,当偏心率较小时,流体混合以内回转区运动为主;由于转子扰动减小,减小了混合器的轴向物质输运。从拉伸流动混合效率角度可知,当导程l=120 mm、偏心率ε=0.67时,混合器的具有相对较高的拉伸混合效率;当导程l=60 mm、偏心率ε=0.33时,混合器的拉伸混合效率相对最低,但其剪切混合效率相对最高。该文为食品及其它混合设备的设计和优化提供了新的研究思路和理论依据。

关 键 词:混合器  食品加工  流场  偏心螺旋转子  有限时间Lyapunov指数  拉格朗日拟序结构  Poincaré截面
收稿时间:2018/5/17 0:00:00
修稿时间:2018/8/31 0:00:00

Analysis on influence of rotor lead and eccentricity on mixing flow field and efficiency of dough mixer
Zhu Xiangzhe,Gao He and Liu Jian.Analysis on influence of rotor lead and eccentricity on mixing flow field and efficiency of dough mixer[J].Transactions of the Chinese Society of Agricultural Engineering,2018,34(20):305-314.
Authors:Zhu Xiangzhe  Gao He and Liu Jian
Institution:School of Mechanical Engineering, Liaoning Shihua University, Fushun 1130011, China,School of Mechanical Engineering, Liaoning Shihua University, Fushun 1130011, China and School of Mechanical Engineering, Liaoning Shihua University, Fushun 1130011, China
Abstract:The chaotic food mixer with an eccentric spiral rotor is a new type of food processing device, in which the food fluids with long molecular chains can not be damaged by high shear stresses, such as traditional twin screw extruders. In fact, the previous researches had demonstrated that the food melt with high viscosity flowing in the food mixer has the nature of chaotic mixing. However, as a dynamic system of flow, the traditional Euler methods is difficult to distinguish the chaotic manifolds, which is a barrier for better understanding the mixing mechanism in the internal mixer. From a new viewpoint of 3D Lagrangian, the objective of our study is to explore the chaotic mixing mechanism in this new kind of food mixer under the disturbance of eccentric spiral rotor, to visually locate the poor and well mixing regions in the mixer and optimize the key geometric parameters of the eccentric spiral rotors. Firstly, a numerical simulation of the three-dimensional flow field in the food mixer is carried out using the mesh superposition technique (MST) and CFD code of Polyflow without considering the re-meshing for the periodical geometric changes. The Carreau-Yasuda constitutive model was used to describe the rheological behavior of the food material. Based on the transient velocity distributions, the finite time Lyapunov exponent (FTLE), Lagrangian coherent structure (LCS) and Poincaré section were calculated to analyze the fluid transport and mixing in the new chaotic food mixer with helical eccentric rotors. The LCS from the ridges of FTLE as a boundary was adopted to reveal the chaotic and regular zones in the mixer. And the particle tracking was used to illustrate the different fluid motions in the flow dynamic system based on the fourth-order Runge-Kutta scheme. Then the effects of rotor eccentric ratio on the chaos scale and particles motions in the regular of the mixer were studied, respectively. Moreover, based on the quantitative mixing measures, such as mixing shear rate, logarithmic of stretching, instantaneous mixing efficiency and average time mixing efficiency, the rotor lead and eccentricity rate were optimized to increase the mixing inefficiency of the chaotic food mixer. The results show that the hyperbolic LCSs divide into two regions with different particle motion characteristics for the food mixer, such as the inner rotary zone and the outer spiral zone. With the increase of rotor eccentric ratio, the strength of chaotic mixing in the outer spiral zone increases and that in the inner rotary zone decreases. When the rotor has little eccentric ratio, the mixing mainly depends on the fluid transport in the inner rotary zone. Then the axial velocity of fluid decreases significantly, but the mixing at radial direction of the inner rotary zone increases. Through optimization of the eccentricity and the lead distance of the eccentric rotor, it can be found that the mixer has relatively higher overall mixing efficiency with the lead of 120 mm and the eccentricity of 0.67, following is the lead of 60 mm and the eccentricity of 0.97, and the mixer has relatively poorer overall mixing efficiency with the lead of 60 mm and the eccentricity of 0.33. This paper has shown that the Lagrangian fresh perspective is more feasible than traditional Euler method in numerically investigate the evolution of two-dimensional mixing performance within a novel mixer. FTLE and LCS are useful tools for analyzing chaotic mixing flow in the mixer. This method provides new research ideas and theoretical basis for the design and optimization of food and other mixed equipment, which provides a better understanding the mixing mechanisms in a flow dynamic system.
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