柔性桨与自浮颗粒协同强化高黏度流体混沌混合

doi:10.3969/j.issn.0438-1157.2013.08.013

化工学报 ›› 2013, Vol. 64 ›› Issue (8): 2794-2800.DOI: 10.3969/j.issn.0438-1157.2013.08.013

柔性桨与自浮颗粒协同强化高黏度流体混沌混合

刘作华¹, 杨鲜艳¹, 谢昭明¹, 刘仁龙¹, 陶长元¹, 王运东²

1. 重庆大学化学化工学院, 重庆 400044;
2. 清华大学化学工程系, 北京 100084

收稿日期:2012-12-16 修回日期:2013-04-02 出版日期:2013-08-05 发布日期:2013-08-05
通讯作者: 刘作华(1973- ),男,博士,副教授。
作者简介:刘作华(1973- ),男,博士,副教授。
基金资助:
国家重点基础研究发展计划项目(2012CDA01203);教育部新世纪优秀人才支持计划项目(NCET-0552);清华大学化学工程联合国家重点实验室开放课题(SKL-ChE-12A02)。

Chaotic mixing performance of high-viscosity fluid synergistically intensified by flexible impeller and floating particles

LIU Zuohua¹, YANG Xianyan¹, XIE Zhaoming¹, LIU Renlong¹, TAO Changyuan¹, WANG Yundong²

1. School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 400044, China;
2. Department of Chemical Engineering, Tsinghua University, Beijing 100084, China

Received:2012-12-16 Revised:2013-04-02 Online:2013-08-05 Published:2013-08-05
Supported by:
supported by the National Basic Research Program of China(2012CDA01203),the New Century Excellent Talents in University(NCET-0552)and the Key Laboratory of Chemical Engineering(SKL-ChE-12A02).

摘要/Abstract

摘要： 高黏度流体混合处于层流状态,存在混沌混合区和隔离区,混沌混合是提高其混合效率的有效方法。为增强高黏度流体的混沌混合,在甘油体系中采用柔性搅拌桨并加入自浮颗粒,实验研究了最大Lyapunov指数(LE_max)随单位体积功耗(P_v)的变化规律。结果表明,只加入固体颗粒对原体系LE_max的影响不大,当P_v=2000 W·m^-3时,使用柔性桨后体系LE_max增加10.29%;柔性桨与固体颗粒协同作用时,可使体系LE_max增加30.86%。在P_v≤2000 W·m^-3时,柔性桨和自浮颗粒协同强化高黏度流体混沌混合的效果最好。

关键词: 柔性搅拌桨, 自浮颗粒, 高黏度流体, 最大Lyapunov指数, 混沌混合

Abstract: There are both a chaotic mixing region and an isolated mixing region for the high-viscosity laminar flow mixing system.Increasing chaotic mixing is the effective method to enhance mixing performance.To obtain good mixing performance in the high viscosity fluid mixing system,flexible impeller together with floating particles were used in the glycerol mixing system.The largest Lyapunov exponent(LE_max)was obtained to study the relationship between chaotic mixing degree and power consumption(P_v).It indicated that only adding the floating particles had no effect on LE_max,but the flexible impeller could contribute to enlarging LE_max.When P_v was 2000 W·m^-3,the LE_max of the primary system could be enlarged by 10.29% while using flexible impeller,and when floating particles and flexible impeller worked together,LE_max could be enlarged by 30.86%.At a low P_v(P_v≤2000 W·m^-3),the chaotic mixing of high-viscosity fluid using floating particles synergistically with flexible impeller was much better than the system using the traditional turbine impeller.

Key words: flexible impeller, floating particle, high-viscosity fluid, largest Lyapunov exponent, chaotic mixing

中图分类号:

TQ027.2

刘作华, 杨鲜艳, 谢昭明, 刘仁龙, 陶长元, 王运东. 柔性桨与自浮颗粒协同强化高黏度流体混沌混合[J]. 化工学报, 2013, 64(8): 2794-2800.

LIU Zuohua, YANG Xianyan, XIE Zhaoming, LIU Renlong, TAO Changyuan, WANG Yundong. Chaotic mixing performance of high-viscosity fluid synergistically intensified by flexible impeller and floating particles[J]. CIESC Journal, 2013, 64(8): 2794-2800.

参考文献 28

[1]	Chen Mei(陈梅),Fan Xijun(范西俊),Dou Mei(窦梅),Wu Jia(吴嘉).Two-dimensional mixing flow field of high viscosity fluid[J].Journal of Chemical Industry and Engineering(China)(化工学报),1994, 45(1):10-16
[2]	Cui Yingning(崔应宁),Wu Dejun(吴德钧),Shi Litian(施力田).Temperature distribution uniformity of high viscosity fluid in a stirred tank[J].Journal of Chemical Industry and Engineering(China)(化工学报),1991,1:25-32
[3]	Lamberto D J,Alvarez M M,Muzzio F J.Experimental and computional investigation of the laminar flow structure in a stirred tank[J].Chemical Engineering Science,1999,54:919-942
[4]	Arratia P E,Lacombe J P,Shinbort T,Muzzio F J. Segregated regions in continuous laminar stirred tank reactors[J].Chemical Engineering Science,2004,59:1481-1490
[5]	Ohuram N,Makino T,Kaise T,Kataoka K.Transition of organized flow of structure in a stirred vessel at low Reynolds number[J].J.Chem.Eng.Jpn.,2003, 36(12):1458-1463
[6]	Aref H,Balachandar S.Chaotic advection in a Stokes flow[J].Phys.Fluids,1986,29:3515-3521
[7]	Arratia P E,Muzzio F J.Planar-induced fluorescence method for analysis of mixing in laminar flows[J].Ind.Eng.Chem.Res.,2004,43:6557-6568
[8]	Alvarez M M,Zalc J M,Shinbort T,Arratia P E,Muzzio F J.Mechanisms of mixing and creation of structure in laminar stirred tanks[J].AIChE Journal,2002,48(10):2135-2148
[9]	Lamberto D J,Muzzio F J,Swanson P D.Using time dependent RPM to enhance mixing in vessels[J].Chemical Engineering Science,1996,51(5):733-741
[10]	Nomura T,Uchida T,Takahashi K.Enhancement of mixing by unsteady agitation of an impeller in an agitated vessel[J].J.Chem.Eng.Jpn.,1997,30(5):875-879
[11]	Gao Dianrong(高殿荣),Guo Mingjie(郭明杰),Li Yan(李岩),Fan Zhuoli(范卓立).PIV research on unsteady rotational speed chaotic mixing[J].Chinese Journal of Mechanical Engineering(机械工程学报),2006,42(8):44-48
[12]	Arratia P E,Kukura J,Lacombe J,Muzzio F J.Mixing of shear-thinning fluids with yields stress in stirred tanks[J].AIChE Journal,2006,52(7):2310-2322
[13]	Karcz J,Cudak M,Szoplik J.Stirring of a liquid in a stirred tank with an eccentrically located impeller[J].Chemical Engineering Science,2005,60:2369-2380
[14]	Liu Zuohua(刘作华),Ning Weizheng(宁伟征),Sun Ruixiang(孙瑞祥),Zhou Xiaoxia(周小霞),Tao Changyuan(陶长元).Fractal flow structure in air jet-stirred reactor with double impeller[J].CIESC Journal(化工学报),2011,62(3):628-635
[15]	Yang Fengling(杨锋苓).Detached eddy simulation and PIV study of the macro-instability in eccentrically stirred tanks.Jinan:Shandong University,2010
[16]	Masiuk S,Rakoczy R.Power consumption,mixing time,heat and mass transfer measurements for liquid vessels that are mixed using reciprocating multiplates agitators[J].Chemical Engineering and Processing,2007,46:89-98
[17]	Hirata Y,Dote T,Yoshioka T.Performance of chaotic mixing caused by reciprocating a disk in a cylindrical vessel[J].Chemical Engineering Research and Design,2007,85(A5):576-582
[18]	Yang Yiwei(杨弋纬),Wang Jiajun(王嘉骏),Gu Xueping(顾雪萍),Feng Lianfang(冯连芳).The application of chaotic mixing in polymer blending[J].Polymer Materials Science and Engineering(高分子材料科学与工程),2012,28(3):186-189
[19]	Li Hongxing(李红星),Wang Jiajun(王嘉骏),Feng Lianfang(冯连芳),Jin Zhijiang(金志江).Research progress of gas dispersion in stirred vessel with medium or high viscosity fluids[J].Chemical Industry and Engineering Progress(化工进展),2012,31(7):1414-1417
[20]	Liu Renlong(刘仁龙),Liao Jun(廖军),Liu Zuohua(刘作华),Chen Nanxiong(陈南雄),Tao Changyuan(陶长元),Wang Yundong(王运东).Kolmogorov entropy of fluid chaotic mixing in eccentric air jet-stirred reactors[J].China Science Paper(中国科技论文),2012,7(6):428-432
[21]	Ning Weizheng(宁伟征).Eccentric jet strengthen fluid chaotic mixing[D].Chongqing:Chongqing University,2012
[22]	Burkett J R,Hight L M,Kenny P,Wilker J J.Oysters produce an organicinorganic adhesive for intertidal reef construction[J].Journal American Chemical Society,2010,132(36):12531-12533
[23]	Lamberto D J,Alvarez M M,Muzzio F J.Computational analysis of regular and chaotic mixing in a stirred tank reactor[J].Chemical Engineering Science,2001,56:4887-4899
[24]	Koji Takahashi,Mitsunori Motoda.Chaotic mixing created by object inserted in a vessel agitated by an impeller[J].Chemical Engineering Research and Design,2009,87:386-390
[25]	Lü Jinhu(吕金虎),Lu Jun'an(陆君安),Chen Shihua(陈士华).Nonlinear Time Series Analysis and Application(混沌时间序列分析及其应用)[M].Wuhan:Wuhan University Press,2005
[26]	Wolf A,Swift J B,Swinney H L,Vastano J A. Determining Lyapunov exponents from a series[J].Physica D,1985,16:285-317
[27]	Fan Yurun(范毓润),Lu Zhumin(卢著敏).Periodic and a periodic-chaotic mixing between eccentric cylinders[J].Journal of Chemical Industry and Engineering(China)(化工学报),2002,53(6):660-663
[28]	Liu Zuohua(刘作华),Zeng Qiqin(曾启琴),Wang Yundong(王运东),Sun Ruixiang(孙瑞祥),Ning Weizheng(宁伟征),Tao Changyuan(陶长元).Study on laminar mixing enhanced by flexible impeller in high viscosity fluid stirred tank[J].China Science Paper(中国科技论文),2012,7:185-189

柔性桨与自浮颗粒协同强化高黏度流体混沌混合

Chaotic mixing performance of high-viscosity fluid synergistically intensified by flexible impeller and floating particles

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