Assessment of different methods of analysis to characterise the mixing of shear-thinning fluids in a Kenics KM static mixer using PLIF

被引:37
作者
Alberini, F. [1 ]
Simmons, M. J. H. [1 ]
Ingram, A. [1 ]
Stitt, E. H. [2 ]
机构
[1] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
[2] Johnson Matthey Technol Ctr, Billingham TS23 1LB, Cleveland, England
基金
英国工程与自然科学研究理事会;
关键词
Scale and intensity of segregation; Mixing performance; PLIE; Non-Newtonian fluid blending; Static mixer; NON-NEWTONIAN FLUIDS; PRESSURE-DROP; LAMINAR-FLOW;
D O I
10.1016/j.ces.2014.03.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The performance of Kenics KM static mixers has been determined for the blending of two shear-thinning fluid streams with identical or different rheology. Planar Laser Induced Fluorescence (PLIF) has been used to obtain the concentration distribution at the mixer outlet by doping one fluid stream with fluorescent dye upstream of the mixer inlet. The effect of scale of the static mixer, total flow rate, flow ratio between the fluid streams and inlet configuration have been investigated. The applicability of different methods to characterise mixing performance is examined by comparing conventional mixing measures such as coefficient of variation and maximum striation area against recent alternative methods presented in the literature, such as the areal distribution method developed by Alberini et al. (2014). A method of characterising individual striations by determining their distribution as a function of size and concentration is also presented. These findings illustrate the complexity of information-rich PDF images, and highlight how different methods of analysis may be appropriate given the dependencies of the downstream process. (C) 2014 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY license.
引用
收藏
页码:152 / 169
页数:18
相关论文
共 14 条
[1]  
Adamiak I, 2001, INZ CHEM PROCESOWA, V22, P175
[2]   Use of an Areal Distribution of Mixing Intensity to Describe Blending of Non-Newtonian Fluids in a Kenics KM Static Mixer Using PLIF [J].
Alberini, F. ;
Simmons, M. J. H. ;
Ingram, A. ;
Stitt, E. H. .
AICHE JOURNAL, 2014, 60 (01) :332-342
[3]  
CHANDRA KG, 1992, CHEM ENG SCI, V47, P2097
[4]   MEASURING THE SCALE OF SEGREGATION IN MIXING DATA [J].
Kukukova, Alena ;
Aubin, Joelle ;
Kresta, Suzanne M. .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2011, 89 (05) :1122-1138
[5]   A new definition of mixing and segregation: Three dimensions of a key process variable [J].
Kukukova, Alena ;
Aubin, Joelle ;
Kresta, Suzanne M. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (4A) :633-647
[6]  
Meyer A., 2004, Handbook of Industrial Mixing: Science and Practice, P391, DOI [DOI 10.1002/0471451452.CH7, 10.1002/0471451452, DOI 10.1002/0471451452]
[7]  
Peryt-Stawiarska S, 2011, PRZEM CHEM, V90, P1661
[8]   Fluctuations of the non-Newtonian fluid flow in a Kenics static mixer: An experimental study [J].
Peryt-Stawiarska, Sylwia ;
Jaworski, Zdzislaw .
POLISH JOURNAL OF CHEMICAL TECHNOLOGY, 2008, 10 (03) :35-37
[9]   Development of positron emission particle tracking for studying laminar mixing in Kenics static mixer [J].
Rafiee, Marjan ;
Simmons, Mark J. H. ;
Ingram, Andy ;
Stitt, E. Hugh .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (11) :2106-2113
[10]   Numerical simulation and mixing study of pseudoplastic fluids in an industrial helical static mixer [J].
Rahmani, Ramin K. ;
Keith, Theo G. ;
Ayasoufi, Anahita .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2006, 128 (03) :467-480