Comparison between 3-D-PTV and 2-D-PIV for determination of hydrodynamics of complex fluids in a stirred vessel

被引:28
作者
Alberini, F. [1 ]
Liu, L. [2 ]
Stitt, E. H. [2 ]
Simmons, M. J. H. [1 ]
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
“创新英国”项目; 英国工程与自然科学研究理事会;
关键词
3-D-PTV; 2-D-PIV; Transitional regime; Turbulent regime; Non-Newtonian fluids; PARTICLE TRACKING VELOCIMETRY; NON-NEWTONIAN FLUIDS; IMAGE VELOCIMETRY; PTV ALGORITHM; PIV; CALIBRATION; CAMERA; FLOW; ACCURACY; 3D-PTV;
D O I
10.1016/j.ces.2017.05.034
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The capabilities of 3-D-Particle Tracking Velocimetry (PTV) to measure flow fields during the blending of Newtonian and non -Newtonian fluids in a standard baffled cylindrical vessel are assessed. The results are benchmarked against conventional 2-D Particle Image Velocimetry (PIV) data. The vessel, of diameter T = 0.19 m, is equipped with a 6-blade down-pumping PBT impeller of diameter, D = 0.5T. Experiments in the low transitional (Re 70), and transitional (Re 1000) regimes have been conducted, using a range of Newtonian and non-Newtonian fluids. Turbulent flow measurements (Re > 20,000) are made using Newtonian fluids. Data from both techniques are compared in terms of average flow field and, where appropriate, turbulent fluctuating velocity components. Particular emphasis is given on how comparisons can be made between the Eulerian Ply data and the Euler-Lagrangian PTV data. The overall results demonstrate the validity of the PTV technique in this application to acquire average flow fields which are in good agreement with PIV. Turbulent flow properties are less well resolved by PTV due in part to the large size of the tracer particle used. Other advantages and limitations of PTV versus Ply are also discussed. Crown Copyright (C) 2017 Published by Elsevier Ltd.
引用
收藏
页码:189 / 203
页数:15
相关论文
共 44 条
[1]   CFD analysis of caverns and pseudo-caverns developed during mixing of non-newtonian fluids [J].
Adams, L. W. ;
Barigou, M. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2007, 85 (A5) :598-604
[2]  
ADRIAN RJ, 1991, ANNU REV FLUID MECH, V23, P261, DOI 10.1146/annurev.fluid.23.1.261
[3]   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
[4]  
Atkinson C., 2013, MEAS SCI TECHNOL, V24
[5]   PIV measurements of flow in an aerated tank stirred by a down- and an up-pumping axial flow impeller [J].
Aubin, J ;
Le Sauze, N ;
Bertrand, J ;
Fletcher, DF ;
Xuereb, C .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2004, 28 (05) :447-456
[6]   The performance of a new PTV algorithm applied in super-resolution PIV [J].
Bastiaans, RJM ;
van der Plas, GAJ ;
Kieft, RN .
EXPERIMENTS IN FLUIDS, 2002, 32 (03) :346-356
[7]   Using positron emission particle tracking (PEPT) to study the turbulent flow in a baffled vessel agitated by a Rushton turbine: Improving data treatment and validation [J].
Chiti, Fabio ;
Bakalis, Serafim ;
Bujalski, Waldemar ;
Barigou, Mostafa ;
Eaglesham, Archie ;
Nienow, Alvin W. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (10A) :1947-1960
[8]   Local gas and liquid phase velocity measurement in a miniature stirred vessel using PIV combined with a new image processing algorithm [J].
Chung, K. H. K. ;
Simmons, M. J. H. ;
Barigou, M. .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2009, 33 (04) :743-753
[9]  
Fangary Y.S., 1999, FLOW STUDIES STIRRED
[10]   Experimental investigation of the flow dynamics of rheologically complex fluids in a Maxblend impeller system using PIV [J].
Fontaine, A. ;
Guntzburger, Y. ;
Bertrand, F. ;
Fradette, L. ;
Heuzey, M. -C. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (01) :7-17