Using Positron Emission Particle Tracking (PEPT) to Study Mixing in Stirred Vessels: Validation and Tackling Unsolved Problems in Opaque Systems

被引:18
作者
Barigou, Mostafa [1 ]
Chiti, Fabio [1 ]
Pianko-Oprych, Paulina [1 ]
Guida, Antonio [1 ]
Adams, Luke [1 ]
Fan, Xianfeng [2 ]
Parker, David J. [2 ]
Nienow, Alvin William [1 ]
机构
[1] Univ Birmingham, Dept Chem Engn, Birmingham B15 2TT, W Midlands, England
[2] Univ Birmingham, Sch Phys & Astron, Birmingham B15 2TT, W Midlands, England
基金
英国工程与自然科学研究理事会;
关键词
PEPT; Liquid Mixing; Solids Distribution; Shear-Thinning Slurry; Lagrangian Data; RUSHTON TURBINE; FLOW; LDA;
D O I
10.1252/jcej.08we262
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Positron emission particle tracking (PEPT) is a new technique allowing the quantitative study of flow phenomena in three dimensions in opaque systems that cannot be studied by techniques based on optical methods such as particle image velocimetry (PIV) or Laser Doppler anemometry (LDA). Here, the technique is initially described along with studies validating the technique, comparing velocity profiles from a Rushton and a pitched blade turbine in turbulent transparent systems from PEPT with PIV and LDA. Subsequently, results are presented showing, for the first time, the spatial distribution of suspended particles of two sizes throughout the vessel; and velocity profiles for the solid and liquid phase in low viscosity and high solid concentration three-phase (s-g-l) systems under fully turbulent conditions. Finally, three-dimensional flow fields, occupancy maps and Poincare maps are presented, again for the first time, arising from the mixing of two different non-Newtonian shear thinning yield stress slurries. Clearly, PEPT offers many possibilities for obtaining quantitative data previously unobtainable for a wide range of important mixing problems relevant to a broad spectrum of the process industries.
引用
收藏
页码:839 / 846
页数:8
相关论文
共 15 条
[1]  
ADAMS L, 2008, P ISMIP 6 NIAG CAN
[2]   Particle tracking in opaque mixing systems: An overview of the capabilities of PET and PEPT [J].
Barigou, M .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A9) :1258-1267
[3]  
BROWN D, 2008, COMMUNICATION
[4]  
Chiti F, 2008, THESIS U BIRMINGHAM
[5]  
DYSTER KN, 1993, CHEM ENG RES DES, V71, P11
[6]  
FANGARY YS, 1999, ICHEME S SER, V146, P23
[7]   Explaining mass transfer observations in multiphase stiffed reactors: particle-liquid slip velocity measurements using PEPT [J].
Fishwick, RP ;
Winterbottom, JM ;
Stitt, EH .
CATALYSIS TODAY, 2003, 79 (1-4) :195-202
[8]   Positron emission particle tracking in a mechanically agitated solid-liquid suspension of coarse particles [J].
Guida, A. ;
Fan, X. ;
Parker, D. J. ;
Nienow, A. W. ;
Barigou, M. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (4A) :421-429
[9]  
GUIDA A, 2008, P 11 INT C MULT FLOW, P99
[10]   ESTIMATION OF CAVERN SIZES IN A SHEAR-THINNING PLASTIC FLUID AGITATED BY A RUSHTON TURBINE BASED ON LDA MEASUREMENTS [J].
HIRATA, Y ;
NIENOW, AW ;
MOORE, IPT .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1994, 27 (02) :235-237