Experimental verification of solid-like and fluid-like states in the homogeneous fluidization regime of Geldart A particles

The mechanisms underlying homogeneous fluidization of Geldart A particles have been debated for decades. Some ascribed the stability to inter-particle forces, while others insisted a purely hydrodynamic explanation. Valverde et al. (2001) fluidized 8.53–μm (i.e., Geldart C) particles by the addition of fumed silica nanoparticles and found that even during homogeneous fluidization both solid-like and fluid-like behavior can be distinguished. However, it is still unclear whether both states exist for true Geldart A particles. In this paper, particulate fluidization characteristics of three typical Geldart A powders were studied by camera recording, electrical capacitance tomography, and pressure fluctuation. For the first time, the existence of both solid-like state dominated by inter-particle forces and fluid-like state by fluid dynamics during homogeneous expansion of Geldart A particles was experimentally verified. Furthermore, the ability and performance of the used measurement techniques to identify di...

[1]  Wuqiang Yang,et al.  Investigation of gas–solid bubbling fluidized beds using ECT with a modified Tikhonov regularization technique , 2018 .

[2]  A. Jaworski,et al.  Comparative study of two non-intrusive measurement methods for bubbling gas-solids fluidized beds: Electrical capacitance tomography and pressure fluctuations , 2017 .

[3]  J. Valverde,et al.  Magnetic stabilization of fluidized beds: Effect of magnetic field orientation , 2017 .

[4]  A. Wachs,et al.  Controlling the Quality of Two-Way Euler/Lagrange Numerical Modeling of Bubbling and Spouted Fluidized Beds Dynamics , 2017 .

[5]  Wuqiang Yang,et al.  Investigation of wetting and drying process in a gas-solid fluidized bed by electrical capacitance tomography and pressure measurement , 2016 .

[6]  Yong Yan,et al.  Non-intrusive measurement and hydrodynamics characterization of gas–solid fluidized beds: a review , 2016 .

[7]  Hongzhong Li,et al.  A transfer coefficient-based structure parameters method for CFD simulation of bubbling fluidized beds , 2016 .

[8]  Peiyuan Liu,et al.  Fine-particle defluidization: Interaction between cohesion, Young׳s modulus and static bed height , 2016 .

[9]  P. C. Sande,et al.  Fine Mesh Computational Fluid Dynamics Study on Gas-Fluidization of Geldart A Particles: Homogeneous to Bubbling Bed , 2016 .

[10]  Zhang Yuli,et al.  Measuring minimum fluidization velocity of Geldart particles by use of electrical capacitance tomography , 2016 .

[11]  JOHNSON MATTHEY,et al.  Industrial Tomography : Systems and Applications ” , 2016 .

[12]  Jingdai Wang,et al.  A CFD study of a bi-disperse gas–solid fluidized bed: Effect of the EMMS sub grid drag correction , 2015 .

[13]  L. Mazzei,et al.  An investigation on the mechanics of homogeneous expansion in gas-fluidized beds , 2015 .

[14]  Jiamin Ye,et al.  Measurement of particle concentration in a Wurster fluidized bed by electrical capacitance tomography sensors , 2014 .

[15]  Sofiane Benyahia,et al.  The effect of cohesive forces on the fluidization of aeratable powders , 2014 .

[16]  Wuqiang Yang,et al.  Investigation on Hydrodynamics of Triple-Bed Combined Circulating Fluidized Bed using Electrostatic Sensor and Electrical Capacitance Tomography , 2013 .

[17]  José Manuel Valverde Millán Fluidization of Fine Powders: Cohesive versus Dynamical Aggregation , 2013 .

[18]  Todd Pugsley,et al.  A critical evaluation of literature correlations for predicting bubble size and velocity in gas–solid fluidized beds , 2011 .

[19]  Barry J. Azzopardi,et al.  Comparison between Electrical Capacitance Tomography and Wire Mesh Sensor Output for Air/Silicone Oil Flow in a Vertical Pipe , 2010 .

[20]  Jam Hans Kuipers,et al.  CFD study of the minimum bubbling velocity of Geldart A particles in gas-fluidized beds , 2010 .

[21]  J. Kuipers,et al.  Coexistence of solidlike and fluidlike states in a deep gas-fluidized bed , 2010 .

[22]  Jam Hans Kuipers,et al.  Why the two-fluid model fails to predict the bed expansion characteristics of Geldart A particles in gas-fluidized beds: A tentative answer , 2009 .

[23]  R. Girimonte,et al.  The minimum bubbling velocity of fluidized beds operating at high temperature , 2009 .

[24]  J.A.M. Kuipers,et al.  Two-fluid modeling of Geldart A particles in gas-fluidized beds , 2008 .

[25]  B. Azzopardi Flow Patterns: Does Gas/Solids Flow Pattern Correspond to Churn Flow in Gas/Liquid Flow , 2008 .

[26]  Jose Manuel Valverde,et al.  Types of gas fluidization of cohesive granular materials. , 2007, Physical review. E, Statistical, nonlinear, and soft matter physics.

[27]  Yung C. Liang,et al.  Hazard of electrostatic generation in a pneumatic conveying system: electrostatic effects on the accuracy of electrical capacitance tomography measurements and generation of spark , 2007 .

[28]  Jose Manuel Valverde,et al.  Effect of vibration on agglomerate particulate fluidization , 2006 .

[29]  J.A.M. Kuipers,et al.  The effects of particle and gas properties on the fluidization of Geldart A particles , 2005 .

[30]  Antonio Castellanos,et al.  The relationship between attractive interparticle forces and bulk behaviour in dry and uncharged fine powders , 2005 .

[31]  Chao Zhu,et al.  Gas fluidization characteristics of nanoparticle agglomerates , 2005 .

[32]  M. Ye Multi-level modeling of dense gas-solid two-phase flows , 2005 .

[33]  J. Kuipers,et al.  Discrete particle simulation of the homogeneous fluidization of Geldart A particles , 2004 .

[34]  Jam Hans Kuipers,et al.  A numerical study of fluidization behavior of Geldart A particles using a discrete particle model , 2004 .

[35]  Sankaran Sundaresan,et al.  INSTABILITIES IN FLUIDIZED BEDS , 2003 .

[36]  P. Mills,et al.  Effect of particle size and interparticle force on the fluidization behavior of gas-fluidized beds. , 2003, Physical review. E, Statistical, nonlinear, and soft matter physics.

[37]  Wen-ching Yang Handbook of Fluidization and Fluid-Particle Systems , 2003 .

[38]  Lihui Peng,et al.  Image reconstruction algorithms for electrical capacitance tomography , 2003 .

[39]  P. Mills,et al.  Experimental study on the dynamics of gas-fluidized beds. , 2003, Physical review. E, Statistical, nonlinear, and soft matter physics.

[40]  Yassir Makkawi,et al.  Fluidization regimes in a conventional fluidized bed characterized by means of electrical capacitance tomography , 2002 .

[41]  Sankaran Sundaresan,et al.  Electrical Capacitance Tomography Measurements on the Pneumatic Conveying of Solids , 2001 .

[42]  Jose Manuel Valverde,et al.  The settling of fine cohesive powders , 2001 .

[43]  J. Valverde,et al.  Self-diffusion in a gas-fluidized bed of fine powder. , 2001, Physical review letters.

[44]  Mark A. Bennett,et al.  Application of capacitance electrical tomography for on-line and off-line analysis of flow pattern in horizontal pipeline of pneumatic conveyer , 2000 .

[45]  Wuqiang Yang,et al.  An image-reconstruction algorithm based on Landweber's iteration method for electrical-capacitance tomography , 1999 .

[46]  Wuqiang Yang,et al.  New AC-based capacitance tomography system , 1999 .

[47]  Antonio F. Fortes,et al.  Particle aggregation and the van der Waals forces in gas-solids fluidization , 1998 .

[48]  Douglas J. Durian,et al.  Particle Motions in a Gas-Fluidized Bed of Sand , 1997 .

[49]  Andrew N. Norris,et al.  Particle granular temperature in gas fluidized beds , 1996 .

[50]  Derek Wilkinson,et al.  Determination of minimum fluidization velocity by pressure fluctuation measurement , 1995 .

[51]  D. Geldart,et al.  Fluidization of FCC powders in the bubble-free regime: effect of types of gases and temperature , 1995 .

[52]  R. Jackson,et al.  The mechanics of gas fluidized beds with an interval of stable fluidization , 1993, Journal of Fluid Mechanics.

[53]  L. G. Gibilaro,et al.  A fully predictive criterion for the transition between particulate and aggregate fluidization , 1984 .

[54]  P. Rowe,et al.  The measurement of emulsion phase voidage in gas fluidized beds of fine powders , 1983 .

[55]  D. Geldart,et al.  Behaviour of gas-fluidized beds of fine powders part III. Effective thermal conductivity of a homogeneously expanded bed , 1980 .

[56]  D. Geldart,et al.  Behaviour of gas-fluidized beds of fine powders part I. Homogeneous expansion , 1980 .

[57]  Sabodh K. Garg,et al.  Dynamics of gas‐fluidized beds , 1975 .

[58]  K. Rietema,et al.  The effect of interparticle forces on the expansion of a homogeneous gas-fluidised bed , 1973 .

[59]  D. Geldart Types of gas fluidization , 1973 .