An experimental assessment of fluid-solid drag models based on the pressure drop in bidisperse fixed beds

被引:5
作者
Marchelli, Filippo [1 ,2 ]
Di Felice, Renzo [1 ]
机构
[1] Univ Genoa, Dept Civil Chem & Environm Engn DICCA, Via allOpera Pia 15a, I-16145 Genoa, Italy
[2] Univ Trento, Dept Civil Environm & Mech Engn DICAM, Via Mesiano 77, I-38123 Trento, Italy
关键词
Fluid-solid momentum exchange; Fluidization; Lattice Boltzmann-based models; Polydispersity; MINIMUM FLUIDIZATION VELOCITY; LATTICE-BOLTZMANN SIMULATION; DIRECT NUMERICAL-SIMULATION; PARTICLE-SIZE DISTRIBUTION; CFD-DEM SIMULATION; PACKED-BEDS; BINARY-MIXTURES; MONO-DISPERSE; FLOW; SEGREGATION;
D O I
10.1016/j.ijmultiphaseflow.2023.104513
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Experimental data on binary fixed beds were gathered from the literature and produced by us through experiments in a vertical column fed with liquid water. Then, we used the fluid pressure drop data to compare the performance of the existing models that can predict the fluid-solid drag force for polydisperse systems. The results show that the models behave quite similarly and do not offer significant advantages compared to the Ergun equation, aside from being able to yield the force values for the different particle types. The accuracy of the predictions does not appear to be influenced by the Reynolds number and the particle diameter ratio but seems generally better for equivolumetric mixtures. This work highlights that more research is needed in this field and provides additional experimental data that were lacking for certain operational conditions and may be useful for future works.
引用
收藏
页数:14
相关论文
共 56 条
[1]   Pairwise-interaction extended point-particle model for particle-laden flows [J].
Akiki, G. ;
Moore, W. C. ;
Balachandar, S. .
JOURNAL OF COMPUTATIONAL PHYSICS, 2017, 351 :329-357
[2]   Assessment of correlations for minimum fluidization velocity of binary mixtures of particles in gas fluidized beds [J].
Alghamdi, Yusif A. ;
Peng, Zhengbiao ;
Almutairi, Zeyad ;
Alibrahim, Hamza ;
Al-Alweet, Fayez M. ;
Moghtaderi, Behdad ;
Doroodchi, Elham .
POWDER TECHNOLOGY, 2021, 394 :1231-1239
[3]   Evaluation of correlations for minimum fluidization velocity (Umf) in gas-solid fluidization [J].
Anantharaman, Aditya ;
Cocco, Ray A. ;
Chew, Jia Wei .
POWDER TECHNOLOGY, 2018, 323 :454-485
[4]   Unresolved CFD-DEM simulation of spherical and ellipsoidal particles in conical and prismatic spouted beds [J].
Atxutegi, A. ;
Kieckhefen, P. ;
Pietsch, S. ;
Aguado, R. ;
Olazar, M. ;
Heinrich, S. .
POWDER TECHNOLOGY, 2021, 389 (389) :493-506
[5]   Drag force of intermediate Reynolds number flow past mono- and bidisperse arrays of spheres [J].
Beetstra, R. ;
van der Hoef, M. A. ;
Kuipers, J. A. M. .
AICHE JOURNAL, 2007, 53 (02) :489-501
[6]   Mixing and segregation in a bidisperse gas-solid fluidised bed: a numerical and experimental study [J].
Bokkers, GA ;
Annaland, MVS ;
Kuipers, JAM .
POWDER TECHNOLOGY, 2004, 140 (03) :176-186
[7]  
Carman P.C., 1937, T I CHEM ENG-LOND, V15, P150
[8]   A semi-empirical model for the drag force and fluid-particle interaction in polydisperse suspensions [J].
Cello, Fernando ;
Di Renzo, Alberto ;
Di Maio, Francesco Paolo .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (10) :3128-3139
[9]   Numerical investigation of the particle circulation characteristics in a tapered fluidized bed [J].
Che, Hanqiao ;
Chen, Tang .
ENGINEERING COMPUTATIONS, 2022, 39 (09) :3296-3319
[10]   Analysis of particle size distribution in municipal wastewaters [J].
Cornacchia, Matteo ;
Moser, Gabriele ;
Saturno, Ezio ;
Trucco, Andrea ;
Costamagna, Paola .
ENVIRONMENTAL TECHNOLOGY & INNOVATION, 2022, 27