CFD modeling of liquid-solid fluidized beds of polydisperse struvite crystals

被引:22
作者
Rahaman, Md. Saifur [1 ]
Choudhury, Mahbuboor R. [1 ]
Ramamurthy, Amruthur S. [1 ]
Mavinic, Donald S. [2 ]
Ellis, Naoko [3 ]
Taghipour, Fariborz [3 ]
机构
[1] Concordia Univ, Dept Bldg Civil & Environm Engn, 1455 de Malsonneuve Blvd West,EV 6-139, Montreal, PQ H3G 1M8, Canada
[2] Univ British Columbia, Dept Civil Engn, Pollut Control & Waste Management Grp, 2002-6250 Appl Sci Lane, Vancouver, BC V6T 1Z4, Canada
[3] Univ British Columbia, Dept Chem & Biol Engn, Fluidizat Res Ctr, 227-2360 East Mall, Vancouver, BC V6T 1Z4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Computational fluid dynamics; Modeling; Liquid-solid; Struvite; Polydispersed crystals; Fluidized bed; PILOT-SCALE; PHOSPHORUS RECOVERY; WASTE-WATER; GRANULAR FLOW; CRYSTALLIZATION; SIMULATION; KINETICS; HYDRODYNAMICS; SUPERNATANT; PARTICLES;
D O I
10.1016/j.ijmultiphaseflow.2017.09.011
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
In a liquid-solid fluidized bed crystallization system (having particles of different sizes), two opposite processes (classification and dispersion) influence overall particle size distribution. interactions between these processes make designing crystallizers challenging, as the solid crystals within the bed exhibit some degree of mixing. Therefore, a better understanding of bed expansion and particle mixingisegregation is required to design fluidized bed crystallizers. In this study, a numerical investigation of the hydrodynamics of liquid-solid fluidized beds of polydisperse struvite crystals was thoroughly performed for the first time. This study also tested and validated three established empirical drag law correlations used to explain momentum exchange between solid and liquid phases. Wen and Yu (1966) and Gidaspow (1994) drag law models showed greater predictive power in terms of pressure drop and voidage in the fluidized beds of multi-particle systems. The simulated bed expansion behavior of different sizes of struvite crystals was found to be consistent with experimental results. At steady state, six different size groups of struvite studied in this investigation were found to be classified according to their sizes with limited intermixing between successive layers. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:48 / 61
页数:14
相关论文
共 48 条
[1]   Pilot-scale study of phosphorus recovery through struvite crystallization - examining the process feasibility [J].
Adnan, A ;
Mavinic, DS ;
Koch, FA .
JOURNAL OF ENVIRONMENTAL ENGINEERING AND SCIENCE, 2003, 2 (05) :315-324
[2]   Multiphase CFD modeling: Fluid dynamics aspects in scale-up of a fluidized-bed crystallizer [J].
Al-Rashed, Mohsen ;
Wojcik, Janusz ;
Plewik, Roch ;
Synowiec, Piotr ;
Kus, Agata .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 63 :7-15
[3]   Phosphorus removal from a real anaerobic supernatant by struvite crystallization [J].
Battistoni, P ;
De Angelis, A ;
Pavan, P ;
Prisciandaro, M ;
Cecchi, F .
WATER RESEARCH, 2001, 35 (09) :2167-2178
[4]   Dissolution kinetics of struvite pellets grown in a pilot-scale crystallizer [J].
Bhuiyan, M. I. H. ;
Mavinic, D. S. ;
Beckie, R. D. .
CANADIAN JOURNAL OF CIVIL ENGINEERING, 2009, 36 (03) :550-558
[5]   Nucleation and growth kinetics of struvite in a fluidized bed reactor [J].
Bhuiyan, M. Iqbal H. ;
Mavinic, D. S. ;
Beckie, R. D. .
JOURNAL OF CRYSTAL GROWTH, 2008, 310 (06) :1187-1194
[6]  
BOORAM CV, 1975, T ASAE, V18, P340
[7]  
Bowers KE, 2005, T ASAE, V48, P1217, DOI 10.13031/2013.18504
[8]   CFD modelling of a liquid-solid fluidized bed [J].
Cornelissen, Jack T. ;
Taghipour, Fariborz ;
Escudie, Renaud ;
Ellis, Naoko ;
Grace, John R. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (22) :6334-6348
[9]   Multivariate optimization of phosphate removal and recovery from aqueous solution by struvite crystallization in a fluidized-bed reactor [J].
de Luna, Mark Daniel G. ;
Abarca, Ralf Ruffel M. ;
Su, Chia-Chi ;
Huang, Yao-Hui ;
Lu, Ming-Chun .
DESALINATION AND WATER TREATMENT, 2015, 55 (02) :496-505
[10]   HYDRODYNAMICS OF LIQUID FLUIDIZATION [J].
DIFELICE, R .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (08) :1213-1245