CFD analysis of fluidized beds using wastes from post-consumer carton packaging

被引:3
作者
Freitas, T. M. [1 ]
Arrieche, L. S. [1 ]
Ribeiro, D. C. [1 ]
Gidaspow, D. [2 ]
Bacelos, M. S. [1 ]
机构
[1] Univ Fed Espirito Santo, Dept Engn & Tecnol, Programa Posgrad Energia, Rodovia BR 101 Norte,Km 60, BR-29932540 Sao Mateus, ES, Brazil
[2] IIT, Amour Coll Engn, Dept Chem & Biol Engn, Suite 142,Perlstein Hall,10 West 33rd St, Chicago, IL 60616 USA
关键词
Solid waste; Multiphase flow; Fluidization; Computational fluid dynamics; EXPERIMENTAL VALIDATION; REACTION-KINETICS; SIMULATION; REACTOR; HYDRODYNAMICS; PARTICLES; PYROLYSIS; BINARY; SHAPE;
D O I
10.1016/j.cep.2016.12.002
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Fluidized bed reactors can be used for fast pyrolysis of polyethylene-aluminum composite (LOPE/Al) to achieve good gas-solid mixing together with high rates of heat and mass transfer in bed columns. Pyrolysis of waste from post-consumer carton package (i.e., polyethylene-aluminum composite) reduces the manufacturing costs of new packages as it permits to produce them using the recovered aluminum and polyethylene in the process. Therefore, this research aims at modelling and analyzing the gas-solid flow in fluidized beds composed of sand and LOPE/Al mixtures. For all mixtures used, results show that gas-solid flow can be well described by the Eulerian-Eulerian Granular model coupled with the usage of parameterized Syamlal-O'Brien's model for momentum transfer between phases. For bed mixtures with up to 20% LOPE/Al composite, the bed pressure drop can be predicted by the model with an error of less than 18%. In addition, for bed mixtures operating at air velocities higher than 50% minimum fluidization, significant segregation of LOPE/Al was not observed. This result indicates that bed mixtures can achieve a good gas-solid contact in the bubble fluidization regime and can be used as a fluidized bed reactor for pyrolysis of wastes from post-consumer carton packages. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:89 / 100
页数:12
相关论文
共 46 条
[1]   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
[2]   Analysis of reaction kinetics of carton packaging pyrolysis [J].
Alvarenga, L. M. ;
Xavier, T. P. ;
Barrozo, M. A. S. ;
Bacelos, M. S. ;
Lira, T. S. .
CHISA 2012, 2012, 42 :113-122
[3]  
Alvarenga L.M., COMPUTER AIDED CHEM, P180
[4]   Determination of activation energy of pyrolysis of carton packaging wastes and its pure components using thermogravimetry [J].
Alvarenga, Larissa M. ;
Xavier, Thiago P. ;
Barrozo, Marcos Antonio S. ;
Bacelos, Marcelo S. ;
Lira, Taisa S. .
WASTE MANAGEMENT, 2016, 53 :68-75
[5]   Hydrodynamic and solid residence time distribution in a circulating fluidized bed: Experimental and 3D computational study [J].
Andreux, Regis ;
Petit, Geoffrey ;
Hemati, Mehrdji ;
Simonin, Olivier .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2008, 47 (03) :463-473
[6]  
[Anonymous], 1987, US
[7]   On the characterization of size and shape of irregular particles [J].
Bagheri, G. H. ;
Bonadonna, C. ;
Manzella, I. ;
Vonlanthen, P. .
POWDER TECHNOLOGY, 2015, 270 :141-153
[8]   CFD modeling of hydrodynamic and heat transfer in fluidized bed reactors [J].
Behjat, Yaghoub ;
Shahhosseini, Shahrokh ;
Hashemabadi, S. Hassan .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2008, 35 (03) :357-368
[9]   Two- and three-dimensional CFD modeling of Geldart A particles in a thin bubbling fluidized bed: Comparison of turbulence and dispersion coefficients [J].
Chalermsinsuwan, Benjapon ;
Gidaspow, Dimitri ;
Piumsomboon, Pornpote .
CHEMICAL ENGINEERING JOURNAL, 2011, 171 (01) :301-313
[10]   CFD modeling of tapered circulating fluidized bed reactor risers: Hydrodynamic descriptions and chemical reaction responses [J].
Chalermsinsuwan, Benjapon ;
Kuchonthara, Prapan ;
Piumsomboon, Pornpote .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (11) :1144-1160